WO2010092684A1 - Operating gas circulation type engine - Google Patents

Operating gas circulation type engine Download PDF

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Publication number
WO2010092684A1
WO2010092684A1 PCT/JP2009/052431 JP2009052431W WO2010092684A1 WO 2010092684 A1 WO2010092684 A1 WO 2010092684A1 JP 2009052431 W JP2009052431 W JP 2009052431W WO 2010092684 A1 WO2010092684 A1 WO 2010092684A1
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WO
WIPO (PCT)
Prior art keywords
condensed water
working gas
pumping
gas circulation
amount
Prior art date
Application number
PCT/JP2009/052431
Other languages
French (fr)
Japanese (ja)
Inventor
享 加藤
澤田 大作
黒木 錬太郎
Original Assignee
トヨタ自動車株式会社
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Application filed by トヨタ自動車株式会社 filed Critical トヨタ自動車株式会社
Priority to PCT/JP2009/052431 priority Critical patent/WO2010092684A1/en
Priority to JP2010550377A priority patent/JPWO2010092684A1/en
Publication of WO2010092684A1 publication Critical patent/WO2010092684A1/en

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M21/00Apparatus for supplying engines with non-liquid fuels, e.g. gaseous fuels stored in liquid form
    • F02M21/02Apparatus for supplying engines with non-liquid fuels, e.g. gaseous fuels stored in liquid form for gaseous fuels
    • F02M21/0218Details on the gaseous fuel supply system, e.g. tanks, valves, pipes, pumps, rails, injectors or mixers
    • F02M21/0227Means to treat or clean gaseous fuels or fuel systems, e.g. removal of tar, cracking, reforming or enriching
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N5/00Exhaust or silencing apparatus combined or associated with devices profiting by exhaust energy
    • F01N5/02Exhaust or silencing apparatus combined or associated with devices profiting by exhaust energy the devices using heat
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02DCONTROLLING COMBUSTION ENGINES
    • F02D19/00Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures
    • F02D19/12Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures peculiar to engines working with non-fuel substances or with anti-knock agents, e.g. with anti-knock fuel
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M21/00Apparatus for supplying engines with non-liquid fuels, e.g. gaseous fuels stored in liquid form
    • F02M21/02Apparatus for supplying engines with non-liquid fuels, e.g. gaseous fuels stored in liquid form for gaseous fuels
    • F02M21/0203Apparatus for supplying engines with non-liquid fuels, e.g. gaseous fuels stored in liquid form for gaseous fuels characterised by the type of gaseous fuel
    • F02M21/0206Non-hydrocarbon fuels, e.g. hydrogen, ammonia or carbon monoxide
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M25/00Engine-pertinent apparatus for adding non-fuel substances or small quantities of secondary fuel to combustion-air, main fuel or fuel-air mixture
    • F02M25/022Adding fuel and water emulsion, water or steam
    • F02M25/0221Details of the water supply system, e.g. pumps or arrangement of valves
    • F02M25/0222Water recovery or storage
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M25/00Engine-pertinent apparatus for adding non-fuel substances or small quantities of secondary fuel to combustion-air, main fuel or fuel-air mixture
    • F02M25/022Adding fuel and water emulsion, water or steam
    • F02M25/032Producing and adding steam
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M26/00Engine-pertinent apparatus for adding exhaust gases to combustion-air, main fuel or fuel-air mixture, e.g. by exhaust gas recirculation [EGR] systems
    • F02M26/13Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories
    • F02M26/22Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories with coolers in the recirculation passage
    • F02M26/23Layout, e.g. schematics
    • F02M26/28Layout, e.g. schematics with liquid-cooled heat exchangers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M26/00Engine-pertinent apparatus for adding exhaust gases to combustion-air, main fuel or fuel-air mixture, e.g. by exhaust gas recirculation [EGR] systems
    • F02M26/13Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories
    • F02M26/35Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories with means for cleaning or treating the recirculated gases, e.g. catalysts, condensate traps, particle filters or heaters
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M26/00Engine-pertinent apparatus for adding exhaust gases to combustion-air, main fuel or fuel-air mixture, e.g. by exhaust gas recirculation [EGR] systems
    • F02M26/13Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories
    • F02M26/36Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories with means for adding fluids other than exhaust gas to the recirculation passage; with reformers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2240/00Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
    • F01N2240/02Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being a heat exchanger
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M21/00Apparatus for supplying engines with non-liquid fuels, e.g. gaseous fuels stored in liquid form
    • F02M21/02Apparatus for supplying engines with non-liquid fuels, e.g. gaseous fuels stored in liquid form for gaseous fuels
    • F02M21/0218Details on the gaseous fuel supply system, e.g. tanks, valves, pipes, pumps, rails, injectors or mixers
    • F02M21/0248Injectors
    • F02M21/0275Injectors for in-cylinder direct injection, e.g. injector combined with spark plug
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/30Use of alternative fuels, e.g. biofuels

Definitions

  • the present invention relates to a working gas circulation engine, and more particularly to a working gas circulation engine in which working gas contained in exhaust gas is circulated from the exhaust side to the intake side of the combustion chamber and can be supplied to the combustion chamber again.
  • a working gas circulation engine that is a so-called closed-cycle engine that can circulate the working gas contained in the exhaust gas from the exhaust side of the combustion chamber to the intake side and supply it again to the combustion chamber.
  • Such a working gas circulation engine has a combustion chamber to which oxygen as an oxidant, hydrogen as a fuel, and a working gas having a higher specific heat ratio than air are supplied, and the working gas is sucked from the exhaust side of the combustion chamber.
  • a circulation path that can be circulated to the combustion chamber and re-supplied to the combustion chamber.
  • the working gas is thermally expanded in the combustion chamber as the hydrogen burns, generating power and releasing the working gas to the atmosphere. Without being supplied again to the combustion chamber via the circulation path.
  • a hydrogen engine disclosed in Patent Document 1 below As a conventional working gas circulation engine, for example, a hydrogen engine disclosed in Patent Document 1 below is known.
  • oxygen and hydrogen are supplied to a combustion chamber, and argon is circulated as a working gas to increase thermal efficiency, for example, composed of a monoatomic gas and having a higher specific heat ratio than air.
  • argon is thermally expanded by combustion of hydrogen in a combustion chamber, and thereby a piston is pushed down to generate power.
  • the hydrogen engine described in Patent Document 1 as a conventional working gas circulation engine is a molecule composed of three atoms (triatomic molecules), which liquefies water vapor having a smaller specific heat ratio than argon and removes it as condensed water.
  • an object of the present invention is to provide a working gas circulation engine capable of appropriately treating condensed water.
  • a working gas circulation engine is supplied with an oxidizing agent, a fuel that generates water vapor by combustion with the oxidizing agent, and a working gas having a higher specific heat ratio than air,
  • a circulation path that can be circulated from the exhaust side to the intake side of the combustion chamber and re-supplied to the combustion chamber, and a condensing means that is provided in the circulation path and condenses the water vapor contained in the exhaust gas into condensed water.
  • the condensed water storage means capable of storing the condensed water, the pressure feeding means for pumping the condensed water stored in the condensed water storage means at a pressure higher than the atmospheric pressure, and the condensation pumped by the pressure feeding means
  • the oxidant may be oxygen
  • the fuel may be hydrogen
  • the evaporation means evaporates the condensed water by exhaust heat of the exhaust gas upstream of the condensing means with respect to the circulation direction of the working gas circulating in the circulation path.
  • the pressure feeding means is provided in a condensed water path connecting the condensed water storage means and the evaporation means so that the condensed water can flow, and the condensed water path is provided in the condensed water path.
  • You may comprise so that it may have the pump which pressurizes the said condensed water of a path
  • the pressure feeding unit connects the condensed water storage unit and the evaporation unit so that the condensed water can flow, and a space portion for storing the condensed water is sealed.
  • a condensed water path that communicates with the circulation path via the condensed water storage means, and pressurizes the condensed water in the condensed water path with a pressure of gas in the circulation path higher than atmospheric pressure to store the condensed water. You may comprise so that it pumps from the means side to the said evaporation means side.
  • the pressure feeding means is branched from the circulation path, is provided with working gas storage means for storing the relatively high pressure working gas, the working gas storage means, and the circulation path. Adjusting means for adjusting the inflow and outflow of the working gas between them.
  • the working gas circulation engine may be configured to include a pumping amount control unit that controls a pumping amount of the condensed water by the pumping unit based on a generation amount of the condensed water.
  • the pumping amount control means may control the pumping amount so that the pumping amount becomes equal to the generated amount.
  • the working gas circulation engine may further include a flow rate detection unit that detects a flow rate of the condensed water to the condensed water storage unit, and the pumping amount control unit may detect a flow rate of the condensed water detected by the flow rate detection unit.
  • the pumping amount may be controlled based on the above.
  • the working gas circulation engine may further include a water level detection unit that detects a level of the condensed water stored in the condensed water storage unit, and the pumping amount control unit may detect the condensation detected by the water level detection unit. The pumping amount may be controlled based on the water level.
  • the pumping amount control means may be configured to control the pumping amount based on a supply amount of the oxidant or the fuel supplied to the combustion chamber.
  • the pumping amount control means may be configured to control the pumping amount of the condensed water based on the engine load and the engine speed.
  • the working gas circulation engine may be configured to include waste heat recovery means for recovering the energy of water vapor generated by evaporating the condensed water by the evaporation means as kinetic energy.
  • the temperature detection means for detecting the temperature of the condensed water stored in the condensed water storage means, and the temperature detected by the temperature detection means is less than or equal to a preset predetermined temperature. In some cases, it may be configured to include heat transfer means for moving the heat of water vapor through the waste heat recovery means to the condensed water stored in the condensed water storage means.
  • the working gas circulation engine further includes a water level detection unit that detects a level of the condensed water stored in the condensed water storage unit, and the heat transfer unit has a water level detected by the water level detection unit in advance. When the water level is equal to or lower than a predetermined water level, water vapor that has passed through the waste heat recovery means may be introduced into the condensed water stored in the condensed water storage means.
  • the condensed water can be appropriately processed.
  • FIG. 1 is a schematic configuration diagram of a working gas circulation engine according to Embodiment 1 of the present invention.
  • FIG. 2 is a schematic configuration diagram of a working gas circulation engine according to Modification 1 of the present invention.
  • FIG. 3 is a schematic configuration diagram of a working gas circulation engine according to the second embodiment of the present invention.
  • FIG. 4 is a schematic configuration diagram of a working gas circulation engine according to Modification 2 of the present invention.
  • FIG. 5 is a schematic configuration diagram of a working gas circulation engine according to the third embodiment of the present invention.
  • FIG. 6 is a flowchart for explaining the control of the pumping amount of the working gas circulation engine according to the third embodiment of the present invention.
  • FIG. 1 is a schematic configuration diagram of a working gas circulation engine according to Embodiment 1 of the present invention.
  • FIG. 2 is a schematic configuration diagram of a working gas circulation engine according to Modification 1 of the present invention.
  • FIG. 3 is a schematic configuration diagram of a working gas circulation engine according to
  • FIG. 7 is a schematic schematic configuration diagram of a working gas circulation engine according to Embodiment 4 of the present invention.
  • FIG. 8 is a diagram showing a pressure feed amount map of the working gas circulation engine according to the fourth embodiment of the present invention.
  • FIG. 9 is a flowchart for explaining the control of the pumping amount of the working gas circulation engine according to the fourth embodiment of the present invention.
  • FIG. 10 is a schematic schematic configuration diagram of a working gas circulation engine according to the fifth embodiment of the present invention.
  • FIG. 11 is a diagram showing a pressure feed amount map of the working gas circulation engine according to the fifth embodiment of the present invention.
  • FIG. 12 is a diagram showing a response delay time map of the working gas circulation engine according to the fifth embodiment of the present invention.
  • FIG. 13 is a flowchart for explaining the pressure feed amount control of the working gas circulation engine according to the fifth embodiment of the present invention.
  • FIG. 14 is a schematic configuration diagram of a working gas circulation engine according to Modification 3 of the present invention.
  • FIG. 15 is a schematic configuration diagram of a working gas circulation engine according to Embodiment 6 of the present invention.
  • FIG. 16 is a schematic schematic configuration diagram of a working gas circulation engine according to a seventh embodiment of the present invention.
  • FIG. 17 is a flowchart for explaining condensate temperature control of the working gas circulation engine according to the seventh embodiment of the present invention.
  • FIG. 18 is a schematic schematic configuration diagram of a working gas circulation engine according to an eighth embodiment of the present invention.
  • FIG. 19 is a flowchart illustrating condensate temperature / water level control of the working gas circulation engine according to the eighth embodiment of the present invention.
  • FIG. 20 is a schematic schematic configuration diagram of a working gas circulation engine according to Modification 4 of the present invention.
  • (Embodiment 1) 1 is a schematic schematic configuration diagram of a working gas circulation engine according to Embodiment 1 of the present invention
  • FIG. 2 is a schematic schematic configuration diagram of a working gas circulation engine according to Modification 1 of the present invention. is there.
  • the working gas circulation engine 1 of the present embodiment includes a combustion chamber CC to which an oxidant, fuel, and a working gas that generates power accompanying combustion of the fuel are supplied, and the combustion chamber CC.
  • a so-called closed cycle engine configured to supply the working gas to the combustion chamber CC again through the circulation path 20 without being released to the atmosphere. It is.
  • the working gas circulation engine 1 burns fuel in a combustion chamber CC and generates power by thermally expanding the working gas as the fuel burns.
  • the working gas circulation engine 1 includes an engine body 10 in which a combustion chamber CC is formed, a circulation path 20 that connects the intake side and the exhaust side of the combustion chamber CC, and an oxidant supply that supplies an oxidant to the combustion chamber CC.
  • a device 30, a fuel supply device 40 that supplies fuel to the combustion chamber CC, and an electronic control unit (ECU) 50 that controls each part of the working gas circulation engine 1 are provided.
  • the combustion chamber CC and the circulation path 20 of the engine body 10 are both filled with working gas, and the working gas circulates between the combustion chamber CC and the circulation path 20. 1 shows only one cylinder, the working gas circulation engine 1 of the present invention is not limited to this, and a multi-cylinder engine body 10 can also be applied.
  • the combustion chamber CC of the present embodiment is formed in the engine body 10.
  • the combustion chamber CC of the engine body 10 is supplied with an oxidant, a fuel that generates water vapor by combustion with the oxidant, and a working gas. As the exhaust gas after combustion, water vapor and working gas can be exhausted.
  • the engine body 10 includes a cylinder head 11, a cylinder block 12, and a piston 13 that form a combustion chamber CC.
  • the piston 13 is connected to the crankshaft 19 via the connecting rod 14 and is disposed so as to be able to reciprocate in a space defined between the recess 11 a on the lower surface of the cylinder head 11 and the cylinder bore 12 a of the cylinder block 12.
  • the combustion chamber CC is configured by a space surrounded by the wall surface of the recess 11 a of the cylinder head 11, the wall surface of the cylinder bore 12 a, and the top surface 13 a of the piston 13.
  • the engine body 10 has a cylinder head 11 formed with an intake port 11b and an exhaust port 11c. Both the intake port 11b and the exhaust port 11c form part of the circulation path 20. One end of each of the intake port 11b and the exhaust port 11c opens into the combustion chamber CC.
  • the engine main body 10 is provided with an intake valve 15 at an opening portion of the intake port 11b on the combustion chamber CC side.
  • the intake valve 15 opens the opening on the combustion chamber CC side of the intake port 11b when the valve is opened, and closes the opening on the combustion chamber CC side of the intake port 11b when the valve is closed.
  • the engine body 10 is provided with an exhaust valve 16 at an opening portion of the exhaust port 11c on the combustion chamber CC side.
  • the exhaust valve 16 opens the opening on the combustion chamber CC side of the exhaust port 11c when the valve is opened, and closes the opening on the combustion chamber CC side of the exhaust port 11c when the valve is closed.
  • the intake valve 15 and the exhaust valve 16 for example, there are those that are opened and closed in accordance with the rotation of a camshaft (not shown) and the elastic force of an elastic member (string spring).
  • a camshaft is interlocked with the rotation of the crankshaft 19 by interposing a power transmission mechanism composed of a chain, a sprocket, etc. between the camshaft and the crankshaft 19, Open / close drive is performed at a preset opening / closing timing.
  • the engine body 10 may include a variable valve mechanism such as a so-called variable valve timing & lift mechanism that can change the opening / closing timing and lift amount of the intake valve 15 and the exhaust valve 16, thereby The opening / closing timing and lift amount of the valve 15 and the exhaust valve 16 can be changed to suitable ones according to the operating conditions. Furthermore, the engine body 10 is applied with a so-called electromagnetically driven valve that opens and closes the intake valve 15 and the exhaust valve 16 using electromagnetic force in order to obtain the same effect as the variable valve mechanism. Also good.
  • a variable valve mechanism such as a so-called variable valve timing & lift mechanism that can change the opening / closing timing and lift amount of the intake valve 15 and the exhaust valve 16, thereby The opening / closing timing and lift amount of the valve 15 and the exhaust valve 16 can be changed to suitable ones according to the operating conditions.
  • the engine body 10 is applied with a so-called electromagnetically driven valve that opens and closes the intake valve 15 and the exhaust valve 16 using electromagnetic force in order to obtain the same effect as the variable valve mechanism. Also
  • the engine body 10 has an intake pipe 17 connected to an opening of the intake port 11b opposite to the combustion chamber CC side, and an exhaust pipe 18 connected to an opening of the exhaust port 11c opposite to the combustion chamber CC side. It is connected.
  • the intake pipe 17 and the exhaust pipe 18 together form part of the circulation path 20.
  • the intake pipe 17 is formed in a cylindrical shape and allows fluid to pass therethrough.
  • the combustion chamber CC contains argon (Ar) as a working gas and oxygen (O 2 ) as an oxidant. It is an intake passage for supplying. In other words, when the intake valve 15 is opened, the oxidant and the working gas are supplied (intake) from the intake pipe 17 to the combustion chamber CC via the intake port 11b.
  • the exhaust pipe 18 is formed in a cylindrical shape so that a fluid can pass therethrough.
  • the exhaust pipe 18 serves as a working gas from the combustion chamber CC.
  • This is an exhaust passage for discharging argon (Ar) and water vapor (H 2 O). That is, when the exhaust valve 16 is opened, the combustion chamber CC exhausts water vapor and working gas to the exhaust pipe 18 through the exhaust port 11c as exhaust gas after combustion of fuel.
  • the circulation path 20 can circulate the working gas contained in the exhaust gas exhausted to the exhaust pipe 18 from the exhaust side to the intake side of the combustion chamber CC and supply it to the combustion chamber CC again.
  • the circulation path 20 includes the intake port 11b and the exhaust port 11c described above, and a circulation passage 21 that connects the other end of the intake port 11b and the other end of the exhaust port 11c.
  • the circulation path 20 and the combustion chamber CC basically form a closed space.
  • the circulation passage 21 is formed in a cylindrical shape and allows fluid to pass therethrough.
  • the intake pipe 17 and the exhaust pipe 18 described above form part of the circulation passage 21.
  • This working gas circulation engine 1 is filled with working gas in a closed space composed of the circulation path 20 and the combustion chamber CC.
  • the working gas circulation engine 1 circulates the working gas through the intake pipe 17 of the circulation path 20, the intake port 11b into the combustion chamber CC, the exhaust port 11c of the circulation path 20 from the combustion chamber CC, the exhaust pipe 18, and the exhaust gas.
  • the air is circulated from the port 11c and the exhaust pipe 18 to the intake pipe 17 and the intake port 11b through the circulation passage 21 again. That is, the circulation path 20 connects the intake side (intake port 11b side) and the exhaust side (exhaust port 11c side) of the combustion chamber CC outside the combustion chamber CC, and again without releasing the working gas to the atmosphere. Supply to combustion chamber CC.
  • the circulator 20 has both ends communicating with the combustion chamber CC, an exhaust gas containing water vapor and working gas flows from one end into the combustion chamber CC, and an oxidant that the combustion chamber CC takes in from the other end. And the working gas can flow out to the combustion chamber CC.
  • the working gas circulation engine 1 when the intake valve 15 is opened, the oxidant and working gas in the circulation passage 21 are supplied to the combustion chamber CC via the intake pipe 17 and the intake port 11b. Further, in the working gas circulation engine 1, when the exhaust valve 16 is opened, the exhaust gas in the combustion chamber CC is discharged to the circulation passage 21 through the exhaust port 11c and the exhaust pipe 18.
  • the circulation path 21 of the circulation path 20 includes, for example, a first circulation path 21a, a second circulation path 21b, and a third circulation path 21c.
  • the first circulation passage 21 a connects the other end of the intake port 11 b and a discharge port 32 a of an oxidant supply means 32 described later in the oxidant supply device 30.
  • the second circulation passage 21b connects the other end of the exhaust port 11c and an exhaust gas inlet 60a of a condenser 60 as a condensing means of the present invention described later.
  • the heat exchanger 90 as an evaporation means of the present invention described later is provided in the second circulation passage 21b.
  • the third circulation passage 21 c connects the working gas discharge port 60 b of the condenser 60 and the working gas introduction port 32 b of the oxidant supply means 32.
  • the intake pipe 17 described above forms part of the first circulation passage 21a, while the exhaust pipe 18 forms part of the second circulation passage 21b.
  • a gas having a higher specific heat ratio than air is used as the working gas filled in the closed space formed by the circulation path 20 and the combustion chamber CC.
  • the working gas for example, a monoatomic gas is used.
  • the working gas of the present embodiment has a higher specific heat ratio than air, and for example, a rare gas such as argon (Ar) or helium (He) that is a monoatomic gas is used.
  • the working gas is described as using argon (Ar) as described above.
  • the oxidant supply device 30 supplies oxidant to the combustion chamber CC via the intake pipe 17 and the intake port 11b of the circulation path 20, and includes an oxidant storage tank 31, an oxidant supply means 32, an oxidant.
  • a supply passage 33, a regulator 34, and an oxidant flow meter 35 are included.
  • the oxidant storage tank 31 stores the oxidant in a high pressure state.
  • the oxidant supply means 32 supplies the oxidant stored in the oxidant storage tank 31 to the circulation passage 21.
  • the oxidant supply passage 33 connects the oxidant storage tank 31 and the oxidant supply means 32.
  • the regulator 34 and the oxidant flow meter 35 are provided on the oxidant supply passage 33.
  • the oxidant supply means 32 of the present embodiment the oxidant flowing from the oxidant supply passage 33 and the working gas flowing from the circulation passage 21 through the working gas introduction port 32b are mixed, An oxidant mixing means is used for flowing the mixed oxidant and working gas from the discharge port 32a to the downstream side of the circulation passage 21 (the intake port 11b side). Therefore, the oxidant supply device 30 of the present embodiment can not only supply the oxidant to the circulation passage 21 but also mix it with the working gas passing through the circulation passage 21 and send it to the circulation passage 21. As a result, the oxidant is supplied to the combustion chamber CC together with the working gas via the intake port 11b when the intake valve 15 is opened.
  • the oxidant supply means 32 is not limited to the above-described configuration, and is controlled by the electronic control unit 50 so that the oxidant is injected and supplied to the circulation path 20, for example, the circulation path 21 or the intake port 11b.
  • An agent injection valve may be used.
  • the regulator 34 adjusts the pressure downstream of the regulator 34 in the oxidant supply passage 33 (on the engine body 10 side) to a target pressure in accordance with a command from the electronic control unit 50. In other words, the regulator 34 controls the flow rate of the oxidant in the oxidant supply passage 33.
  • the oxidant flow meter 35 is a means for measuring the flow rate of the oxidant in the oxidant supply passage 33 and measures the flow rate of the oxidant adjusted by the regulator 34. The measurement signal of the oxidant flow meter 35 is transmitted to the electronic control unit 50.
  • oxygen (O 2 ) is used as the oxidant supplied by the oxidant supply device 30 as described above. That is, the oxidant storage tank 31 of the present embodiment stores oxygen as an oxidant at a high pressure of about 70 MPa, for example, and the oxidant supply means 32 supplies this high-pressure oxygen (O 2 ) to the circulation passage 21. .
  • the fuel supply device 40 supplies fuel to the combustion chamber CC, and includes a fuel storage tank 41, a fuel injection means 42, a fuel supply passage 43, a regulator 44, a fuel flow meter 45, a surge tank 46, and the like. It is comprised including.
  • the fuel storage tank 41 stores fuel in a high pressure state.
  • the fuel injection means 42 injects the fuel stored in the fuel storage tank 41 into the combustion chamber CC.
  • the fuel supply passage 43 connects the fuel storage tank 41 and the fuel injection means 42.
  • the regulator 44, the fuel flow meter 45, and the surge tank 46 are provided on the fuel supply passage 43.
  • the regulator 44, the fuel flow meter 45, and the surge tank 46 are directed from the upstream side (the fuel storage tank 41 side) to the downstream side (the fuel injection means 42 side) with respect to the fuel supply direction in the fuel supply passage 43.
  • the regulator 44, the fuel flow meter 45, and the surge tank 46 are provided in this order.
  • the fuel injection means 42 of the present embodiment is provided in the cylinder head 11 so that the fuel can be directly injected into the combustion chamber CC.
  • the fuel injection means 42 is a so-called fuel injection valve controlled by the electronic control unit 50.
  • the electronic control unit 50 for example, the fuel injection timing or the injection amount, in other words, the supply according to the driving state (requested engine load) required by the driver for the working gas circulation engine 1 and the operating state such as the engine speed. Control the amount.
  • the driving force (requested engine load) required by the driver for the working gas circulation engine 1 is set based on, for example, the accelerator opening degree of the vehicle on which the working gas circulation engine 1 is mounted.
  • the electronic control unit 50 can obtain the driving force required for the working gas circulation engine 1 at the current engine speed based on the engine speed of the working gas circulation engine 1 and the requested driving force. Determine how much hydrogen can be supplied.
  • the engine speed of the working gas circulation engine 1 can be detected based on, for example, a crank angle sensor 51.
  • the crank angle sensor 51 detects, for example, a crank angle that is a rotation angle of the crankshaft 19 of the working gas circulation engine 1.
  • the crank angle sensor 51 transmits a detection signal to the electronic control unit 50.
  • the electronic control unit 50 determines an intake stroke, a compression stroke, an expansion stroke, and an exhaust stroke in each cylinder based on the detected crank angle, and the engine speed (rpm) as the rotational speed of the working gas circulation engine 1. ) Is calculated.
  • the engine speed corresponds to the rotational speed of the crankshaft 19 in other words, and if the rotational speed of the crankshaft 19 increases, the engine rotational speed that is the rotational speed of the crankshaft 19 also increases.
  • the regulator 44 adjusts the pressure downstream of the regulator 44 in the fuel supply passage 43 (on the fuel flow meter 45 and surge tank 46 side) to the set pressure.
  • the fuel flow meter 45 is a means for measuring the fuel flow rate in the fuel supply passage 43 and measures the fuel flow rate adjusted by the regulator 44.
  • the measurement signal of the fuel flow meter 45 is transmitted to the electronic control device 50.
  • the surge tank 46 is intended to reduce pulsation generated in the fuel supply passage 43 when fuel is injected by the fuel injection means 42.
  • the fuel supplied by the fuel supply device 40 one that generates water vapor by combustion is used, and in the present embodiment, hydrogen (H 2 ) is used as described above. That is, the fuel storage tank 41 of the present embodiment stores hydrogen as fuel at a high pressure of, for example, about 70 MPa, and the fuel injection means 42 injects this high pressure hydrogen into the combustion chamber CC.
  • the working gas circulation engine 1 of this embodiment is exemplified as one in which hydrogen as a fuel and oxygen as an oxidant are supplied into the combustion chamber CC to diffuse and burn hydrogen. That is, the working gas circulation engine 1 configured as described above includes high-pressure hydrogen (H 2 ) in high-temperature compressed gas (oxygen (O 2 ) and argon (Ar)) formed in the combustion chamber CC. ) Is self-ignited, and hydrogen and compressed gas (oxygen) are combusted while being diffusely mixed.
  • hydrogen and oxygen (O 2 ) react in the combustion chamber CC to generate water vapor (H 2 O), and argon (Ar) having a large specific heat ratio.
  • the piston 13 is pushed down by the diffusion combustion of hydrogen and the thermal expansion of argon, thereby generating power.
  • the working gas circulation engine 1 opens the exhaust valve 16 when the combustion of hydrogen and the thermal expansion of argon are completed (for example, when the piston 13 is located near the bottom dead center). Accordingly, exhaust gas containing water vapor and argon is discharged from the combustion chamber CC to the exhaust pipe 18 through the exhaust port 11c.
  • the argon in the exhaust gas discharged is circulated from the exhaust side to the intake side of the combustion chamber CC via the circulation path 20 and supplied to the combustion chamber CC from the intake side again in order to increase the thermal efficiency of the engine body 10. There is a need to.
  • this working gas circulation engine 1 is provided with a means on the circulation path 20 for removing water vapor contained in the exhaust gas.
  • the working gas circulation engine 1 includes a condenser 60 as a condensing means as means for removing water vapor contained in the exhaust gas flowing through the circulation path 20.
  • the working gas circulation engine 1 further includes a cooling water circulation path 61, a cooling water pump 62, and a radiator 63.
  • the condenser 60 is provided in the circulation path 20 to condense the water vapor contained in the exhaust gas into condensed water (H 2 O).
  • the condenser 60 is provided between the second circulation passage 21b and the third circulation passage 21c on the circulation passage 21. That is, the condenser 60 is provided on the exhaust side of the oxidant supply means 32 on the circulation passage 21.
  • the condenser 60 is connected so that the cooling water circulation path 61 passes through the inside.
  • the cooling water circulation path 61 circulates cooling water as a heat exchange medium through the condenser 60, and the cooling water can flow.
  • the cooling water circulation path 61 is a closed annular path and is filled with cooling water.
  • the cooling water pump 62 is provided on the cooling water circulation path 61, and the cooling water in the cooling water circulation path 61 can be circulated through the cooling water circulation path 61 by driving the cooling water pump 62.
  • the radiator 63 is provided on the cooling water circulation path 61 and can cool the cooling water circulating in the cooling water circulation path 61.
  • the radiator 63 of the present embodiment acts as a heat radiating means, and can cool the cooling water circulating through the cooling water circulation path 61 by the traveling wind of the vehicle on which the working gas circulation engine 1 is mounted.
  • the condenser 60 circulates through the cooling water circulation path 61 and is circulated and supplied with the cooling water cooled by the radiator 63, thereby heat-exchanging the cooling water and the exhaust gas flowing through the circulation path 20.
  • water vapor (H 2 O) contained in the exhaust gas is liquefied and condensed to be condensed water and separated from the exhaust gas. That is, the condenser 60 can separate the exhaust gas into argon and condensed water.
  • the cooling water whose temperature has risen due to heat exchange by exchanging heat with the exhaust gas in the circulation path 20 in the condenser 60 is radiated when circulating through the cooling water circulation path 61 and again passing through the radiator 63. As a result, the temperature is lowered, that is, cooled. That is, the cooling water circulating in the cooling water circulation path 61 radiates the heat absorbed by the condenser 60 by the radiator 63.
  • the condensed water separated by the condenser 60 is discharged to the condensed water discharge passage 64 through the condensed water discharge port 60c of the condenser 60, and is outside the system of the circulation path 20, here as condensed water storage means described later.
  • the condensed water storage tank 70 is discharged.
  • the condenser 60 and the radiator 63 are configured to reach a temperature at which the water vapor in the exhaust gas is liquefied and condensed when the hottest exhaust gas that can be assumed during engine operation is discharged from the combustion chamber CC.
  • the capacity capable of lowering the exhaust gas temperature (in other words, the exhaust gas cooling performance) is set.
  • the exhaust gas discharged from the combustion chamber CC may contain not only water vapor and argon but also hydrogen or oxygen.
  • the supply amount of hydrogen to the combustion chamber CC is larger than a predetermined amount relative to oxygen, unburned hydrogen remains and is discharged to the circulation path 20 as it is.
  • the supply amount of oxygen to the combustion chamber CC is larger than a predetermined amount with respect to hydrogen, oxygen remains and is discharged to the circulation path 20 as it is.
  • hydrogen and oxygen in the exhaust gas are discharged from the working gas discharge port 60b of the condenser 60 to the third circulation passage 21c together with argon after the water vapor in the exhaust gas is separated by the condenser 60. Accordingly, hydrogen and oxygen in the exhaust gas circulate through the circulation path 20 similarly to argon and are supplied again to the combustion chamber CC.
  • the working gas circulation engine 1 detects the amount of hydrogen or oxygen in the gas (circulation gas) circulating in the circulation path 20 from the exhaust side to the intake side, and determines when the hydrogen or oxygen reaches the combustion chamber CC. As a matter of course, the injection amount of hydrogen from the fuel supply device 40 or the supply amount of oxygen from the oxidant supply device 30 is adjusted. Thereby, the working gas circulation engine 1 can prevent excessive hydrogen or oxygen in the combustion chamber CC.
  • the working gas circulation engine 1 is a fuel concentration detection means for detecting the concentration of fuel in the circulation gas circulating through the circulation path 20, here, a hydrogen concentration detection means for detecting the hydrogen concentration in the circulation gas.
  • a hydrogen concentration sensor 52 and an oxidant concentration detection means for detecting the concentration of the oxidant in the circulation gas here an oxygen concentration detection means for detecting the oxygen concentration in the circulation gas
  • an oxygen concentration sensor 53 is provided.
  • the hydrogen concentration sensor 52 and the oxygen concentration sensor 53 each transmit a detection signal to the electronic control unit 50.
  • the electronic control unit 50 grasps the remaining amount of hydrogen or oxygen in the circulating gas from the respective detection signals, estimates the time when the hydrogen or oxygen reaches the combustion chamber CC, and determines the amount of hydrogen in the fuel injection means 42.
  • the injection amount or the target pressure of the regulator 34 (that is, the supply amount of oxygen) is controlled.
  • the piston 13 is pushed down by the thermal expansion of argon having a large specific heat ratio accompanying the combustion of hydrogen in the combustion chamber CC.
  • this cycle is repeated with the intake stroke, compression stroke, combustion stroke, and exhaust stroke as one cycle.
  • the reciprocating motion of the piston 13 is transmitted to the crankshaft 19 by the connecting rod 14, and the reciprocating motion is converted into rotational motion by the action of the connecting rod 14 and the crankshaft 19, and the crankshaft 19 rotates.
  • the electronic control unit 50 determines the rotational position of the crankshaft 19, the accelerator opening that is the operation amount of an accelerator pedal (not shown) provided in the driver's seat of the vehicle, the remaining amount of hydrogen or oxygen in the circulating gas, and the like.
  • the hydrogen injection amount of the fuel injection means 42 or the target pressure of the regulator 34 (that is, the oxygen supply amount) is controlled according to the operating state.
  • the working gas circulation engine 1 reciprocates the intake valve 15 and the exhaust valve 16 as the crankshaft 19 rotates, and repeats communication and disconnection between the circulation path 20 and the combustion chamber CC. And repeat the above four steps.
  • the intake valve 15 is closed, both the intake valve 15 and the exhaust valve 16 are closed, and the piston 13 is moved from the bottom dead center to the top dead center.
  • oxygen and argon in the combustion chamber CC are compressed and the temperature rises.
  • the working gas circulation engine 1 injects high-pressure hydrogen into high-temperature compressed gas (oxygen and argon) formed in the combustion chamber CC in the combustion stroke, so that a part of the hydrogen is injected. It self-ignites and burns while diffusing and mixing hydrogen and compressed gas (oxygen).
  • oxygen and argon having a large specific heat ratio causes thermal expansion, and the piston 13 is pushed down by the diffusion combustion of hydrogen and the thermal expansion of argon, whereby the working gas circulation engine 1 Generate power.
  • the intake valve 15 is kept closed, the exhaust valve 16 is opened, and the piston 13 is moved from the bottom dead center side to the top dead center side.
  • the exhaust gas containing water vapor and argon is discharged from the combustion chamber CC to the exhaust pipe 18 via the exhaust port 11c of the circulation path 20.
  • the working gas circulation engine 1 In the working gas circulation engine 1, exhaust gas containing water vapor and argon is discharged from the combustion chamber CC to the circulation path 20, and when this exhaust gas circulates in the circulation path 20 toward the combustion chamber CC. In the condenser 60, the water vapor in the exhaust gas is liquefied, condensed and separated. As a result, the working gas circulation engine 1 does not supply steam with a small specific heat ratio to the combustion chamber CC, and again supplies argon as a working gas with a large specific heat ratio to the combustion chamber CC. High driving can be performed.
  • the working gas circulation engine 1 removes water vapor in the exhaust gas in the condenser 60 when the exhaust gas is circulated toward the combustion chamber CC as a circulation gas.
  • the working gas circulation engine 1 does not supply water vapor with a small specific heat ratio to the combustion chamber CC, but again supplies argon as a working gas with a large specific heat ratio to the combustion chamber CC, thereby performing an operation with high thermal efficiency. ing.
  • the working gas circulation engine 1 discharges the condensed water separated by the condenser 60 from the condensed water discharge port 60c to the condensed water discharge passage 64, drains it outside the system of the circulation path 20, and simply condensate water. Since the size of the condensed water storage tank 70 is limited only by being stored in the storage tank 70, various problems such as deterioration of the mountability may occur. Therefore, it is necessary to appropriately process this condensed water. .
  • the working gas circulation engine 1 is provided with a condensate water storage tank for storing condensate water so as to cover the exhaust pipe 18 through which high-temperature exhaust gas after combustion flows.
  • the condensed water can be appropriately treated by treating after evaporating the water, there is room for further improvement in terms of mountability. That is, the working gas circulation engine 1 is stored in the condensed water storage tank when the condensed water storage tank is provided so as to cover the exhaust pipe 18 as described above and the condensed water is evaporated using the exhaust heat. In order to bring the condensed water into contact with the outer surface of the exhaust pipe 18, the condensed water storage tank must be disposed in a limited mounting space near the exhaust pipe 18.
  • the working gas circulation engine 1 has less freedom in mounting the condensed water storage tank. For example, to ensure a sufficient capacity of the condensed water storage tank, the working gas circulation engine 1 is made larger. On the other hand, there is a risk that sufficient condensate storage tank capacity cannot be secured.
  • the working gas circulation engine 1 of the present embodiment causes the condensed water stored in the condensed water storage tank 70 as the condensed water storage means to be discharged from the atmospheric pressure by the pressure feeding unit 80 as the pressure feeding means.
  • the condensed water is pumped to the heat exchanger 90 as the evaporation means at a high pressure, and the condensed water pumped by the heat exchanger 90 is evaporated using the exhaust heat of the exhaust gas, so that the condensed water is appropriately processed. Yes.
  • the condensed water storage tank 70 can store condensed water.
  • the condensed water storage tank 70 can store the condensed water separated by the condenser 60 and is connected to the condensed water discharge passage 64. Therefore, the condensed water separated by the condenser 60 is discharged to the condensed water discharge passage 64 via the condensed water discharge port 60 c of the condenser 60 and discharged to the condensed water storage tank 70.
  • the pressure feeding unit 80 pumps the condensed water stored in the condensed water storage tank 70 at a pressure higher than the atmospheric pressure.
  • the pumping unit 80 of this embodiment includes a condensed water path 81 and a condensed water pump 82.
  • Condensed water path 81 allows condensed water to flow inside.
  • the condensed water path 81 connects the condensed water storage tank 70 and a heat exchanger 90 described later so that condensed water can flow.
  • the condensed water path 81 is configured to include the above-described condensed water discharge path 64 and the atmosphere opening path 83.
  • the condensed water discharge passage 64 connects the condensed water discharge port 60c of the condenser 60 and the condensed water storage tank 70, and one end is connected to the condensed water discharge port 60c of the condenser 60.
  • the end opens to a space for storing condensed water inside the condensed water storage tank 70.
  • the atmosphere opening passage 83 opens the inside of the condensed water storage tank 70 to the atmosphere via a heat exchanger 90 to be described later, and one end opens to a space for storing condensed water inside the condensed water storage tank 70. The other end opens to the atmosphere.
  • a heat exchanger 90 described later is provided in the atmosphere opening passage 83. As a result, as will be described later, the condensed water pumped from the condensed water storage tank 70 to the heat exchanger 90 via the atmosphere release passage 83 evaporates in the heat exchanger 90 to become water vapor, and this water vapor is released to the atmosphere. The other end of the passage 83 is opened to the atmosphere.
  • the condensed water path 81 as a whole is a path in which one end on the condensed water discharge passage 64 side is connected to the condensed water discharge port 60c of the condenser 60 and the other end on the atmosphere opening passage 83 side is opened to the atmosphere.
  • the condensed water storage tank 70 is provided between the condensed water discharge passage 64 and the atmosphere release passage 83, and the heat exchanger 90 is provided on the atmosphere release passage 83.
  • the condensate pump 82 is provided in the condensate path 81 and pressurizes the condensate and pumps it from the condensate storage tank 70 side to the heat exchanger 90 side.
  • the condensed water pump 82 of the present embodiment is provided on the atmosphere opening passage 83 in the condensed water path 81.
  • the condensed water pump 82 is provided in the atmosphere opening passage 83 between the opening of the atmosphere opening passage 83 located inside the condensed water storage tank 70 and a heat exchanger 90 described later.
  • the condensed water pump 82 sucks condensed water stored in the condensed water storage tank 70 into the atmosphere opening passage 83 through an opening of the atmosphere opening passage 83 located inside the condensed water storage tank 70, and this condensed water is atmospheric pressure. Pressurize to a higher pressure.
  • the condensed water pump 82 pressurizes the pressure of the condensed water in the atmosphere open passage 83 of the condensed water path 81 to a pressure higher than the atmospheric pressure, and then pumps the condensed water from the condensed water storage tank 70 side to the heat exchanger 90 side.
  • this condensed water pump 82 can adjust the pumping amount of condensed water by the drive being controlled by the electronic control apparatus 50, for example.
  • the heat exchanger 90 evaporates the condensed water pumped by the pumping unit 80 by the exhaust heat of the exhaust gas.
  • the heat exchanger 90 evaporates the condensed water by the exhaust heat of the exhaust gas by exchanging heat between the exhaust gas and the condensed water.
  • the heat exchanger 90 is provided in the circulation path 20.
  • the heat exchanger 90 of the present embodiment is provided on the second circulation passage 21 b in the circulation passage 21. That is, the heat exchanger 90 is provided between the exhaust port 11c and the condenser 60 in the second circulation passage 21b, and the exhaust gas introduction port 90a for introducing the exhaust gas therein is provided in the exhaust port of the second circulation passage 21b.
  • An exhaust gas discharge port 90b that is connected to the 11c side and discharges exhaust gas from the inside is connected to the condenser 60 side of the second circulation passage 21b.
  • the heat exchanger 90 is connected so that the atmosphere opening passage 83 of the condensed water passage 81 passes through the inside.
  • the condensed water path 81 is provided so as to pass through the inside of the heat exchanger 90.
  • the heat exchanger 90 exchanges heat between the exhaust gas flowing through the second circulation passage 21b and the condensed water that is pumped through the atmosphere opening passage 83 by the condensed water pump 82, and this heat is generated by the exhaust heat of the exhaust gas.
  • the condensed water can be evaporated.
  • the heat exchanger 90 evaporates the condensed water by the exhaust gas upstream of the condenser 60 with respect to the circulation direction of the working gas circulating in the circulation path 20, that is, the exhaust heat of the high-temperature exhaust gas after combustion. Can be made.
  • the condensed water separated by the condenser 60 is discharged to the condensed water storage tank 70 via the condensed water discharge port 60c and the condensed water discharge passage 64. It is stored in the water storage tank 70.
  • the condensed water stored in the condensed water storage tank 70 is sucked into the atmospheric open passage 83 through the opening of the atmospheric open passage 83 located inside the condensed water storage tank 70 when the condensed water pump 82 is driven. Is pressurized to a high pressure and fed toward the heat exchanger 90. Then, the condensed water pressure-fed toward the heat exchanger 90 through the atmosphere opening passage 83 reaches the heat exchanger 90.
  • the condensed water that is pumped by the condensed water pump 82 through the atmosphere opening passage 83 and reaches the heat exchanger 90 flows through the second circulation passage 21b and is introduced into the heat exchanger 90 by the heat exchanger 90.
  • the heat of the exhaust gas is absorbed and the temperature rises. As a result, it evaporates and becomes water vapor.
  • the water vapor generated by the evaporation of the condensed water in the heat exchanger 90 flows in one direction from the heat exchanger 90 side to the atmosphere side through the atmosphere opening passage 83 and is released from the opening of the atmosphere opening passage 83 to the atmosphere. .
  • the working gas circulation engine 1 is separated by the condenser 60 by evaporating the condensed water in the condensed water storage tank 70 by using the exhaust heat of the exhaust gas in the heat exchanger 90 and releasing it into the atmosphere as water vapor. Since the condensed water thus treated can be appropriately processed, the capacity of the condensed water storage tank 70 can be relatively reduced, and the mounting property of the working gas circulation engine 1 on the vehicle can be improved.
  • the working gas circulation engine 1 pumps the condensed water stored in the condensed water storage tank 70 to the heat exchanger 90 by the pumping unit 80 and evaporates the condensed water. Therefore, it is not necessary to directly contact the condensed water stored in the exhaust pipe 18 and the outer surface of the exhaust pipe 18 forming the second circulation passage 21b, and it is not necessary to arrange the condensed water storage tank 70 in a limited mounting space near the exhaust pipe 18. . As a result, this working gas circulation engine 1 can improve the degree of freedom of the place where the condensed water storage tank 70 is mounted.
  • this working gas circulation engine 1 may, for example, increase the size of the working gas circulation engine 1 in order to ensure a sufficient capacity of the condensed water storage tank 70, or conversely, a sufficient capacity of the condensed water storage tank 70. Can not be secured. Further, in this working gas circulation engine 1, since the condensed water is not in direct contact with the exhaust pipe 18 forming the second circulation passage 21b, it is possible to prevent the exhaust pipe 18 from locally lowering the temperature. As a result, it is possible to suppress the occurrence of thermal distortion in the exhaust pipe 18, thereby improving the durability of the exhaust pipe 18.
  • the working gas circulation engine 1 pumps the condensed water stored in the condensed water storage tank 70 to the heat exchanger 90 at a pressure higher than the atmospheric pressure by the pumping unit 80 and generates water vapor generated in the heat exchanger 90. From the condensed water storage tank 70 side through the heat exchanger 90 to the atmosphere side in one direction after the condensed water and the heat exchanger 90 evaporate. It is possible to prevent the condensed water and water vapor from flowing back through the atmosphere opening passage 83. As a result, the working gas circulation engine 1 can pump the condensed water stored in the condensed water storage tank 70 to the heat exchanger 90 by the pumping unit 80, evaporate the condensed water, and reliably release it to the atmosphere. .
  • this working gas circulation engine 1 is provided in the second circulation passage 21b upstream of the condenser 60 with respect to the circulation direction of the working gas in which the heat exchanger 90 circulates in the circulation path 20, so that heat exchange is performed. Since the exhaust heat of the exhaust gas before the condenser 90 reaches the condenser 60 can be absorbed by the condensed water, the temperature of the exhaust gas before being introduced into the condenser 60 can be lowered. As a result, since the working gas circulation engine 1 can lower the temperature of the exhaust gas introduced into the condenser 60, the exhaust gas temperature is lowered to a temperature at which the water vapor in the exhaust gas is liquefied and condensed.
  • the condenser 60 and the radiator 63 can be reduced in size.
  • the working gas circulation engine 1 can reduce the temperature of the exhaust gas introduced into the condenser 60, the amount of heat that the cooling water takes from the exhaust gas in the condenser 60 can be reduced.
  • the capacity of the device 60 and the radiator 63 can be reduced.
  • the working gas circulation engine 1 can separate the water vapor from the exhaust gas by the condenser 60 and the radiator 63 having a relatively small capacity, and can prevent a decrease in the average specific heat ratio of the working gas. The highly efficient operation can be maintained while the working gas circulation engine 1 is downsized and mountability is improved.
  • this working gas circulation engine 1 is exhausted by exchanging heat between the exhaust gas and the condensed water in the heat exchanger 90 without providing a condenser, a radiator, etc. separately from the radiator 63 for the condenser 60, for example. Since the temperature of the gas can be lowered, the working gas circulation engine 1 can be downsized also in this respect, and as a result, the mounting property of the working gas circulation engine 1 on the vehicle can be improved. .
  • the condensate resulting from the heat exchange between the exhaust gas and the condensed water in the heat exchanger 90 is, for example, the second circulation passage 21 b and the exhaust gas inlet 60 a.
  • oxygen as an oxidant
  • hydrogen as a fuel that generates water vapor by combustion with this oxygen
  • a specific heat ratio higher than that of air Argon is supplied and can expand as the hydrogen burns
  • the combustion chamber CC is capable of exhausting water vapor and argon as the exhaust gas after the hydrogen combustion, and the argon contained in the exhaust gas is the combustion chamber.
  • a circulation path 20 that can be circulated from the exhaust side of the CC to the intake side and supplied to the combustion chamber CC again, a condenser 60 that is provided in the circulation path 20 and that condenses water vapor contained in the exhaust gas into condensed water,
  • the condensed water storage tank 70 capable of storing water
  • the pumping unit 80 for pumping the condensed water stored in the condensed water storage tank 70 at a pressure higher than the atmospheric pressure, and the condensed water pumped by the pumping unit 80
  • the working gas circulation engine 1 pumps the condensed water stored in the condensed water storage tank 70 to the heat exchanger 90 at a pressure higher than the atmospheric pressure by the pressure feeding unit 80, and the pressure is fed by the heat exchanger 90. Since the condensed water is evaporated using the exhaust heat of the exhaust gas, the condensed water stored in the condensed water storage tank 70 can be discharged to the atmosphere as water vapor. As a result, for example, a working gas circulation engine 1 can be mounted on the vehicle, and the condensed water separated by the condenser 60 can be appropriately treated.
  • the working gas circulation engine 1 according to the embodiment of the present invention described above, the oxidant is oxygen and the fuel is hydrogen. Therefore, the working gas circulation engine 1 separates the water vapor generated by the combustion of oxygen and hydrogen as condensed water by the condenser 60, temporarily stores the condensed water in the condensed water storage tank 70, and then presses the pressure feeding unit 80. And the heat exchanger 90 can be discharged into the atmosphere as water vapor and processed appropriately.
  • the heat exchanger 90 is located upstream of the condenser 60 with respect to the circulation direction of the working gas circulating in the circulation path 20.
  • the condensed water is evaporated by the exhaust heat of the exhaust gas. Accordingly, the working gas circulation engine 1 evaporates the condensed water by the exhaust heat of the exhaust gas upstream of the condenser 60 with respect to the circulation direction of the working gas through which the heat exchanger 90 circulates in the circulation path 20.
  • the condensed water can be efficiently evaporated by the exhaust heat of the relatively high temperature exhaust gas.
  • the working gas circulation engine 1 can absorb the exhaust heat of the exhaust gas before reaching the condenser 60 into the condensed water, the temperature of the exhaust gas introduced into the condenser 60 can be reduced. The capacity of the condenser 60 and the radiator 63 can be reduced. As a result, the working gas circulation engine 1 can reduce the size of the condenser 60 and the radiator 63, and can further improve the mountability after properly treating the condensed water separated by the condenser 60. .
  • the pressure feeding unit 80 connects the condensed water storage tank 70 and the heat exchanger 90 so that the condensed water can flow.
  • a condensate water pump 82 is provided in the condensate water path 81 and pressurizes the condensate water in the condensate water path 81 and pumps it from the condensate water storage tank 70 side to the heat exchanger 90 side. Therefore, the working gas circulation engine 1 pumps the condensed water stored in the condensed water storage tank 70 to the heat exchanger 90 via the condensed water path 81 at a pressure higher than the atmospheric pressure by the condensed water pump 82 to exchange heat.
  • the working gas circulation engine 1 can pump the condensed water stored in the condensed water storage tank 70 to the heat exchanger 90 by the pumping unit 80, evaporate the condensed water, and reliably release it to the atmosphere. .
  • the heat exchanger 90 is condensed water by the exhaust heat of the exhaust gas upstream of the condenser 60 with respect to the circulation direction of the working gas provided in the second circulation passage 21b and circulating in the circulation path 20.
  • the heat exchanger 90 is provided, for example, on the downstream side of the condenser 60 in the circulation passage 21 as long as it can obtain a heat quantity sufficient to evaporate the condensed water from the exhaust heat of the exhaust gas. It may be.
  • the heat exchanger 90 since the exhaust heat of the exhaust gas after combustion becomes relatively high as it becomes closer to the exhaust port 11c side of the combustion chamber CC, the heat exchanger 90 is relatively in the combustion chamber CC in the circulation passage 21.
  • the heat exchanger 90 is preferably provided on the upstream side of the working gas discharge port 60b of the condenser 60, and more specifically, on the upstream side of the exhaust gas introduction port 60a of the condenser 60 as described above. More preferably, it is provided.
  • the atmosphere opening passage 83 that forms the condensed water path 81 may be configured such that a part of the condensed water storage tank 70 side from the heat exchanger 90 passes inside the condenser 60.
  • the cooling water circulation path 61 and the air release path 83 need only be separate from each other inside the condenser 60.
  • the working gas circulation engine 1 reaches the heat exchanger 90 because the condensed water moving toward the heat exchanger 90 in the atmosphere opening passage 83 absorbs the exhaust heat of the exhaust gas in the condenser 60. Therefore, the heat exchanger 90 can efficiently evaporate the condensed water preheated in the condenser 60.
  • the condensed water pump 82 of the pressure feeding unit 80 may be provided other than the atmosphere opening passage 83.
  • FIG. 2 is a schematic configuration diagram of a working gas circulation engine according to Modification 1 of the present invention.
  • the working gas circulation engine 1A includes a pumping unit 80A as a pumping unit, and the pumping unit 80A includes a condensed water path 81 and a condensed water pump 82A.
  • the condensed water path 81 includes a condensed water discharge path 64 and an atmosphere opening path 83.
  • the condensed water pump 82A is provided in the condensed water path 81, pressurizes condensed water, and pumps the condensed water from the condensed water storage tank 70A side to the heat exchanger 90 side.
  • the condensed water pump 82 ⁇ / b> A of this modification is provided on the condensed water discharge passage 64 in the condensed water path 81.
  • the condensate water storage tank 70A as the condensate storage means of this modification has a sealed space for storing condensate. Therefore, the condensed water pump 82A pumps the condensed water in the condensed water discharge passage 64 so as to push it toward the condensed water storage tank 70A side in which the internal space is sealed, so that the inside of the condensed water storage tank 70A. Can be pressurized to a pressure higher than atmospheric pressure, and the condensed water stored in the condensed water storage tank 70 ⁇ / b> A can be pumped toward the heat exchanger 90 side through the atmosphere opening passage 83.
  • the working gas circulation engine 1A pumps the condensed water stored in the condensed water storage tank 70A to the heat exchanger 90 at a pressure higher than the atmospheric pressure by the pumping unit 80A.
  • the condensed water thus pumped is evaporated using the exhaust heat of the exhaust gas, so that the condensed water stored in the condensed water storage tank 70A can be discharged to the atmosphere as water vapor.
  • the mounting property of the working gas circulation engine 1A on the vehicle can be improved, and the condensed water separated by the condenser 60 can be appropriately treated.
  • the working gas circulation engine 1A exchanges heat of the condensed water stored in the condensed water storage tank 70A through the condensed water path 81 at a pressure higher than the atmospheric pressure by the condensed water pump 82A. Since the water vapor generated by the heat exchanger 90 is pumped to the vessel 90 and released to the atmosphere, it is possible to prevent the condensed water and water vapor flowing through the condensed water passage 81 from flowing backward. As a result, the working gas circulation engine 1 can pump the condensed water stored in the condensed water storage tank 70A to the heat exchanger 90 by the pumping section 80A, evaporate the condensed water, and reliably release it to the atmosphere. .
  • FIG. 3 is a schematic schematic configuration diagram of a working gas circulation engine according to Embodiment 2 of the present invention
  • FIG. 4 is a schematic schematic configuration diagram of a working gas circulation engine according to Modification 2 of the present invention. is there.
  • the working gas circulation engine according to the second embodiment has substantially the same configuration as the working gas circulation engine according to the first embodiment, but the structure of the pressure feeding means is different from that of the working gas circulation engine according to the first embodiment.
  • symbol is attached
  • the working gas circulation engine 201 includes a pressure feeding unit 280 as pressure feeding means, as shown in FIG.
  • the pumping unit 280 pumps the condensed water stored in the condensed water storage tank 270 at a pressure higher than the atmospheric pressure.
  • the pumping unit 280 includes a condensed water passage 81, and the condensed water passage 81 includes a condensed water discharge passage 64 and an air release passage 83.
  • the condensed water path 81 has a path in which one end on the condensed water discharge passage 64 side is connected to the condensed water discharge port 60c of the condenser 60 and the other end on the atmosphere opening path 83 side is opened to the atmosphere.
  • a condensed water storage tank 270 as condensed water storage means is provided between the water discharge passage 64 and the atmosphere release passage 83, and a heat exchanger 90 is provided on the atmosphere release passage 83.
  • the pumping unit 280 of the present embodiment does not include the condensed water pump 82 (see FIG. 1) and the condensed water pump 82A (see FIG. 2) described above, and the pumping unit 80 (see FIG. 1) This is different from the pressure feeding unit 80A (see FIG. 2).
  • the condensed water storage tank 270 of this embodiment has the space part which stores condensed water sealed like the condensed water storage tank 70A (refer FIG. 2) demonstrated above.
  • the condensed water path 81 of the pumping unit 280 of this embodiment connects the condensed water storage tank 270 and the heat exchanger 90 so that the condensed water can flow, and the space for storing the condensed water is sealed.
  • the condensed water storage tank 270 communicates with the circulation path 20. That is, the condensed water path 81 is configured to communicate with the circulation path 21 of the circulation path 20 through the condenser 60 via the condensed water storage tank 270 in which the space for storing condensed water is sealed. .
  • the pressure feeding unit 280 uses the pressure of the circulation passage 21 of the circulation path 20, that is, the pressure of the gas in the circulation path 21, after the condensed water storage tank 270 is sealed, The condensed water is pressurized and fed from the condensed water storage tank 270 side to the heat exchanger 90 side.
  • the pressure feeding unit 280 pressurizes the condensed water in the condensed water path 81 and pumps it from the condensed water storage tank 270 side to the heat exchanger 90 side when the pressure in the circulation path 21 of the circulation path 20 becomes higher than the atmospheric pressure. Can do.
  • the pressure feeding unit 280 pushes the condensed water in the condensed water discharge passage 64 toward the condensed water storage tank 270 that is in a sealed state by the pressure of the circulation passage 21 of the circulation path 20 higher than the atmospheric pressure.
  • the pressure inside the condensed water storage tank 270 is increased to a pressure higher than the atmospheric pressure, and the condensed water stored in the condensed water storage tank 270 is transferred to the heat exchanger 90 side via the atmosphere opening passage 83. Can be pumped toward.
  • the pressure in the circulation path 21 of the circulation path 20 does not need to be higher than the atmospheric pressure in the entire circulation path 20, for example, in the vicinity of a portion where condensed water is discharged from the condenser 60, that is, a condensed water discharge port. What is necessary is just to make the vicinity of 60c higher than atmospheric pressure.
  • the working gas circulation engine 201 causes the condensed water stored in the condensed water storage tank 270 to be higher than the atmospheric pressure by the pumping unit 280.
  • the condensate stored in the condensate storage tank 270 is steamed because the condensed water pumped by the heat exchanger 90 is evaporated using the exhaust heat of the exhaust gas.
  • the mounting property of the working gas circulation engine 201 on the vehicle can be improved, and the condensed water separated by the condenser 60 can be appropriately treated.
  • the pressure feeding unit 280 connects the condensed water storage tank 270 and the heat exchanger 90 so that the condensed water can flow
  • a condensed water path 81 communicates with the circulation path 20 via a condensed water storage tank 270 in which the space for storing the condensed water is hermetically sealed, and the condensed water is caused by the gas pressure in the circulation path 20 higher than the atmospheric pressure.
  • the condensed water in the path 81 is pressurized and fed from the condensed water storage tank 270 side to the heat exchanger 90 side.
  • the working gas circulation engine 201 pumps the condensed water stored in the condensed water storage tank 270 to the heat exchanger 90 via the condensed water path 81 by the pressure of the gas in the circulation path 20 higher than the atmospheric pressure. Since the water vapor generated in the exchanger 90 is released to the atmosphere, it is possible to reliably prevent the condensed water flowing through the condensed water path 81 (water vapor after being evaporated in the heat exchanger 90) from flowing backward. As a result, the working gas circulation engine 1 can pump the condensed water stored in the condensed water storage tank 270 to the heat exchanger 90 by the pumping unit 280, evaporate the condensed water, and reliably release it to the atmosphere. .
  • the working gas circulation engine 201 pressurizes the condensed water in the condensed water path 81 using the pressure of the gas in the circulation path 20 after the pressure feeding unit 280 has sealed the condensed water storage tank 270 in a sealed state. Since it is pumped from the condensed water storage tank 270 side to the heat exchanger 90 side, for example, there is no need to provide the condensed water pump 82 (see FIG. 1) and the condensed water pump 82A (see FIG. 2) as described above.
  • the working gas circulation engine 201 can be reduced in size, and the mounting property of the working gas circulation engine 201 on the vehicle can be further improved.
  • the pumping unit 280 of the working gas circulation engine 201 described above may further include working gas storage means and adjustment means.
  • FIG. 4 is a schematic configuration diagram of a working gas circulation engine according to the second modification of the present invention.
  • the working gas circulation engine 201A includes a pressure feeding unit 280A as pressure feeding means.
  • the condensed water storage tank 270 has a sealed space for storing condensed water.
  • the pumping unit 280A of the present modification has substantially the same configuration as the above-described pumping unit 280, but further includes a high-pressure tank 284A as a working gas storage unit and a pressure regulating valve 285A as a regulating unit. It differs from the above-mentioned pumping part 280 by the point comprised.
  • the high-pressure tank 284A is provided to be branched from the circulation path 20, and stores, for example, a working gas having a relatively high pressure compared to the gas pressure in the circulation path 20.
  • the high-pressure tank 284A is provided on the circulation passage 21 of the circulation passage 20, here, the branch passage 286A branched from the third circulation passage 21c.
  • the inside of the high-pressure tank 284A communicates with the inside of the third circulation passage 21c via the branch passage 286A.
  • the pressure regulating valve 285A regulates the inflow / outflow of the working gas between the high pressure tank 284A and the circulation passage 21 of the circulation path 20, in this case, the third circulation path 21c.
  • the pressure regulating valve 285A is provided in the branch passage 286A, and the opening and closing operation of the valve body is executed, the opening degree of the branch passage 286A is adjusted, and the passage area of the branch passage 286A is adjusted, so that the high pressure tank 284A and the third circulation are provided.
  • the inflow and outflow of the working gas to and from the passage 21c can be adjusted.
  • the opening degree of the pressure regulating valve 285A is adjusted by the electronic control unit 50, and the flow of working gas between the high pressure tank 284A and the third circulation passage 21c is adjusted.
  • the pressure of the gas in the circulation passage 21 of the circulation path 20 can be made higher than the atmospheric pressure, so that the pressure feeding unit 280A condenses using the pressure of the gas in the circulation path 21 of the circulation path 20.
  • the condensed water in the water path 81 can be pressurized and fed from the condensed water storage tank 270 side to the heat exchanger 90 side.
  • the opening degree of the pressure regulating valve 285A is adjusted by the electronic control unit 50, and the inflow / outflow of the working gas between the high pressure tank 284A and the third circulation passage 21c is regulated, so By controlling the pressure of the gas inside, the pumping amount of the condensed water can be adjusted.
  • the pressure feeding unit 280A is branched from the circulation path 20 and stores a relatively high pressure working gas 284A. You may comprise so that it may have the pressure control valve 285A which adjusts the inflow / outflow of the working gas between the high pressure tank 284A and the circulation path 20.
  • the pressure of the gas in the circulation path 20 can be made higher than the atmospheric pressure by adjusting the opening degree of the pressure control valve 285A by the electronic control unit 50, whereby the pressure feeding unit 280A
  • the pressure feeding unit 280A regulates the opening degree of the pressure regulating valve 285A without controlling the combustion state of oxygen and hydrogen in the combustion chamber CC, in other words, without controlling the supply amount of oxygen and hydrogen.
  • the pressure of the gas in the circulation path 20 can be adjusted by adjusting the flow of the working gas between the high-pressure tank 284A and the third circulation passage 21c, for example, the condensed water pump 82 (FIG. 1). And the condensate pump 82A (see FIG. 2) can be adjusted without changing the combustion state of oxygen and hydrogen in the combustion chamber CC.
  • FIG. 5 is a schematic schematic configuration diagram of a working gas circulation engine according to the third embodiment of the present invention
  • FIG. 6 is a flowchart for explaining pressure feed amount control of the working gas circulation engine according to the third embodiment of the present invention. It is.
  • the working gas circulation engine according to the third embodiment has substantially the same configuration as the working gas circulation engine according to the first embodiment, but is different from the working gas circulation engine according to the first embodiment in that it includes a pressure feed amount control unit. Different.
  • the working gas circulation engine 301 is functionally conceptually provided with a pumping amount control unit 351 as a pumping amount control unit in an electronic control unit (ECU) 50.
  • ECU electronice control unit
  • the electronic control unit 50 is mainly configured of a microcomputer, and includes a processing unit 50a, a storage unit 50b, and an input / output unit 50c, which are connected to each other and can exchange signals with each other.
  • a drive circuit (not shown) for driving each part of the vehicle including the working gas circulation engine 301 and the various sensors described above are connected to the input / output unit 50c.
  • the input / output unit 50c is connected to these sensors and the like.
  • the storage unit 50b stores a computer program for controlling each unit of the working gas circulation engine 301.
  • the storage unit 50b is a hard disk device, a magneto-optical disk device, a non-volatile memory such as a flash memory (a storage medium that can only be read such as a CD-ROM), or a RAM (Random Access Memory).
  • a volatile memory or a combination thereof can be used.
  • the processing unit 50a is configured by a memory (not shown) and a CPU (Central Processing Unit), and includes at least the above-described pumping amount control unit 351.
  • Various controls by the electronic control unit 50 are performed by the processing unit 50a reading the computer program into a memory incorporated in the processing unit 50a based on the detection results of the sensors provided in the respective units, and depending on the calculation results. This is executed by sending a control signal.
  • the processing unit 50a appropriately stores a numerical value in the middle of the calculation in the storage unit 50b, and extracts the stored numerical value to execute the calculation.
  • you may control by the dedicated hardware different from the electronic controller 50 instead of the said computer program.
  • the pumping amount control part 351 adjusts the pumping quantity of the condensed water in the pumping part 80 by controlling the drive of the condensate pump 82.
  • the pumping amount control unit 351 of the present embodiment controls the driving of the condensed water pump 82 based on the amount of condensed water generated separated by the condenser 60 to control the pumping amount of condensed water.
  • the working gas circulation engine 301 of this embodiment includes a flow rate sensor 54 as a flow rate detection means.
  • the flow rate sensor 54 detects the flow rate of the condensed water to the condensed water storage means.
  • the flow rate sensor 54 of the present embodiment is provided in the condensed water discharge passage 64 that forms the condensed water passage 81.
  • the condensed water discharge port 60 c and the condensed water discharge passage 64 are connected from the condenser 60.
  • the flow rate of the condensed water discharged to the condensed water storage tank 70 is detected.
  • the flow sensor 54 transmits a detection signal to the electronic control device 50.
  • the pumping amount control unit 351 detects and acquires the generation amount of the condensed water separated by the condenser 60 based on the flow rate of the condensed water detected by the flow sensor 54.
  • the pumping amount control part 351 controls the drive of the condensed water pump 82 based on the acquired amount of condensed water, and controls the pumping amount of condensed water. More specifically, the pumping amount control unit 351 controls the pumping amount so that the condensate pumping amount by the condensate pump 82 is substantially equal to the acquired condensed water generation amount.
  • the pumping amount control unit 351 may use the flow rate of the condensed water detected by the flow sensor 54 as it is as a value corresponding to the amount of condensed water generated.
  • the pumping amount control unit 351 controls the pumping amount of the condensed water by the pumping unit 80 based on the flow rate of the condensed water detected by the flow sensor 54, and as a result, the pumping unit based on the amount of condensed water generated.
  • the amount of condensed water pumped by 80 can be controlled.
  • the pumping amount controller 351 controls the driving of the condensate pump 82 based on the amount of condensed water generated, and the amount of condensed water pumped is almost equal to the amount of condensed water generated. Therefore, the condensed water in the condensed water storage tank 70 is pumped toward the heat exchanger 90 and evaporated with a pumping amount corresponding to the amount of condensed water generated. Therefore, the amount of condensed water stored in the condensed water storage tank 70 can be reduced. Therefore, since the working gas circulation engine 301 can reduce the amount of condensed water stored in the condensed water storage tank 70, the condensed water is appropriately treated after the condensed water separated by the condenser 60 is processed. The capacity of the water storage tank 70 can be reduced, so that the mounting property of the working gas circulation engine 301 on the vehicle can be further improved.
  • This control routine is repeatedly executed at a control cycle of several ms to several tens of ms.
  • the pumping amount control unit 351 of the electronic control device 50 detects and acquires the generation amount of the condensed water separated by the condenser 60 based on the flow rate of the condensed water detected by the flow sensor 54 (S100).
  • the pumping amount control unit 351 compares the amount of condensed water generated acquired in S100 with the current amount of condensed water pumped by the condensed water pump 82, and the amount of condensed water generated is the current amount of condensed water. It is determined whether the amount is greater than the pumping amount (S101).
  • the pumping amount controller 351 controls the driving of the condensed water pump 82 to set the pumping amount of the condensed water in advance.
  • the predetermined amount is increased (S102), the current control cycle is terminated, and the process proceeds to the next control cycle.
  • the pumping amount control unit 351 controls the driving of the condensed water pump 82 to preset the pumping amount of condensed water.
  • the predetermined amount is decreased (S103), the current control cycle is terminated, and the process proceeds to the next control cycle.
  • the working gas circulation engine 301 causes the condensed water stored in the condensed water storage tank 70 to be higher than the atmospheric pressure by the pumping unit 80.
  • the condensate stored in the condensate storage tank 70 is steamed because the condensed water pumped by the heat exchanger 90 is evaporated using the exhaust heat of the exhaust gas.
  • the mounting property of the working gas circulation engine 301 on the vehicle can be improved, and the condensed water separated by the condenser 60 can be appropriately treated.
  • the working gas circulation engine 301 includes the pumping amount control unit 351 that controls the pumping amount of the condensed water by the pumping unit 80 based on the generation amount of the condensed water. . Therefore, in the working gas circulation engine 301, the pumping amount control unit 351 controls the driving of the condensate pump 82 of the pumping unit 80 based on the amount of condensed water generated, and the condensate pumping of the condensed water by the condensate pump 82 of the pumping unit 80 is performed.
  • the condensed water in the condensed water storage tank 70 can be pressure-fed and evaporated toward the heat exchanger 90 with a pumping amount corresponding to the amount of condensed water generated.
  • the amount of condensate stored in can be reduced.
  • the working gas circulation engine 301 can appropriately reduce the capacity of the condensed water storage tank 70 after properly treating the condensed water separated by the condenser 60. Can be further improved.
  • the working gas circulation engine 301 controls the pumping amount by the pumping unit 80 based on the amount of condensed water generated, the amount of heat absorbed by the condensed water from the exhaust gas in the heat exchanger 90 is also the amount of condensed water generated. Therefore, the amount of condensed water generated in the condenser 60 itself can be optimized.
  • the pumping amount control unit 351 includes the pumping unit such that the pumping amount by the pumping unit 80 is equal to the amount of condensed water generated.
  • the pumping amount by 80 is controlled. Therefore, the working gas circulation engine 301 controls the pumping amount by the pumping unit 80 so that the pumping amount control unit 351 controls the pumping amount of the condensed water to be substantially equal to the amount of condensed water generated.
  • the amount of condensed water stored in 70 can be minimized.
  • the flow rate sensor 54 that detects the flow rate of the condensed water to the condensed water storage tank 70 is provided, and the pumping amount control unit 351 includes: The pumping amount by the pumping unit 80 is controlled based on the flow rate of the condensed water detected by the flow sensor 54. Therefore, the working gas circulation engine 301 detects the amount of condensed water or a value corresponding to the amount of condensed water based on the actual flow rate of condensed water to the condensed water storage tank 70 detected by the flow sensor 54. Therefore, the accurate amount of condensed water generated can be acquired, and the amount of pumping by the pumping unit 80 can be accurately determined based on this exact amount of condensed water generated or a value corresponding to the amount of condensed water generated. Can be controlled.
  • the pumping amount control unit 351 has been described as adjusting the pumping amount of the condensed water in the pumping unit 80 by controlling the driving of the condensed water pump 82 of the pumping unit 80.
  • the amount control unit 351 The oxygen and hydrogen combustion state, in other words, the supply amount of oxygen and hydrogen is controlled, and the pressure of the gas in the circulation passage 21 of the circulation path 20 is controlled, thereby controlling the pumping amount of the condensed water by the pumping unit 280. be able to.
  • the pressure feed amount control unit 351 is configured to adjust the pressure feed amount of the condensed water in the pressure feed unit 280A (see FIG. 4) included in the working gas circulation engine 201A (see FIG. 4) of the second modification.
  • the opening of 285A see FIG. 4
  • the amount of condensed water pumped by the pumping unit 280A can be controlled.
  • FIG. 7 is a schematic schematic configuration diagram of a working gas circulation engine according to Embodiment 4 of the present invention
  • FIG. 8 is a diagram illustrating a pressure feed amount map of the working gas circulation engine according to Embodiment 4 of the present invention
  • FIG. 9 is a flowchart for explaining the control of the pumping amount of the working gas circulation engine according to the fourth embodiment of the present invention.
  • the working gas circulation engine according to the fourth embodiment has substantially the same configuration as the working gas circulation engine according to the third embodiment, but the working gas according to the third embodiment is provided with a water level detection means instead of the flow rate detection means. It is different from the circulation type engine.
  • symbol is attached
  • the working gas circulation engine 401 is functionally conceptually provided with a pumping amount control unit 451 as a pumping amount control unit in an electronic control unit (ECU) 50.
  • ECU electronice control unit
  • the pumping amount control part 451 controls the pumping amount of the condensed water in the pumping part 80 by controlling the drive of the condensed water pump 82.
  • the pumping amount control unit 451 of this embodiment controls the driving of the condensed water pump 82 based on the amount of condensed water generated separated by the condenser 60 and controls the pumping amount of condensed water.
  • the working gas circulation engine 401 of this embodiment includes a water level sensor 55 as water level detection means.
  • the water level sensor 55 detects the water level of the condensed water stored in the condensed water storage tank 70.
  • the water level sensor 55 is provided inside the condensed water storage tank 70 and detects the height from the bottom of the condensed water storage tank 70 to the water level of the condensed water, that is, the water level of the condensed water storage tank 70.
  • the water level sensor 55 transmits a detection signal to the electronic control unit 50.
  • the pumping amount control unit 451 detects and acquires the generation amount of condensed water separated by the condenser 60 based on the water level of the condensed water storage tank 70 detected by the water level sensor 55.
  • the pumping amount control unit 451 compares the water level of the condensed water storage tank 70 detected by the water level sensor 55 in the current control cycle with the water level of the condensed water storage tank 70 detected by the water level sensor 55 in the previous control cycle. Then, by calculating these differences, the amount of condensed water separated by the condenser 60 is calculated and acquired.
  • the pumping amount control part 451 controls the drive of the condensed water pump 82 based on the acquired amount of condensed water, and controls the pumping amount of condensed water.
  • the pumping amount control unit 451 is the same as the pumping amount control unit 351 (see FIG. 5) of the third embodiment described above, and the amount of condensed water generated by acquiring the condensate pumping amount by the condensed water pump 82 of the pumping unit 80. However, here, the amount of condensed water generated by the pumping amount control unit 451 and the condensed water detected by the water level sensor 55 in the current control cycle are controlled. Based on the level of the condensed water in the storage tank 70, the drive of the condensed water pump 82 of the pressure feeding unit 80 may be controlled to control the amount of condensed water pumped.
  • the pumping amount control unit 451 of the present embodiment obtains the pumping amount of the condensed water by the pumping unit 80 based on, for example, the pumping amount map m01 illustrated in FIG.
  • the horizontal axis indicates the water level of the condensed water storage tank 70
  • the vertical axis indicates the amount of condensed water generated.
  • the pumping amount map m01 describes the relationship between the water level of the condensed water storage tank 70, the amount of condensed water generated, and the amount of condensed water pumped by the pumping unit 80.
  • the pumping amount map m01 the amount of condensed water pumped by the pumping unit 80 increases as the water level of the condensed water storage tank 70 increases, and increases as the amount of condensed water generated increases.
  • the pumping amount map m01 is stored in the storage unit 50b. Based on this pumping amount map m01, the pumping amount control unit 451 determines the condensed water generated by the pumping unit 80 from the acquired amount of condensed water and the level of condensed water in the condensed water storage tank 70 detected by the water level sensor 55. Find the pumping amount.
  • required the pumping amount of the condensed water by the pumping part 80 using the pumping amount map m01 this embodiment is not limited to this.
  • the pumping amount control unit 451 may determine the pumping amount of the condensed water by the pumping unit 80 based on a mathematical expression corresponding to the pumping amount map m01. The same applies to various maps described below.
  • the pumping amount control unit 451 controls the driving of the condensate pump 82 based on the acquired amount of condensed water, and controls the pumping amount by the condensate pump 82. Since the condensed water in the condensed water storage tank 70 can be pumped toward the heat exchanger 90 and evaporated with a pumping amount corresponding to the amount of condensed water generated, the condensation stored in the condensed water storage tank 70 The amount of water can be reduced. Therefore, since the working gas circulation engine 401 can reduce the amount of condensed water stored in the condensed water storage tank 70, the condensed water is properly treated after the condensed water separated by the condenser 60 is processed. The capacity of the water storage tank 70 can be reduced, so that the mounting property of the working gas circulation engine 401 on the vehicle can be further improved.
  • the working gas circulation engine 401 detects the amount of condensed water generated and detected by the pumping amount control unit 451 based on the level of condensed water in the condensed water storage tank 70 detected by the water level sensor 55.
  • the condensed water in the condensed water storage tank 70 can be pumped with a pumping amount corresponding to the amount of condensed water generated while maintaining the water level of the condensed water in the storage tank 70 at an appropriate water level. It is possible to prevent the condensed water from being depleted, and to prevent the condensed water pump 82 from sucking gas.
  • the working gas circulation engine 401 has a relatively high level of condensed water in the condensed water storage tank 70 detected by the water level sensor 55, assuming that the amount of condensed water generated is constant. Accordingly, the pumping amount control unit 451 relatively increases the pumping amount of the condensed water by the pumping unit 80, and the water level of the condensed water in the condensed water storage tank 70 detected by the water level sensor 55 has relatively decreased. In response to this, the pumping amount control unit 451 relatively decreases the pumping amount of the condensed water by the pumping unit 80, thereby reliably maintaining the water level of the condensed water in the condensate water storage tank 70 at an appropriate level. can do.
  • the pumping amount control unit 451 may use the level of the condensed water in the condensed water storage tank 70 detected by the water level sensor 55 as a value corresponding to the amount of condensed water generated. That is, the pumping amount control unit 451 controls the amount of condensed water pumped by the pumping unit 80 based on the level of condensed water in the condensed water storage tank 70 detected by the water level sensor 55, resulting in generation of condensed water. Based on the amount, the pumping amount of the condensed water by the pumping unit 80 can be controlled.
  • This control routine is repeatedly executed at a control cycle of several ms to several tens of ms.
  • the pumping amount control unit 451 of the electronic control device 50 acquires the water level of the condensed water in the condensed water storage tank 70 detected by the water level sensor 55 (S200).
  • the pumping amount control unit 451 determines the water level of the condensed water storage tank 70 detected by the water level sensor 55 in the previous control cycle and the water level of the condensed water storage tank 70 detected by the water level sensor 55 in the current control cycle. By comparing and calculating these differences, the amount of condensed water separated by the condenser 60 is calculated and acquired (S201).
  • the pumping amount control unit 45 for example, based on the pumping amount map m01, the current condensate water level in the condensate storage tank 70 detected by the water level sensor 55 in S200 and the amount of condensate generation acquired in S201. From this, the pumping amount of the condensed water by the pumping unit 80 is obtained (S202).
  • the pumping amount control unit 451 controls the driving of the condensed water pump 82 of the pumping unit 80 based on the pumping amount of the condensed water by the pumping unit 80 calculated in S202, and changes the pumping amount by the condensed water pump 82. (S203), the current control cycle is terminated, and the process proceeds to the next control cycle.
  • the working gas circulation engine 401 is configured to cause the condensed water stored in the condensed water storage tank 70 to be higher than the atmospheric pressure by the pumping unit 80.
  • the condensate stored in the condensate storage tank 70 is steamed because the condensed water pumped by the heat exchanger 90 is evaporated using the exhaust heat of the exhaust gas.
  • the mounting property of the working gas circulation engine 401 on the vehicle can be improved, and the condensed water separated by the condenser 60 can be appropriately treated.
  • the working gas circulation engine 401 is configured so that the pumping amount control unit 451 is based on the acquired amount of condensed water. Since the condensate pump 82 is controlled to control the pumping amount of the condensate water by the condensate pump 82 of the pumping unit 80, the condensate of the condensate storage tank 70 can be condensed with a pumping amount corresponding to the amount of condensed water generated. Since water can be pumped toward the heat exchanger 90 and evaporated, the amount of condensed water stored in the condensed water storage tank 70 can be reduced. As a result, the working gas circulation engine 401 can appropriately reduce the capacity of the condensed water storage tank 70 after properly treating the condensed water separated by the condenser 60. Can be further improved.
  • the pressure level control unit includes the water level sensor 55 that detects the water level of the condensed water stored in the condensed water storage tank 70.
  • 451 controls the amount of condensed water pumped by the condensed water pump 82 of the pumping unit 80 based on the water level of the condensed water detected by the water level sensor 55. Therefore, the working gas circulation engine 401 detects and acquires the amount of condensed water or a value corresponding to the amount of condensed water based on the level of condensed water in the condensed water storage tank 70 detected by the water level sensor 55. Therefore, the condensed water in the condensed water storage tank 70 can be pumped with a pumping amount corresponding to the amount of condensed water generated while maintaining the water level of the condensed water in the condensed water storage tank 70 at an appropriate level.
  • FIG. 10 is a schematic schematic configuration diagram of a working gas circulation engine according to Embodiment 5 of the present invention
  • FIG. 11 is a diagram illustrating a pressure feed amount map of the working gas circulation engine according to Embodiment 5 of the present invention
  • FIG. 12 is a view showing a response delay time map of the working gas circulation engine according to the fifth embodiment of the present invention
  • FIG. 13 explains the pressure feed amount control of the working gas circulation engine according to the fifth embodiment of the present invention.
  • FIG. 14 is a schematic schematic configuration diagram of a working gas circulation engine according to the third modification of the present invention.
  • the working gas circulation engine according to the fifth embodiment has substantially the same configuration as the working gas circulation engine according to the third and fourth embodiments, but is implemented in that the pumping amount is controlled based on the supply amount of oxidant or fuel. This is different from the working gas circulation engine according to the third and fourth embodiments.
  • action, and effect which are common in embodiment mentioned above while overlapping description is abbreviate
  • the working gas circulation engine 501 is functionally conceptually provided with a pumping amount control unit 551 as a pumping amount control unit in an electronic control unit (ECU) 50.
  • ECU electronice control unit
  • the pressure feed amount control unit 551 adjusts the pressure feed amount of the condensed water in the pressure feed unit 80 by controlling the driving of the condensed water pump 82.
  • the pumping amount control unit 551 of the present embodiment controls the driving of the condensed water pump 82 based on the amount of condensed water generated separated by the condenser 60 to control the pumping amount of condensed water.
  • the amount of condensed water separated by the condenser 60 is an amount corresponding to the amount of water vapor generated by the combustion of hydrogen and oxygen in the combustion chamber CC.
  • the amount of water vapor generated by the combustion of hydrogen and oxygen in the combustion chamber CC is the engine load, in other words, the amount of hydrogen combusted in the combustion chamber CC, in other words, hydrogen supplied to the combustion chamber CC or
  • the amount corresponds to the amount of oxygen supplied.
  • a working gas circulation engine 501 can realize an engine load according to the driving force requested by the driver for the working gas circulation engine 501 as described above.
  • a hydrogen supply amount is set, and an oxygen supply amount is set.
  • the pumping amount control unit 551 of the present embodiment is configured to pump the condensed water by the pumping unit 80 based on the engine load, for example, the supply amount of oxygen as the oxidant or hydrogen as the fuel supplied to the combustion chamber CC.
  • the pumping amount control unit 551 controls the pumping amount of the condensed water by the pumping unit 80 based on the supply amount of hydrogen supplied to the combustion chamber CC.
  • the pumping amount control unit 551 may control the pumping amount of condensed water by the pumping unit 80 based on the supply amount of oxygen supplied to the combustion chamber CC.
  • the pumping amount of the condensed water by the pumping unit 80 may be controlled based on both the supply amount of oxygen and the supply amount of oxygen.
  • the pumping amount control unit 551 acquires the supply amount of hydrogen actually injected from the fuel injection means 42 into the combustion chamber CC, and controls the driving of the condensate pump 82 based on the supply amount of hydrogen to pump condensate water. Control the amount.
  • the pumping amount control unit 551 is actually injected from the fuel injection unit 42 into the combustion chamber CC based on, for example, the opening period of the fuel injection unit (fuel injection valve) 42 or the flow rate of hydrogen detected by the fuel flow meter 45. What is necessary is just to acquire the supply amount of hydrogen.
  • the pumping amount control unit 551 controls the pumping amount of condensed water by the pumping unit 80 based on the supply amount of hydrogen actually injected from the fuel injection means 42 into the combustion chamber CC as a value corresponding to the amount of condensed water generated. As a result, the pumping amount of the condensed water by the pumping unit 80 can be controlled based on the amount of the condensed water generated.
  • the pumping amount control unit 551 estimates and obtains the amount of condensed water generated based on the amount of hydrogen actually injected from the fuel injection means 42 into the combustion chamber CC, and based on the amount of condensed water generated. You may make it control the pumping amount of the condensed water by the pumping part 80. FIG.
  • the pumping amount control unit 551 obtains the pumping amount of the condensed water by the pumping unit 80 based on, for example, the pumping amount map m02 shown in FIG.
  • the horizontal axis indicates the hydrogen supply amount
  • the vertical axis indicates the condensate pumping amount.
  • the pumping amount map m02 describes the relationship between the amount of hydrogen actually injected from the fuel injection means 42 into the combustion chamber CC and the pumping amount of condensed water by the pumping unit 80.
  • the pumping amount of the condensed water by the pumping unit 80 increases as the hydrogen supply amount increases.
  • the pumping amount map m02 is stored in the storage unit 50b.
  • the pumping amount control unit 551 obtains the pumping amount of condensed water by the pumping unit 80 from the supply amount of hydrogen actually injected into the combustion chamber CC based on the pumping amount map m02.
  • the relationship between the amount of hydrogen actually injected from the fuel injection means 42 into the combustion chamber CC and the amount of condensed water generated is that the amount of condensed water generated is relatively increased when the amount of hydrogen supplied is relatively increased. As the amount of hydrogen increases and the amount of hydrogen supplied decreases relatively, the amount of condensed water generated also decreases. For this reason, the pumping amount control unit 551 estimates and acquires the amount of condensed water generated based on the amount of hydrogen actually injected from the fuel injection means 42 into the combustion chamber CC, and based on the amount of condensed water generated.
  • a map that is substantially the same as the pumping amount map m02 (a pumping amount map in which the horizontal axis indicates the amount of condensed water generated) may be used.
  • this working gas circulation engine 501 hydrogen supplied to the combustion chamber CC at a certain time burns in the combustion chamber CC, and water vapor generated by this combustion is separated by the condenser 60 and stored as condensed water. There is a certain time delay before the tank 70 is reached. That is, in the working gas circulation engine 501, the supply time when hydrogen is supplied to the combustion chamber CC, and the condensed water corresponding to the supply amount of hydrogen supplied at this supply time actually reaches the condensed water storage tank 70. A predetermined response delay time occurs between the time when the condensed water is reached. The response delay time at the time when the condensed water reaches the supply time varies depending on the flow velocity of the gas flowing through the circulation path 20.
  • the flow rate of the gas flowing through the circulation path 20 varies according to the engine speed of the working gas circulation engine 501. That is, the flow rate of the gas flowing through the circulation path 20 increases as the engine speed increases, and decreases as the engine speed decreases. As a result, the response delay time of the condensed water arrival time with respect to the supply time becomes shorter as the engine speed increases and the flow velocity of the gas flowing through the circulation path 20 increases, and the engine speed decreases and the circulation path 20 decreases. As the flow rate of the gas flowing through decreases, it becomes longer.
  • the pumping amount control unit 551 of the present embodiment further acquires the engine speed of the working gas circulation engine 501 and controls the driving of the condensate pump 82 based on the engine speed, thereby controlling the pumping amount of the condensed water.
  • the pumping amount of the condensed water is controlled based on the response delay time at the time when the condensed water reaches the condensed water.
  • the pumping amount control unit 551 calculates and acquires the engine speed, which is the speed of the crankshaft 19, based on the crank angle detected by the crank angle sensor 51 as described above. And the pumping amount control part 551 calculates
  • the horizontal axis indicates the engine speed
  • the vertical axis indicates the response delay time.
  • the response delay time map m03 describes the relationship between the engine speed acquired by the pumping amount control unit 551 and the response delay time when the condensed water reaches the condensate relative to the supply time.
  • the response delay time map m03 In this response delay time map m03, the response delay time decreases as the engine speed increases.
  • the response delay time map m03 is stored in the storage unit 50b.
  • the pumping amount control unit 551 obtains a response delay time from the engine speed based on the response delay time map m03.
  • the pumping amount control unit 551 pumps the condensate so that it becomes the pumping amount of the condensed water based on the supply amount of hydrogen actually injected into the combustion chamber CC after the response delay time obtained based on the engine speed has elapsed.
  • the drive of the condensed water pump 82 of the part 80 is controlled.
  • the working gas circulation engine 501 of the present embodiment is configured so that the condensed water corresponding to the supply time when hydrogen is supplied to the combustion chamber CC and the supply amount of hydrogen supplied at this supply time is stored in the condensed water storage tank 70.
  • the condensate pumping amount can be controlled based on the response delay time between the condensate arrival time and the condensate water arrival point at which the condensate water is supplied by the pumping unit 80 according to the actual hydrogen supply amount to the combustion chamber CC.
  • the predictive control of the pumping amount can be executed accurately. That is, the working gas circulation engine 501 of the present embodiment is configured to reduce the amount of condensed water pumped by the pumping unit 80 with respect to the amount of condensed water generated according to the amount of hydrogen actually injected into the combustion chamber CC. Since the responsiveness can be followed accurately, the condensed water storage tank 70 can be downsized as a result.
  • This control routine is repeatedly executed at a control cycle of several ms to several tens of ms.
  • the pumping amount control unit 551 of the electronic control unit 50 actually starts from the fuel injection unit 42 based on the valve opening period of the fuel injection unit (fuel injection valve) 42 or the flow rate of hydrogen detected by the fuel flow meter 45, for example.
  • a supply amount of hydrogen injected into the combustion chamber CC is acquired (S300).
  • the pumping amount control unit 551 calculates the pumping amount of condensed water by the pumping unit 80 from the hydrogen supply amount acquired in S300 (S301).
  • the pumping amount control unit 551 calculates and acquires the engine speed based on the crank angle detected by the crank angle sensor 51, and calculates the response delay time from the engine speed based on the response delay time map m03, for example. Calculate (S302).
  • the pumping amount control unit 551 stores the pumping amount calculated in S301 in the storage unit 50b as the pumping amount after the response delay time calculated in S302 (S303).
  • the pumping amount control unit 551 calls the current pumping amount from the storage unit 50b (S304).
  • the pumping amount control unit 551 controls the driving of the condensed water pump 82 of the pumping unit 80 based on the current pumping amount called in S304, and changes the pumping amount by the condensed water pump 82 (S305). End the current control cycle and move to the next control cycle.
  • the working gas circulation engine 501 has the condensed water stored in the condensed water storage tank 70 higher than the atmospheric pressure by the pumping unit 80.
  • the condensate stored in the condensate storage tank 70 is steamed because the condensed water pumped by the heat exchanger 90 is evaporated using the exhaust heat of the exhaust gas.
  • the mounting property of the working gas circulation engine 501 on the vehicle can be improved, and the condensed water separated by the condenser 60 can be appropriately processed.
  • the working gas circulation engine 501 is configured such that the pumping amount control unit 551 condenses the pumping unit 80 based on the amount of condensed water generated. Since the driving of the water pump 82 is controlled and the amount of condensed water pumped by the condensed water pump 82 of the pressure feeding unit 80 is controlled, the condensed water in the condensed water storage tank 70 is heated with the amount of pumping according to the amount of condensed water generated. Since it can be pumped toward the exchanger 90 and evaporated, the amount of condensed water stored in the condensed water storage tank 70 can be reduced. As a result, the working gas circulation engine 501 can reduce the capacity of the condensed water storage tank 70 after properly treating the condensed water separated by the condenser 60, and thus the working gas circulation engine 501. Can be further improved.
  • the pumping amount control unit 551 is based on oxygen or hydrogen supplied to the combustion chamber CC, here, the supply amount of hydrogen.
  • the pumping amount of the condensed water by the pumping unit 80 is controlled. Therefore, the working gas circulation engine 501 is a sensor that directly detects the amount of condensed water actually generated, such as the flow rate sensor 54 (see FIG. 5) and the water level sensor 55 (see FIG. 7) described above.
  • the condensate water by the pressure feed unit 80 is based on the supply amount of hydrogen actually injected from the fuel injection means 42 into the combustion chamber CC as a value corresponding to the amount of condensed water generated by the pressure feed amount control unit 551.
  • the pumping amount of the condensed water by the pumping unit 80 can be controlled based on the amount of condensed water generated.
  • the working gas circulation engine 501 can suppress the number of parts constituting the working gas circulation engine 501 and can reduce the manufacturing cost of the working gas circulation engine 501.
  • the pumping amount control unit 551 controls the pumping amount of the condensed water by the pumping unit 80 based on the engine load and the engine speed. To do. Therefore, the working gas circulation engine 501 has a response delay time corresponding to the engine speed by the pumping amount control unit 551 controlling the pumping amount of the condensed water by the pumping unit 80 based on the engine load and the engine speed. After the elapse of time, the driving of the condensate pump 82 of the pumping unit 80 can be controlled so that the engine load, for example, the condensate pumping amount based on the hydrogen supply amount, can be controlled.
  • the amount of condensed water pumped by the pumping section 80 can be accurately followed with high response to the amount of condensed water generated according to the amount of hydrogen injected into the combustion chamber CC.
  • the condensed water storage tank 70 can be reduced in size.
  • the pumping amount control unit 551 is actually connected to the fuel injection means 42 based on the valve opening period of the fuel injection means (fuel injection valve) 42 or the hydrogen flow rate detected by the fuel flow meter 45. Although it demonstrated as what acquires the supply amount of the hydrogen injected into the combustion chamber CC, it is not restricted to this.
  • FIG. 14 is a schematic configuration diagram of a working gas circulation engine according to the third modification of the present invention.
  • the working gas circulation engine 501A includes a pressure sensor 56A as pressure detecting means, as shown in FIG.
  • the pressure sensor 56 ⁇ / b> A is provided in the fuel storage tank 41 and detects the pressure in the fuel storage tank 41.
  • the pressure sensor 56 ⁇ / b> A transmits a detection signal to the electronic control device 50.
  • the pumping amount control unit 551 calculates and acquires the supply amount of hydrogen actually injected from the fuel injection means 42 into the combustion chamber CC based on the pressure in the fuel storage tank 41 detected by the pressure sensor 56A. It may be. That is, the pumping amount control unit 551 is actually injected from the fuel injection means 42 into the combustion chamber CC based on the fluctuation amount of the pressure in the fuel storage tank 41 detected by the pressure sensor 56A, that is, the reduction amount.
  • the supply amount of hydrogen can be calculated. Even in this case, the working gas circulation engine 501A directly determines the amount of condensed water actually generated, such as the flow rate sensor 54 (see FIG. 5) and the water level sensor 55 (see FIG. 7) described above.
  • the pressure feed control unit 551 determines the value corresponding to the amount of condensed water generated based on the supply amount of hydrogen actually injected from the fuel injection means 42 into the combustion chamber CC. As a result, the amount of condensed water pumped by the pumping unit 80 can be controlled based on the amount of condensed water generated.
  • FIG. 15 is a schematic configuration diagram of a working gas circulation engine according to Embodiment 6 of the present invention.
  • the working gas circulation engine according to the sixth embodiment has substantially the same configuration as the working gas circulation engine according to the first embodiment, but is different from the working gas circulation engine according to the first embodiment in that it includes waste heat recovery means. Different.
  • the working gas circulation engine 601 includes an expander 610 as waste heat recovery means, as shown in FIG.
  • the expander 610 collects the energy of water vapor generated by evaporating condensed water by the heat exchanger 90 as kinetic energy.
  • the expander 610 is provided in the atmosphere opening passage 83 that forms the condensed water passage 81.
  • the expander 610 is provided between the heat exchanger 90 in the atmosphere opening passage 83 and the opening on the atmosphere side. As a result, the expander 610 is introduced with water vapor generated in the heat exchanger 90 through the atmosphere opening passage 83.
  • the expander 610 expands the water vapor to work, that is, rotates the output rotation member 611 by the expansion of the water vapor, thereby converting the energy of the water vapor into the rotational kinetic energy of the output rotation member 611. . That is, the expander 610 recovers the energy of water vapor generated in the heat exchanger 90, converts it into mechanical energy, and outputs the mechanical energy as the rotational output of the output rotating member 611.
  • the output rotation member 611 is connected to, for example, a rotation shaft of a crankshaft 19 or a generator (not shown), and the rotation output of the output rotation member 611 is transmitted to the rotation shaft of the crankshaft 19 or a generator (not shown). Is done.
  • the working gas circulation engine 601 configured as described above collects the energy of water vapor generated by the expander 610 in the heat exchanger 90 as kinetic energy, and uses the recovered rotational output of the output rotating member 611 as the crankshaft 19 or the like. By transmitting to the rotating shaft of the generator (not shown), for example, the engine output by the engine body 10 for obtaining the output required for the working gas circulation engine 601 as a whole can be relatively reduced. The fuel consumption rate can be suppressed, and the cruising range can be extended.
  • the working gas circulation engine 601 can relatively reduce the engine output by the engine body 10 to obtain the output required for the working gas circulation engine 601 as a whole.
  • the working gas circulation engine 601 Since the engine output by the engine body 10 for obtaining the output required for the entire 601 can be made relatively small, the amount of water vapor generated by the combustion of hydrogen and oxygen can be suppressed. The amount of condensed water generated can be suppressed. As a result, the working gas circulation engine 601 can relatively reduce the capacities of the condenser 60, the radiator 63, and the condensed water storage tank 70, thereby improving the mountability of the working gas circulation engine 601 on the vehicle. be able to.
  • the working gas circulation engine 601 is configured so that the condensed water stored in the condensed water storage tank 70 is higher than the atmospheric pressure by the pumping unit 80.
  • the condensate stored in the condensate storage tank 70 is steamed because the condensed water pumped by the heat exchanger 90 is evaporated using the exhaust heat of the exhaust gas.
  • the mounting property of the working gas circulation engine 601 on the vehicle can be improved, and the condensed water separated by the condenser 60 can be appropriately treated.
  • the expander 610 that recovers the energy of water vapor generated by evaporating condensed water by the heat exchanger 90 as kinetic energy.
  • the working gas circulation engine 601 collects the energy of water vapor generated by the expander 610 in the heat exchanger 90 as kinetic energy, and uses the collected rotational output of the output rotating member 611 as a crankshaft 19 or a generator (not shown).
  • the engine output by the engine body 10 for obtaining the output required for the working gas circulation engine 601 as a whole can be made relatively small, so the fuel consumption rate is suppressed.
  • the cruising distance can be increased, the amount of water vapor and condensed water generated can be suppressed, and the capacities of the condenser 60, radiator 63, and condensed water storage tank 70 can be made relatively small. Therefore, the mounting property of the working gas circulation engine 601 on the vehicle can be improved.
  • FIG. 16 is a schematic schematic configuration diagram of a working gas circulation engine according to Embodiment 7 of the present invention
  • FIG. 17 illustrates condensate temperature control of the working gas circulation engine according to Embodiment 7 of the present invention. It is a flowchart.
  • the working gas circulation engine according to the seventh embodiment has substantially the same configuration as the working gas circulation engine according to the sixth embodiment, but is different from the working gas circulation engine according to the sixth embodiment in that it includes a heat transfer means. .
  • symbol is attached
  • the working gas circulation engine 701 includes a heat transfer unit 720 as heat transfer means, as shown in FIG.
  • the heat transfer unit 720 moves the heat of water vapor via the expander 610 to the condensed water stored in the condensed water storage tank 70 under a predetermined condition.
  • the heat transfer unit 720 includes a branch passage 721, a heat exchanger 722, a flow rate adjustment valve 723, a heat medium circulation path 724, a heat medium pump 725, and a circulation path heat dissipation section 726. Is done.
  • the branch passage 721 is a water vapor passage that branches off from the atmosphere opening passage 83 forming the condensed water passage 81.
  • One end of the branch passage 721 is connected between the expander 610 of the atmosphere release passage 83 and the opening on the atmosphere side, and the other end opens to the atmosphere.
  • the heat exchanger 722 exchanges heat between water vapor flowing through the branch passage 721 and a heat exchange medium (hereinafter referred to as a heat medium) flowing through the heat medium circulation path 724.
  • the heat exchanger 722 is provided in the branch passage 721.
  • the heat exchanger 722 is connected so that the heat medium circulation path 724 passes through the inside.
  • the flow rate adjusting valve 723 adjusts the flow rate of water vapor flowing through the branch passage 721.
  • the flow rate adjustment valve 723 is provided between one end of the branch passage 721 connected to the atmosphere opening passage 83 and the heat exchanger 722.
  • the flow rate adjustment valve 723 is controlled by the electronic control unit 50 so that the opening thereof is controlled, so that the flow rate of water vapor introduced into the heat exchanger 722 through the branch passage 721 can be adjusted.
  • the heat medium circulation path 724 circulates the heat medium in the heat exchanger 722, and the heat medium can flow.
  • the heat medium circulation path 724 is a closed annular path, and the inside is filled with the heat medium.
  • the heat medium circulation path 724 is provided so as to pass through the inside of the heat exchanger 722.
  • the heat medium pump 725 is provided on the path of the heat medium circulation path 724, and the heat medium of the heat medium circulation path 724 is driven in the heat medium circulation path 724 in a predetermined circulation direction by driving the heat medium pump 725. Can be circulated in.
  • the driving of the heat medium pump 725 is controlled by the electronic control device 50, and thus the circulation amount of the heat medium that is circulated through the heat medium circulation path 724 and introduced into the heat exchanger 722 can be adjusted.
  • the circulation path heat radiation part 726 is provided on the route of the heat medium circulation path 724.
  • the circulation path heat radiating unit 726 is configured to come into contact with the condensed water stored in the condensed water storage tank 70.
  • the circulation path heat radiation part 726 is formed so as to meander a part of the heat medium circulation path 724 in the condensed water storage tank 70. Thereby, the circulation path heat radiation part 726 can secure a sufficient contact area with the condensed water stored in the condensed water storage tank 70, that is, a heat radiation area, and can efficiently radiate heat to the condensed water. it can.
  • the flow rate adjustment valve 723 adjusts the flow rate of water vapor flowing through the branch passage 721 so that the water vapor is introduced into the heat exchanger 722, and the heat medium pump 725 is driven to heat the heat medium circulation path 724.
  • the medium circulates between the heat exchanger 722 and the circulation path heat radiating unit 726 the heat of the steam via the expander 610 is transferred to the condensed water storage tank 70 via the heating medium circulating in the heating medium circulation path 724. It can be moved to the stored condensed water.
  • the heat transfer unit 720 exchanges heat with the water vapor via the expander 610 in the heat exchanger 722 by the heat medium circulating in the heat medium circulation path 724 and absorbs heat from the water vapor, so that the temperature of the heat medium Rises.
  • the heat transfer unit 720 absorbs the heat of the water vapor and the heat medium whose temperature has risen circulates in the heat medium circulation path 724, and the condensed water and heat stored in the condensed water storage tank 70 in the circulation path heat radiation part 726.
  • the condensed water absorbs the heat of the heat medium, so that the temperature of the condensed water rises.
  • the heat transfer unit 720 recovers the heat from the water vapor via the expander 610 and raises the temperature of the condensed water stored in the condensed water storage tank 70 by the recovered heat. Note that the water vapor exchanged with the heat medium circulating in the heat medium circulation path 724 by the heat exchanger 722 is released to the atmosphere from the opening at the other end of the branch path 721.
  • the working gas circulation engine 701 of the present embodiment includes a temperature sensor 57 as temperature detecting means, and a functionally conceptual electronic control unit (ECU) 50 is provided with a heat transfer unit control unit 752. Yes.
  • ECU electronice control unit
  • the temperature sensor 57 is provided inside the condensed water storage tank 70 and detects the temperature of the condensed water stored in the condensed water storage tank 70.
  • the temperature sensor 57 transmits a detection signal to the electronic control device 50.
  • the heat transfer unit controller 752 controls the drive of the heat transfer unit 720, and here controls the drive of the flow rate adjustment valve 723 and the heat medium pump 725 of the heat transfer unit 720. And the heat transfer part control part 752 of this embodiment condenses the heat
  • the heat transfer unit control unit 752 performs heat transfer unit 720.
  • the flow rate adjustment valve 723 and the heat medium pump 725 are driven to move the heat of the water vapor via the expander 610 to the condensed water stored in the condensed water storage tank 70.
  • the condensed water stored in the condensed water storage tank 70 is heated by heat recovered from the water vapor via the expander 610 by the heat transfer unit 720 when the temperature is lower than a predetermined temperature set in advance. The temperature rises and is preheated.
  • the working gas circulation engine 701 when the condensed water stored in the condensed water storage tank 70 is at a low temperature that is equal to or lower than a preset predetermined temperature, the working gas circulation engine 701 is not allowed to reach the heat exchanger 90 before the condensed water reaches the heat exchanger 90. By preheating, the preheated condensed water can be efficiently evaporated in the heat exchanger 90. Further, since the temperature of the water vapor introduced into the expander 610 relatively increases, the working gas circulation engine 701 can improve the efficiency of waste heat recovery in the expander 610, that is, the expansion The output of the machine 610 can be increased.
  • the working gas circulation engine 701 can further reduce the engine output by the engine body 10 for obtaining the output required for the working gas circulation engine 701 as a whole, for example. Further, the cruising distance can be further increased and the generation amount of water vapor and the generation amount of condensed water can be further suppressed, and the capacities of the condenser 60, the radiator 63, and the condensed water storage tank 70 can be further increased. Since it can be made small, the mountability of the working gas circulation engine 701 on the vehicle can be further improved.
  • the heat transfer unit controller 752 controls driving of the flow rate adjusting valve 723 and the heat medium pump 725 of the heat transfer unit 720, and the condensed water stored in the condensed water storage tank 70 is controlled.
  • the heat transfer unit 720 adjusts the output of the expander 610 by adjusting the temperature and, in turn, the temperature of the water vapor introduced into the expander 610, and the working gas circulation engine 701 as a whole. It can also function as an adjusting device that adjusts the output of the.
  • This control routine is repeatedly executed at a control cycle of several ms to several tens of ms.
  • the heat transfer unit controller 752 of the electronic control unit 50 acquires the temperature of the condensed water stored in the condensed water storage tank 70 detected by the temperature sensor 57 (S400).
  • the heat transfer unit control unit 752 determines whether or not the temperature of the condensed water acquired in S400 is higher than a predetermined temperature set in advance (S401).
  • the heat transfer unit control unit 752 ends the current control cycle and proceeds to the next control cycle. To do.
  • the heat transfer unit control unit 752 drives the heat medium pump 725 to control it to ON and adjust the flow rate.
  • the valve 723 is driven and opened to a predetermined opening degree corresponding to the temperature of the condensed water (S402), the current control cycle is terminated, and the next control cycle is started.
  • the working gas circulation engine 701 has the condensed water stored in the condensed water storage tank 70 higher than the atmospheric pressure by the pumping unit 80.
  • the condensate stored in the condensate storage tank 70 is steamed because the condensed water pumped by the heat exchanger 90 is evaporated using the exhaust heat of the exhaust gas.
  • the mounting property of the working gas circulation engine 701 on the vehicle can be improved, and the condensed water separated by the condenser 60 can be appropriately treated.
  • the working gas circulation engine 701 collects energy of water vapor generated by the expander 610 in the heat exchanger 90 as kinetic energy. Then, the rotation output of the collected output rotation member 611 is transmitted to the rotation shaft of the crankshaft 19 or a generator (not shown), for example, an engine for obtaining the output required for the entire working gas circulation engine 701 Since the engine output by the main body 10 can be made relatively small, the fuel consumption rate can be suppressed and the cruising distance can be increased, and the amount of water vapor and condensed water can be suppressed. 60, the capacity of the radiator 63, and the condensed water storage tank 70 can be relatively reduced. It is possible to improve the mountability to the vehicle.
  • the temperature sensor 57 that detects the temperature of the condensed water stored in the condensed water storage tank 70, and the temperature sensor 57 detects the temperature.
  • a heat transfer unit 720 that moves the heat of water vapor via the expander 610 to the condensed water stored in the condensed water storage tank 70 when the temperature is equal to or lower than a predetermined temperature set in advance. Therefore, when the condensed water stored in the condensed water storage tank 70 is at a low temperature that is equal to or lower than a predetermined temperature set in advance, the working gas circulation engine 701 uses the condensed water stored in the condensed water storage tank 70.
  • the working gas circulation engine 701 can further suppress the fuel consumption rate and further extend the cruising distance, and can further suppress the generation amount of water vapor and the generation amount of condensed water. Since the capacity
  • the working gas circulation engine 701 adjusts the heat amount of water vapor transferred to the condensed water stored in the condensed water storage tank 70 by the heat transfer unit 720, so that the output of the expander 610 and the working gas circulation engine are adjusted.
  • the output of the entire 701 can be adjusted.
  • FIG. 18 is a schematic schematic configuration diagram of a working gas circulation engine according to an eighth embodiment of the present invention
  • FIG. 19 illustrates condensate temperature and water level control of the working gas circulation engine according to the eighth embodiment of the present invention. It is a flowchart to explain.
  • the working gas circulation engine according to the eighth embodiment has substantially the same configuration as the working gas circulation engine according to the seventh embodiment, but the structure of the heat transfer means is different from that of the working gas circulation engine according to the seventh embodiment.
  • the working gas circulation engine 801 includes a heat transfer unit 820 as heat transfer means, as shown in FIG.
  • the heat transfer unit 820 moves the heat of water vapor via the expander 610 to the condensed water stored in the condensed water storage tank 870 under predetermined conditions.
  • the heat transfer unit 820 of the present embodiment directly introduces the water vapor via the expander 610 into the condensed water storage tank 870, so that the heat of the water vapor together with the water vapor via the expander 610 is transferred to the condensed water storage tank 870. Move to stored condensate.
  • the heat transfer unit 820 of this embodiment includes a branch passage 821 and a flow rate adjustment valve 822.
  • the branch passage 821 is a water vapor passage that branches off from the open air passage 83 forming the condensed water passage 81.
  • One end of the branch passage 821 is connected between the expander 610 of the atmosphere opening passage 83 and the opening on the atmosphere side, and the other end opens inside a condensed water storage tank 870 as condensed water storage means.
  • the flow rate adjustment valve 822 adjusts the flow rate of water vapor flowing through the branch passage 821.
  • the flow rate adjustment valve 822 is controlled by the electronic control unit 50 so that the opening thereof is controlled, and thereby the flow rate of the water vapor introduced into the condensed water storage tank 870 through the branch passage 821 can be adjusted. it can.
  • the heat transfer unit 820 adjusts the flow rate of the water vapor flowing through the branch passage 821 by the flow rate adjustment valve 822 and introduces the water vapor into the condensed water storage tank 870 so that the water vapor via the expander 610 is stored in the condensed water. It is directly introduced into the tank 870, and the heat of the water vapor can be transferred to the condensed water stored in the condensed water storage tank 870 together with the water vapor itself.
  • the heat transfer unit 820 directly introduces the water vapor that has passed through the expander 610 through the branch passage 821 into the condensate water storage tank 870, so that the condensate water and water vapor stored in the condensate water storage tank 870 Heat exchange and the condensed water absorbs the heat of the water vapor, so that the temperature of the condensed water rises. That is, the heat transfer unit 820 directly introduces the water vapor via the expander 610 into the condensed water storage tank 870, so that the heat from the water vapor via the expander 610 is obtained by the condensed water in the condensed water storage tank 870. Waste heat is recovered, and the temperature of the condensed water is increased by the recovered heat.
  • the heat transfer unit 820 directly introduces the water vapor that has passed through the expander 610 via the branch passage 821 into the condensed water storage tank 870, and the condensed water and the water vapor stored in the condensed water storage tank 870 are heated.
  • the temperature of the water vapor is lowered, and a part of the water vapor is liquefied and condensed.
  • the water level of the condensed water stored in the condensed water storage tank 870 rises as a part of the water vapor is liquefied and condensed.
  • the condensed water storage tank 870 of this embodiment has the discharge port 871 which discharge
  • the water vapor introduced into the condensed water storage tank 870 through the branch passage 821 and not liquefied in the condensed water storage tank 870 is discharged to the atmosphere through the discharge port 871.
  • the working gas circulation engine 801 of the present embodiment includes a water level sensor 55 as a water level detection unit and a temperature sensor 57 as a temperature detection unit, and is functionally conceptually an electronic control unit (ECU) 50.
  • the heat transfer unit control unit 852 is provided.
  • the heat transfer unit controller 852 controls the drive of the heat transfer unit 820, and here controls the drive of the flow rate adjustment valve 822 of the heat transfer unit 820. Then, the heat transfer unit control unit 852 of this embodiment drives the flow rate adjustment valve 822 of the heat transfer unit 820 under a predetermined condition, so that the water vapor via the expander 610 is stored in the condensed water storage tank 870. Move to condensed water.
  • the heat transfer unit control unit 852 when the temperature of the condensed water stored in the condensed water storage tank 870 detected by the temperature sensor 57 is equal to or lower than a predetermined temperature set in advance, The flow rate regulating valve 822 is driven, and the water vapor that has passed through the expander 610 is directly introduced into the condensed water storage tank 870 via the branch passage 821.
  • the heat transfer unit 820 directly introduces water vapor via the expander 610. The temperature rises and is preheated by the heat of water vapor.
  • the working gas circulation engine 801 does not reach the heat exchanger 90 before the condensed water reaches the heat exchanger 90.
  • the working gas circulation engine 801 can improve the efficiency of waste heat recovery in the expander 610 since the temperature of the water vapor introduced into the expander 610 is relatively increased. The output of the machine 610 can be increased.
  • the working gas circulation engine 801 can further reduce the engine output by the engine main body 10 for obtaining the output required for the working gas circulation engine 801 as a whole, for example, so that the fuel consumption rate can be reduced. Further, the cruising distance can be further increased and the generation amount of water vapor and the generation amount of condensed water can be further suppressed, and the capacities of the condenser 60, the radiator 63, and the condensed water storage tank 870 can be further relatively increased. Since it can be made small, the mountability of the working gas circulation engine 801 on the vehicle can be further improved.
  • the heat transfer unit control unit 852 controls the driving of the flow rate adjustment valve 822 of the heat transfer unit 820 to adjust the temperature of the condensed water stored in the condensed water storage tank 870, As a result, the heat transfer unit 820 adjusts the output of the expander 610 by adjusting the temperature of water vapor introduced into the expander 610, and further adjusts the output of the working gas circulation engine 801 as a whole. It can also function as an adjusting device.
  • the heat transfer unit controller 852 of the present embodiment performs heat transfer when the water level of the condensed water stored in the condensed water storage tank 870 detected by the water level sensor 55 is equal to or lower than a predetermined water level set in advance.
  • the flow control valve 822 of the unit 820 is driven, and the water vapor that has passed through the expander 610 is directly introduced into the condensed water storage tank 870 via the branch passage 821.
  • water vapor is directly introduced by the heat transfer unit 820 via the expander 610.
  • part of the water vapor liquefies and condenses and the water level rises.
  • the working gas circulation engine 801 passes the expander 610 through the expander 610. Steam is directly introduced and a part of the steam is liquefied and condensed, and its water level rises. For example, it is possible to prevent depletion of condensed water in the condensed water storage tank 870, and the condensed water pump 82 sucks gas. This can be prevented.
  • This control routine is repeatedly executed at a control cycle of several ms to several tens of ms.
  • the heat transfer unit controller 852 of the electronic control unit 50 is stored in the condensed water storage tank 870 detected by the temperature sensor 55 and the temperature of the condensed water stored in the condensed water storage tank 870 detected by the temperature sensor 57.
  • the level of the condensed water is acquired (S500).
  • the heat transfer unit control unit 852 determines whether or not the temperature of the condensed water acquired in S500 is higher than a predetermined temperature set in advance (S501).
  • the heat transfer unit control unit 852 sets the predetermined water level of the condensed water acquired in S500. It is determined whether it is higher than the water level (S502).
  • the heat transfer unit control unit 852 ends the current control cycle and proceeds to the next control cycle. To do.
  • the heat transfer unit control unit 852 drives the flow rate adjustment valve 822 to respond to the temperature of the condensed water.
  • the valve is opened to a predetermined opening degree (S503), the current control cycle is terminated, and the next control cycle is started.
  • the heat transfer unit control unit 852 drives the flow control valve 822 to respond to the water level of the condensed water.
  • the valve is opened to a predetermined opening degree (S503), the current control cycle is terminated, and the next control cycle is started.
  • the working gas circulation engine 801 has the condensed water stored in the condensed water storage tank 870 higher than the atmospheric pressure by the pumping unit 80.
  • the condensate stored in the condensate storage tank 870 is steamed because the condensed water pumped by the heat exchanger 90 is evaporated using the exhaust heat of the exhaust gas.
  • the mounting property of the working gas circulation engine 801 on the vehicle can be improved, and the condensed water separated by the condenser 60 can be appropriately treated.
  • the working gas circulation engine 801 collects the energy of water vapor generated by the expander 610 in the heat exchanger 90 as kinetic energy. Then, by transmitting the rotation output of the collected output rotation member 611 to the rotation shaft of the crankshaft 19 or a generator (not shown), for example, an engine for obtaining an output required for the entire working gas circulation engine 801 Since the engine output by the main body 10 can be made relatively small, the fuel consumption rate can be suppressed and the cruising distance can be increased, and the amount of water vapor and condensed water can be suppressed. 60, the capacity of the radiator 63, and the condensed water storage tank 870 can be relatively reduced, so that the working gas circulation engine 8 It is possible to improve the mountability to the first vehicle.
  • the temperature sensor 57 that detects the temperature of the condensed water stored in the condensed water storage tank 870, and the temperature sensor 57 detects the temperature.
  • a heat transfer unit 820 that moves the heat of the water vapor via the expander 610 to the condensed water stored in the condensed water storage tank 870 when the temperature is equal to or lower than a predetermined temperature set in advance.
  • the working gas circulation engine 801 uses the condensed water stored in the condensed water storage tank 870 to Since the temperature rises and is preheated by the heat recovered from the water vapor via the expander 610 by the heat transfer unit 820, the temperature of the water vapor introduced into the expander 610 is relatively increased to increase the output of the expander 610. Can be increased. As a result, the working gas circulation engine 801 can further suppress the fuel consumption rate and further extend the cruising distance, and can further suppress the generation amount of water vapor and the generation amount of condensed water.
  • the working gas circulation engine 801 adjusts the amount of water vapor transferred to the condensed water stored in the condensed water storage tank 870 by the heat transfer unit 820, so that the output of the expander 610 and the working gas circulation engine can be adjusted. The output of the whole 801 can be adjusted.
  • the working gas circulation engine 801 includes the water level sensor 55 that detects the water level of the condensed water stored in the condensed water storage tank 870, and includes the heat transfer unit 820.
  • the water level detected by the water level sensor 55 is equal to or lower than a predetermined water level set in advance
  • the water vapor through the expander 610 is introduced into the condensed water stored in the condensed water storage tank 870. Therefore, the working gas circulation engine 801 passes the expander 610 by the heat transfer unit 820 when the water level of the condensed water stored in the condensed water storage tank 870 is a low water level equal to or lower than a predetermined water level set in advance.
  • the working gas circulation engine 801 can prevent depletion of the condensed water in the condensed water storage tank 870, for example, by increasing the water level of the condensed water stored in the condensed water storage tank 870. It is possible to prevent the water pump 82 from sucking gas.
  • the working gas circulation engine according to the above-described embodiment of the present invention is not limited to the above-described embodiment, and various modifications can be made within the scope described in the claims.
  • the working gas circulation engine according to the embodiment of the present invention may be configured by combining a plurality of the embodiments described above.
  • the working gas circulation engine according to the embodiment of the present invention includes the working gas circulation engine 501 according to the fifth embodiment (see FIG. 10) and the working gas circulation engine 801 according to the eighth embodiment (see FIG. 18). You may comprise by combining. That is, the working gas circulation engine 801A according to the fourth modification of the present invention shown in FIG.
  • a pumping amount control unit 551 as a pumping amount control unit and a heat transfer unit control unit 852 may be provided.
  • the working gas circulation engine has been described as providing the fuel injection means 42 so that the fuel is directly injected into the combustion chamber CC.
  • the fuel injection means 42 injects the fuel into the intake port 11b. It may be attached to the cylinder head 11 as much as possible. That is, the working gas circulation engine of the present invention described above may be applied to a so-called port injection working gas circulation engine, and even in this case, the condensed water can be appropriately processed. .
  • the working gas circulation engine has been exemplified as a fuel that diffuses and burns hydrogen (H 2 ) as a fuel.
  • a so-called spark ignition combustion is performed by igniting a fuel with a spark plug (not shown).
  • the fuel may be ignited with a spark plug to assist ignition and diffuse combustion may be used. That is, the working gas circulation engine of the present invention described above may be applied to working gas circulation engines having different combustion forms, and even in this case, the condensed water can be appropriately processed.
  • the working gas circulation engine according to the present invention can appropriately process condensed water, and circulates the working gas contained in the exhaust gas from the exhaust side to the intake side of the combustion chamber.
  • the present invention is suitable for various working gas circulation engines that can be supplied to the combustion chamber again.

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Abstract

An operating gas circulation type engine has a combustion chamber (CC) into which an oxidizing agent, fuel which generates water vapor when combusted together with the oxidizing agent, and operating gas which has a higher specific heat ratio than air are supplied, in which the operating gas can expand as the fuel combusts, and which can discharge the water vapor and operating gas as exhaust gas after the combustion of the fuel, a circulating route (20) capable of circulating the operating gas, contained in the exhaust gas, from the exhaust side to the intake side of the combustion chamber (CC) and supplying the operating gas again to the combustion chamber, a condensing means (60) provided in the circulating route (20) and condensing water vapor contained in the exhaust gas to turn the water vapor into condensed water, a condensed water containing means (70) capable of containing the condensed water, a pumping means (80) for pumping the condensed water, contained in the condensed water containing means (70), by higher pressure than the atmospheric pressure, and evaporating means (90) for evaporating the condensed water, pumped by the pumping means (80), by exhaust heat of the exhaust gas. Thus, the condensed water can be appropriately processed.

Description

作動ガス循環型エンジンWorking gas circulation engine
 本発明は、作動ガス循環型エンジンに関し、特に排気ガス中に含まれる作動ガスを燃焼室の排気側から吸気側に循環させ再び燃焼室に供給可能な作動ガス循環型エンジンに関するものである。 The present invention relates to a working gas circulation engine, and more particularly to a working gas circulation engine in which working gas contained in exhaust gas is circulated from the exhaust side to the intake side of the combustion chamber and can be supplied to the combustion chamber again.
 従来のエンジンとして、排気ガス中に含まれる作動ガスを燃焼室の排気側から吸気側に循環させ再び燃焼室に供給可能な、いわゆる、閉サイクルエンジンである作動ガス循環型エンジンが知られている。このような作動ガス循環型エンジンは、酸化剤としての酸素と、燃料としての水素と、空気より比熱比の高い作動ガスとが供給される燃焼室と、作動ガスを燃焼室の排気側から吸気側に循環させ再び燃焼室に供給可能な循環経路とを備え、燃焼室にて水素の燃焼に伴って作動ガスが熱膨張することで動力を発生させると共に、この作動ガスが大気へと放出されることなく循環経路を介して再び燃焼室に供給される。 As a conventional engine, a working gas circulation engine that is a so-called closed-cycle engine that can circulate the working gas contained in the exhaust gas from the exhaust side of the combustion chamber to the intake side and supply it again to the combustion chamber is known. . Such a working gas circulation engine has a combustion chamber to which oxygen as an oxidant, hydrogen as a fuel, and a working gas having a higher specific heat ratio than air are supplied, and the working gas is sucked from the exhaust side of the combustion chamber. A circulation path that can be circulated to the combustion chamber and re-supplied to the combustion chamber. The working gas is thermally expanded in the combustion chamber as the hydrogen burns, generating power and releasing the working gas to the atmosphere. Without being supplied again to the combustion chamber via the circulation path.
 従来の作動ガス循環型エンジンとしては、例えば、下記の特許文献1に開示された水素エンジンが知られている。特許文献1に記載されている水素エンジンは、燃焼室に酸素と、水素とが供給されると共に、熱効率を高めるべく作動ガスとして、例えば、単原子ガスからなり空気より比熱比が大きいアルゴンが循環されている。この作動ガス循環型エンジンは、燃焼室内での水素の燃焼によってアルゴンを熱膨張させ、これによりピストンを押し下げて動力を発生させる。 As a conventional working gas circulation engine, for example, a hydrogen engine disclosed in Patent Document 1 below is known. In the hydrogen engine described in Patent Document 1, oxygen and hydrogen are supplied to a combustion chamber, and argon is circulated as a working gas to increase thermal efficiency, for example, composed of a monoatomic gas and having a higher specific heat ratio than air. Has been. In this working gas circulation engine, argon is thermally expanded by combustion of hydrogen in a combustion chamber, and thereby a piston is pushed down to generate power.
 ここで、燃焼室内では水素の燃焼に伴って水素と酸素とが反応(結合)することで水蒸気が発生するので、循環経路には燃焼室からの排気ガスとして、アルゴンと共に水蒸気が排出される。このため、従来の作動ガス循環型エンジンとして特許文献1に記載されている水素エンジンは、3原子からなる分子(3原子分子)でありアルゴンよりも比熱比が小さい水蒸気を液化させ凝縮水として取り除く凝縮器を循環経路上に配設し、作動ガスとしてのアルゴンが循環して再び燃焼室に供給されるように構成することで、熱効率の低下を抑制している。 Here, since hydrogen and oxygen react (combine) with the combustion of hydrogen in the combustion chamber to generate water vapor, the steam is discharged into the circulation path together with argon as exhaust gas from the combustion chamber. For this reason, the hydrogen engine described in Patent Document 1 as a conventional working gas circulation engine is a molecule composed of three atoms (triatomic molecules), which liquefies water vapor having a smaller specific heat ratio than argon and removes it as condensed water. By disposing the condenser on the circulation path so that argon as the working gas circulates and is supplied to the combustion chamber again, a decrease in thermal efficiency is suppressed.
特開平11-93681号公報JP-A-11-93681
 ところで、上述のような特許文献1に記載されている水素エンジンでは、例えば、凝縮器により排気ガスから凝縮された凝縮水を単純にタンクに貯留するだけではタンクの大きさに限界があるため搭載性が悪化するなど種々の問題が生じうることから、この凝縮水を適正に処理する必要がある。 By the way, in the hydrogen engine described in Patent Document 1 as described above, for example, simply storing the condensed water condensed from the exhaust gas by the condenser in the tank is limited because the size of the tank is limited. Since various problems such as deterioration of properties may occur, it is necessary to appropriately treat this condensed water.
 そこで本発明は、凝縮水を適正に処理することができる作動ガス循環型エンジンを提供することを目的とする。 Therefore, an object of the present invention is to provide a working gas circulation engine capable of appropriately treating condensed water.
 上記目的を達成するために、本発明による作動ガス循環型エンジンは、酸化剤と、当該酸化剤との燃焼により水蒸気を生成する燃料と、空気より比熱比の高い作動ガスとが供給され、前記燃料の燃焼に伴って前記作動ガスが膨張可能であると共に前記燃料の燃焼後の排気ガスとして前記水蒸気と前記作動ガスとを排気可能な燃焼室と、前記排気ガス中に含まれる前記作動ガスを前記燃焼室の排気側から吸気側に循環させ再び前記燃焼室に供給可能な循環経路と、前記循環経路に設けられ前記排気ガス中に含まれる前記水蒸気を凝縮して凝縮水とする凝縮手段と、前記凝縮水を貯留可能な凝縮水貯留手段と、前記凝縮水貯留手段に貯留される前記凝縮水を大気圧よりも高い圧力で圧送する圧送手段と、前記圧送手段により圧送された前記凝縮水を前記排気ガスの排気熱により蒸発させる蒸発手段とを備えることを特徴とする。 In order to achieve the above object, a working gas circulation engine according to the present invention is supplied with an oxidizing agent, a fuel that generates water vapor by combustion with the oxidizing agent, and a working gas having a higher specific heat ratio than air, A combustion chamber in which the working gas can expand as the fuel burns and exhausts the water vapor and the working gas as exhaust gas after the combustion of the fuel, and the working gas contained in the exhaust gas. A circulation path that can be circulated from the exhaust side to the intake side of the combustion chamber and re-supplied to the combustion chamber, and a condensing means that is provided in the circulation path and condenses the water vapor contained in the exhaust gas into condensed water. The condensed water storage means capable of storing the condensed water, the pressure feeding means for pumping the condensed water stored in the condensed water storage means at a pressure higher than the atmospheric pressure, and the condensation pumped by the pressure feeding means The characterized in that it comprises an evaporation means for evaporating the exhaust heat of the exhaust gas.
 また、上記作動ガス循環型エンジンにおいて、前記酸化剤は、酸素であり、前記燃料は、水素であってもよい。 In the working gas circulation engine, the oxidant may be oxygen, and the fuel may be hydrogen.
 また、上記作動ガス循環型エンジンにおいて、前記蒸発手段は、前記循環経路を循環する前記作動ガスの循環方向に対して前記凝縮手段より上流側の前記排気ガスの排気熱により前記凝縮水を蒸発させるように構成してもよい。 In the working gas circulation engine, the evaporation means evaporates the condensed water by exhaust heat of the exhaust gas upstream of the condensing means with respect to the circulation direction of the working gas circulating in the circulation path. You may comprise as follows.
 また、上記作動ガス循環型エンジンにおいて、前記圧送手段は、前記凝縮水貯留手段と前記蒸発手段とを前記凝縮水が流動可能に接続する凝縮水経路と、前記凝縮水経路に設けられ当該凝縮水経路の前記凝縮水を加圧し前記凝縮水貯留手段側から前記蒸発手段側に圧送するポンプとを有するように構成してもよい。 Further, in the working gas circulation engine, the pressure feeding means is provided in a condensed water path connecting the condensed water storage means and the evaporation means so that the condensed water can flow, and the condensed water path is provided in the condensed water path. You may comprise so that it may have the pump which pressurizes the said condensed water of a path | route and pumps it from the said condensed water storage means side to the said evaporation means side.
 また、上記作動ガス循環型エンジンにおいて、前記圧送手段は、前記凝縮水貯留手段と前記蒸発手段とを前記凝縮水が流動可能に接続すると共に、前記凝縮水を貯留する空間部が密閉状態とされた前記凝縮水貯留手段を介して前記循環経路と連通する凝縮水経路を有し、大気圧よりも高い前記循環経路のガスの圧力により前記凝縮水経路の前記凝縮水を加圧し前記凝縮水貯留手段側から前記蒸発手段側に圧送するように構成してもよい。 In the working gas circulation engine, the pressure feeding unit connects the condensed water storage unit and the evaporation unit so that the condensed water can flow, and a space portion for storing the condensed water is sealed. A condensed water path that communicates with the circulation path via the condensed water storage means, and pressurizes the condensed water in the condensed water path with a pressure of gas in the circulation path higher than atmospheric pressure to store the condensed water. You may comprise so that it pumps from the means side to the said evaporation means side.
 また、上記作動ガス循環型エンジンにおいて、前記圧送手段は、前記循環経路から分岐して設けられ相対的に高圧の前記作動ガスを貯留する作動ガス貯留手段と、前記作動ガス貯留手段と前記循環経路との間の前記作動ガスの流出入を調節する調節手段とを有するように構成してもよい。 Further, in the working gas circulation engine, the pressure feeding means is branched from the circulation path, is provided with working gas storage means for storing the relatively high pressure working gas, the working gas storage means, and the circulation path. Adjusting means for adjusting the inflow and outflow of the working gas between them.
 また、上記作動ガス循環型エンジンにおいて、前記凝縮水の発生量に基づいて前記圧送手段による前記凝縮水の圧送量を制御する圧送量制御手段を備えるように構成してもよい。 Further, the working gas circulation engine may be configured to include a pumping amount control unit that controls a pumping amount of the condensed water by the pumping unit based on a generation amount of the condensed water.
 また、上記作動ガス循環型エンジンにおいて、前記圧送量制御手段は、前記圧送量が前記発生量と同等になるように圧送量を制御するように構成してもよい。 In the working gas circulation engine, the pumping amount control means may control the pumping amount so that the pumping amount becomes equal to the generated amount.
 また、上記作動ガス循環型エンジンにおいて、前記凝縮水貯留手段への前記凝縮水の流量を検出する流量検出手段を備え、前記圧送量制御手段は、前記流量検出手段が検出した前記凝縮水の流量に基づいて前記圧送量を制御するように構成してもよい。 The working gas circulation engine may further include a flow rate detection unit that detects a flow rate of the condensed water to the condensed water storage unit, and the pumping amount control unit may detect a flow rate of the condensed water detected by the flow rate detection unit. The pumping amount may be controlled based on the above.
 また、上記作動ガス循環型エンジンにおいて、前記凝縮水貯留手段に貯留されている前記凝縮水の水位を検出する水位検出手段を備え、前記圧送量制御手段は、前記水位検出手段が検出した前記凝縮水の水位に基づいて前記圧送量を制御するように構成してもよい。 The working gas circulation engine may further include a water level detection unit that detects a level of the condensed water stored in the condensed water storage unit, and the pumping amount control unit may detect the condensation detected by the water level detection unit. The pumping amount may be controlled based on the water level.
 また、上記作動ガス循環型エンジンにおいて、前記圧送量制御手段は、前記燃焼室に供給される前記酸化剤又は前記燃料の供給量に基づいて前記圧送量を制御するように構成してもよい。 Further, in the working gas circulation engine, the pumping amount control means may be configured to control the pumping amount based on a supply amount of the oxidant or the fuel supplied to the combustion chamber.
 また、上記作動ガス循環型エンジンにおいて、前記圧送量制御手段は、エンジン負荷及びエンジン回転数に基づいて前記凝縮水の圧送量を制御するように構成してもよい。 Further, in the working gas circulation engine, the pumping amount control means may be configured to control the pumping amount of the condensed water based on the engine load and the engine speed.
 また、上記作動ガス循環型エンジンにおいて、前記蒸発手段により前記凝縮水を蒸発させることで発生する水蒸気のエネルギを運動エネルギとして回収する廃熱回収手段を備えるように構成してもよい。 Further, the working gas circulation engine may be configured to include waste heat recovery means for recovering the energy of water vapor generated by evaporating the condensed water by the evaporation means as kinetic energy.
 また、上記作動ガス循環型エンジンにおいて、前記凝縮水貯留手段に貯留されている前記凝縮水の温度を検出する温度検出手段と、前記温度検出手段が検出した温度が予め設定された所定温度以下である場合に、前記廃熱回収手段を介した水蒸気の熱を前記凝縮水貯留手段に貯留されている前記凝縮水に移動させる熱移動手段とを備えるように構成してもよい。 In the working gas circulation engine, the temperature detection means for detecting the temperature of the condensed water stored in the condensed water storage means, and the temperature detected by the temperature detection means is less than or equal to a preset predetermined temperature. In some cases, it may be configured to include heat transfer means for moving the heat of water vapor through the waste heat recovery means to the condensed water stored in the condensed water storage means.
 また、上記作動ガス循環型エンジンにおいて、前記凝縮水貯留手段に貯留されている前記凝縮水の水位を検出する水位検出手段を備え、前記熱移動手段は、前記水位検出手段が検出した水位が予め設定された所定水位以下である場合に、前記廃熱回収手段を介した水蒸気を前記凝縮水貯留手段に貯留されている前記凝縮水に導入するように構成してもよい。 The working gas circulation engine further includes a water level detection unit that detects a level of the condensed water stored in the condensed water storage unit, and the heat transfer unit has a water level detected by the water level detection unit in advance. When the water level is equal to or lower than a predetermined water level, water vapor that has passed through the waste heat recovery means may be introduced into the condensed water stored in the condensed water storage means.
 本発明に係る作動ガス循環型エンジンによれば、凝縮水を適正に処理することができる。 According to the working gas circulation engine according to the present invention, the condensed water can be appropriately processed.
図1は、本発明の実施形態1に係る作動ガス循環型エンジンの模式的な概略構成図である。FIG. 1 is a schematic configuration diagram of a working gas circulation engine according to Embodiment 1 of the present invention. 図2は、本発明の変形例1に係る作動ガス循環型エンジンの模式的な概略構成図である。FIG. 2 is a schematic configuration diagram of a working gas circulation engine according to Modification 1 of the present invention. 図3は、本発明の実施形態2に係る作動ガス循環型エンジンの模式的な概略構成図である。FIG. 3 is a schematic configuration diagram of a working gas circulation engine according to the second embodiment of the present invention. 図4は、本発明の変形例2に係る作動ガス循環型エンジンの模式的な概略構成図である。FIG. 4 is a schematic configuration diagram of a working gas circulation engine according to Modification 2 of the present invention. 図5は、本発明の実施形態3に係る作動ガス循環型エンジンの模式的な概略構成図である。FIG. 5 is a schematic configuration diagram of a working gas circulation engine according to the third embodiment of the present invention. 図6は、本発明の実施形態3に係る作動ガス循環型エンジンの圧送量制御を説明するフローチャートである。FIG. 6 is a flowchart for explaining the control of the pumping amount of the working gas circulation engine according to the third embodiment of the present invention. 図7は、本発明の実施形態4に係る作動ガス循環型エンジンの模式的な概略構成図である。FIG. 7 is a schematic schematic configuration diagram of a working gas circulation engine according to Embodiment 4 of the present invention. 図8は、本発明の実施形態4に係る作動ガス循環型エンジンの圧送量マップを示す図である。FIG. 8 is a diagram showing a pressure feed amount map of the working gas circulation engine according to the fourth embodiment of the present invention. 図9は、本発明の実施形態4に係る作動ガス循環型エンジンの圧送量制御を説明するフローチャートである。FIG. 9 is a flowchart for explaining the control of the pumping amount of the working gas circulation engine according to the fourth embodiment of the present invention. 図10は、本発明の実施形態5に係る作動ガス循環型エンジンの模式的な概略構成図である。FIG. 10 is a schematic schematic configuration diagram of a working gas circulation engine according to the fifth embodiment of the present invention. 図11は、本発明の実施形態5に係る作動ガス循環型エンジンの圧送量マップを示す図である。FIG. 11 is a diagram showing a pressure feed amount map of the working gas circulation engine according to the fifth embodiment of the present invention. 図12は、本発明の実施形態5に係る作動ガス循環型エンジンの応答遅れ時間マップを示す図である。FIG. 12 is a diagram showing a response delay time map of the working gas circulation engine according to the fifth embodiment of the present invention. 図13は、本発明の実施形態5に係る作動ガス循環型エンジンの圧送量制御を説明するフローチャートである。FIG. 13 is a flowchart for explaining the pressure feed amount control of the working gas circulation engine according to the fifth embodiment of the present invention. 図14は、本発明の変形例3に係る作動ガス循環型エンジンの模式的な概略構成図である。FIG. 14 is a schematic configuration diagram of a working gas circulation engine according to Modification 3 of the present invention. 図15は、本発明の実施形態6に係る作動ガス循環型エンジンの模式的な概略構成図である。FIG. 15 is a schematic configuration diagram of a working gas circulation engine according to Embodiment 6 of the present invention. 図16は、本発明の実施形態7に係る作動ガス循環型エンジンの模式的な概略構成図である。FIG. 16 is a schematic schematic configuration diagram of a working gas circulation engine according to a seventh embodiment of the present invention. 図17は、本発明の実施形態7に係る作動ガス循環型エンジンの凝縮水温度制御を説明するフローチャートである。FIG. 17 is a flowchart for explaining condensate temperature control of the working gas circulation engine according to the seventh embodiment of the present invention. 図18は、本発明の実施形態8に係る作動ガス循環型エンジンの模式的な概略構成図である。FIG. 18 is a schematic schematic configuration diagram of a working gas circulation engine according to an eighth embodiment of the present invention. 図19は、本発明の実施形態8に係る作動ガス循環型エンジンの凝縮水温度・水位制御を説明するフローチャートである。FIG. 19 is a flowchart illustrating condensate temperature / water level control of the working gas circulation engine according to the eighth embodiment of the present invention. 図20は、本発明の変形例4に係る作動ガス循環型エンジンの模式的な概略構成図である。FIG. 20 is a schematic schematic configuration diagram of a working gas circulation engine according to Modification 4 of the present invention.
符号の説明Explanation of symbols
1、1A、201、201A、301、401、501、501A、601、701、801、801A  作動ガス循環型エンジン
10  エンジン本体
11  シリンダヘッド
11b  吸気ポート
11c  排気ポート
12  シリンダブロック
13  ピストン
14  コネクティングロッド
15  吸気バルブ
16  排気バルブ
17  吸気管
18  排気管
19  クランクシャフト
20  循環経路
21  循環通路
21a  第1循環通路
21b  第2循環通路
21c  第3循環通路
30  酸化剤供給装置
40  燃料供給装置
50  電子制御装置
51  クランク角センサ
52  水素濃度センサ
53  酸素濃度センサ
54  流量センサ(流量検出手段)
55  水位センサ(水位検出手段)
56A  圧力センサ
57  温度センサ(温度検出手段)
60  凝縮器(凝縮手段)
61  冷却水循環路
62  冷却水ポンプ
63  ラジエータ
64  凝縮水排出通路
70、70A、270、870  凝縮水貯留タンク(凝縮水貯留手段)
80、80A、280、280A  圧送部(圧送手段)
81  凝縮水経路
82、82A  凝縮水ポンプ(ポンプ)
83  大気開放通路
90  熱交換器(蒸発手段)
284A  高圧タンク(作動ガス貯留手段)
285A  圧力調節弁(調節手段)
286A  分岐通路
351、451、551  圧送量制御部(圧送量制御手段)
610  膨張機(廃熱回収手段)
611  出力回転部材
720、820  熱移動部(熱移動手段)
721  分岐通路
722  熱交換器
723  流量調節弁
724  熱媒循環路
725  熱媒ポンプ
726  循環路放熱部
752、852  熱移動部制御部
821  分岐通路
822  流量調節弁
CC  燃焼室
1, 1A, 201, 201A, 301, 401, 501, 501A, 601, 701, 801, 801A Working gas circulation engine 10 Engine body 11 Cylinder head 11b Intake port 11c Exhaust port 12 Cylinder block 13 Piston 14 Connecting rod 15 Intake Valve 16 Exhaust valve 17 Intake pipe 18 Exhaust pipe 19 Crankshaft 20 Circulation path 21 Circulation path 21a First circulation path 21b Second circulation path 21c Third circulation path 30 Oxidant supply device 40 Fuel supply device 50 Electronic control device 51 Crank angle Sensor 52 Hydrogen concentration sensor 53 Oxygen concentration sensor 54 Flow rate sensor (flow rate detection means)
55 Water level sensor (water level detection means)
56A Pressure sensor 57 Temperature sensor (temperature detection means)
60 Condenser (condensing means)
61 Cooling water circulation path 62 Cooling water pump 63 Radiator 64 Condensed water discharge passages 70, 70A, 270, 870 Condensed water storage tank (condensed water storage means)
80, 80A, 280, 280A pumping section (pumping means)
81 Condensate path 82, 82A Condensate pump (pump)
83 Open air passage 90 Heat exchanger (evaporation means)
284A High-pressure tank (working gas storage means)
285A Pressure regulating valve (regulating means)
286A Branch passages 351, 451, 551 Pressure feed control unit (pressure feed control means)
610 Expander (waste heat recovery means)
611 Output rotating member 720, 820 Heat transfer part (heat transfer means)
721 Branch passage 722 Heat exchanger 723 Flow rate adjustment valve 724 Heat medium circulation path 725 Heat medium pump 726 Circulation path heat radiation part 752,852 Heat transfer part control part 821 Branch passage 822 Flow rate adjustment valve CC Combustion chamber
 以下に、本発明に係る作動ガス循環型エンジンの実施形態を図面に基づいて詳細に説明する。なお、この実施形態によりこの発明が限定されるものではない。また、下記実施形態における構成要素には、当業者が置換可能かつ容易なもの、或いは実質的に同一のものが含まれる。 Hereinafter, an embodiment of a working gas circulation engine according to the present invention will be described in detail with reference to the drawings. In addition, this invention is not limited by this embodiment. In addition, constituent elements in the following embodiments include those that can be easily replaced by those skilled in the art or those that are substantially the same.
(実施形態1)
 図1は、本発明の実施形態1に係る作動ガス循環型エンジンの模式的な概略構成図、図2は、本発明の変形例1に係る作動ガス循環型エンジンの模式的な概略構成図である。
(Embodiment 1)
1 is a schematic schematic configuration diagram of a working gas circulation engine according to Embodiment 1 of the present invention, and FIG. 2 is a schematic schematic configuration diagram of a working gas circulation engine according to Modification 1 of the present invention. is there.
 本実施形態の作動ガス循環型エンジン1は、図1に示すように、酸化剤、燃料及びこの燃料の燃焼に伴って動力を発生させる作動ガスが供給される燃焼室CCと、この燃焼室CCの吸気側と排気側とを繋ぐ循環経路20とを備え、その作動ガスが大気へと放出されることなく循環経路20を介して再び燃焼室CCに供給されるよう構成した、いわゆる閉サイクルエンジンである。この作動ガス循環型エンジン1は、燃焼室CC内で燃料を燃焼させ、この燃料の燃焼に伴って作動ガスを熱膨張させて動力を発生させるものである。 As shown in FIG. 1, the working gas circulation engine 1 of the present embodiment includes a combustion chamber CC to which an oxidant, fuel, and a working gas that generates power accompanying combustion of the fuel are supplied, and the combustion chamber CC. A so-called closed cycle engine configured to supply the working gas to the combustion chamber CC again through the circulation path 20 without being released to the atmosphere. It is. The working gas circulation engine 1 burns fuel in a combustion chamber CC and generates power by thermally expanding the working gas as the fuel burns.
 この作動ガス循環型エンジン1は、燃焼室CCが形成されるエンジン本体10と、燃焼室CCの吸気側と排気側とを繋ぐ循環経路20と、燃焼室CCに酸化剤を供給する酸化剤供給装置30と、燃焼室CCに燃料を供給する燃料供給装置40と、作動ガス循環型エンジン1の各部を制御する電子制御装置(ECU)50とを備える。エンジン本体10の燃焼室CCと循環経路20とは、ともに作動ガスが充填されており、作動ガスは、燃焼室CCと循環経路20との間で循環する。なお、図1に例示するエンジン本体10は、1気筒のみを図示しているが、本発明の作動ガス循環型エンジン1は、これに限らず、多気筒のエンジン本体10も適用可能である。 The working gas circulation engine 1 includes an engine body 10 in which a combustion chamber CC is formed, a circulation path 20 that connects the intake side and the exhaust side of the combustion chamber CC, and an oxidant supply that supplies an oxidant to the combustion chamber CC. A device 30, a fuel supply device 40 that supplies fuel to the combustion chamber CC, and an electronic control unit (ECU) 50 that controls each part of the working gas circulation engine 1 are provided. The combustion chamber CC and the circulation path 20 of the engine body 10 are both filled with working gas, and the working gas circulates between the combustion chamber CC and the circulation path 20. 1 shows only one cylinder, the working gas circulation engine 1 of the present invention is not limited to this, and a multi-cylinder engine body 10 can also be applied.
 本実施形態の燃焼室CCは、エンジン本体10に形成される。このエンジン本体10の燃焼室CCは、酸化剤と、この酸化剤との燃焼により水蒸気を生成する燃料と、作動ガスとが供給され、燃料の燃焼に伴って作動ガスが膨張可能であると共に燃料の燃焼後の排気ガスとして水蒸気と作動ガスとを排気可能なものである。 The combustion chamber CC of the present embodiment is formed in the engine body 10. The combustion chamber CC of the engine body 10 is supplied with an oxidant, a fuel that generates water vapor by combustion with the oxidant, and a working gas. As the exhaust gas after combustion, water vapor and working gas can be exhausted.
 具体的には、エンジン本体10は、燃焼室CCを形成するシリンダヘッド11、シリンダブロック12及びピストン13を備えている。ピストン13は、コネクティングロッド14を介してクランクシャフト19に連結し、シリンダヘッド11の下面の凹部11aとシリンダブロック12のシリンダボア12aとの間に区画される空間内に往復運動可能に配置される。燃焼室CCは、シリンダヘッド11の凹部11aの壁面とシリンダボア12aの壁面とピストン13の頂面13aとで囲まれた空間によって構成される。 Specifically, the engine body 10 includes a cylinder head 11, a cylinder block 12, and a piston 13 that form a combustion chamber CC. The piston 13 is connected to the crankshaft 19 via the connecting rod 14 and is disposed so as to be able to reciprocate in a space defined between the recess 11 a on the lower surface of the cylinder head 11 and the cylinder bore 12 a of the cylinder block 12. The combustion chamber CC is configured by a space surrounded by the wall surface of the recess 11 a of the cylinder head 11, the wall surface of the cylinder bore 12 a, and the top surface 13 a of the piston 13.
 エンジン本体10は、シリンダヘッド11に吸気ポート11b及び排気ポート11cが形成されている。吸気ポート11bと排気ポート11cとは、ともに循環経路20の一部をなすものである。吸気ポート11b、排気ポート11cは、それぞれ一端が燃焼室CC内に開口している。エンジン本体10は、吸気ポート11bの燃焼室CC側の開口部分に吸気バルブ15が配設されている。吸気バルブ15は、開弁時にこの吸気ポート11bの燃焼室CC側の開口を開く一方、閉弁時にこの吸気ポート11bの燃焼室CC側の開口を閉じるものである。エンジン本体10は、排気ポート11cの燃焼室CC側の開口部分に排気バルブ16が配設されている。排気バルブ16は、開弁時にこの排気ポート11cの燃焼室CC側の開口を開く一方、閉弁時にこの排気ポート11cの燃焼室CC側の開口を閉じるものである。 The engine body 10 has a cylinder head 11 formed with an intake port 11b and an exhaust port 11c. Both the intake port 11b and the exhaust port 11c form part of the circulation path 20. One end of each of the intake port 11b and the exhaust port 11c opens into the combustion chamber CC. The engine main body 10 is provided with an intake valve 15 at an opening portion of the intake port 11b on the combustion chamber CC side. The intake valve 15 opens the opening on the combustion chamber CC side of the intake port 11b when the valve is opened, and closes the opening on the combustion chamber CC side of the intake port 11b when the valve is closed. The engine body 10 is provided with an exhaust valve 16 at an opening portion of the exhaust port 11c on the combustion chamber CC side. The exhaust valve 16 opens the opening on the combustion chamber CC side of the exhaust port 11c when the valve is opened, and closes the opening on the combustion chamber CC side of the exhaust port 11c when the valve is closed.
 吸気バルブ15や排気バルブ16としては、例えば、不図示のカムシャフトの回転と弾性部材(弦巻バネ)の弾発力に伴って開閉駆動されるものがある。この種の吸気バルブ15や排気バルブ16においては、そのカムシャフトとクランクシャフト19の間にチェーンやスプロケット等からなる動力伝達機構を介在させることによってそのカムシャフトをクランクシャフト19の回転に連動させ、予め設定された開閉時期に開閉駆動させる。また、このエンジン本体10は、吸気バルブ15と排気バルブ16の開閉時期やリフト量を変更可能な、いわゆる可変バルブタイミング&リフト機構等の可変バルブ機構を備えていてもよく、これにより、その吸気バルブ15や排気バルブ16の開閉時期やリフト量を運転条件に応じた好適なものへと変更できるようになる。さらにまた、このエンジン本体10は、このような可変バルブ機構と同様の作用効果を得るべく、電磁力を利用して吸気バルブ15や排気バルブ16を開閉駆動させる、いわゆる電磁駆動弁を適用してもよい。 As the intake valve 15 and the exhaust valve 16, for example, there are those that are opened and closed in accordance with the rotation of a camshaft (not shown) and the elastic force of an elastic member (string spring). In this type of intake valve 15 and exhaust valve 16, a camshaft is interlocked with the rotation of the crankshaft 19 by interposing a power transmission mechanism composed of a chain, a sprocket, etc. between the camshaft and the crankshaft 19, Open / close drive is performed at a preset opening / closing timing. The engine body 10 may include a variable valve mechanism such as a so-called variable valve timing & lift mechanism that can change the opening / closing timing and lift amount of the intake valve 15 and the exhaust valve 16, thereby The opening / closing timing and lift amount of the valve 15 and the exhaust valve 16 can be changed to suitable ones according to the operating conditions. Furthermore, the engine body 10 is applied with a so-called electromagnetically driven valve that opens and closes the intake valve 15 and the exhaust valve 16 using electromagnetic force in order to obtain the same effect as the variable valve mechanism. Also good.
 また、エンジン本体10は、吸気ポート11bの燃焼室CC側とは反対側の開口に吸気管17が接続される一方、排気ポート11cの燃焼室CC側とは反対側の開口に排気管18が接続されている。吸気管17と排気管18とは、ともに循環経路20の一部をなすものである。吸気管17は、筒状に形成され内部を流体が通過可能なものであり、後述するように燃焼室CCに作動ガスとしてのアルゴン(Ar)と、酸化剤としての酸素(O)とを供給するための吸気通路である。つまり、燃焼室CCは、吸気バルブ15の開弁時に、この吸気管17から吸気ポート11bを介して酸化剤と作動ガスとが供給(吸気)される。一方、排気管18は、筒状に形成され内部を流体が通過可能なものであり、後述するように燃料としての水素(H)の燃焼後の排気ガスとして、燃焼室CCから作動ガスとしてのアルゴン(Ar)と、水蒸気(HO)とを排出するための排気通路である。つまり、燃焼室CCは、排気バルブ16の開弁時に、燃料の燃焼後の排気ガスとして、排気ポート11cを介して水蒸気と作動ガスとを排気管18に排気する。 The engine body 10 has an intake pipe 17 connected to an opening of the intake port 11b opposite to the combustion chamber CC side, and an exhaust pipe 18 connected to an opening of the exhaust port 11c opposite to the combustion chamber CC side. It is connected. The intake pipe 17 and the exhaust pipe 18 together form part of the circulation path 20. The intake pipe 17 is formed in a cylindrical shape and allows fluid to pass therethrough. As will be described later, the combustion chamber CC contains argon (Ar) as a working gas and oxygen (O 2 ) as an oxidant. It is an intake passage for supplying. In other words, when the intake valve 15 is opened, the oxidant and the working gas are supplied (intake) from the intake pipe 17 to the combustion chamber CC via the intake port 11b. On the other hand, the exhaust pipe 18 is formed in a cylindrical shape so that a fluid can pass therethrough. As will be described later, as an exhaust gas after combustion of hydrogen (H 2 ) as a fuel, the exhaust pipe 18 serves as a working gas from the combustion chamber CC. This is an exhaust passage for discharging argon (Ar) and water vapor (H 2 O). That is, when the exhaust valve 16 is opened, the combustion chamber CC exhausts water vapor and working gas to the exhaust pipe 18 through the exhaust port 11c as exhaust gas after combustion of fuel.
 循環経路20は、排気管18に排気された排気ガス中に含まれる作動ガスを燃焼室CCの排気側から吸気側に循環させ再び燃焼室CCに供給可能なものである。循環経路20は、上述した吸気ポート11b及び排気ポート11cと、吸気ポート11bの他端と排気ポート11cの他端とを繋ぐ循環通路21とを含んで構成される。これにより、この循環経路20内と燃焼室CC内とは、基本的には閉塞された空間をなす。循環通路21は、筒状に形成され内部を流体が通過可能なものであり、上述の吸気管17と排気管18とは、この循環通路21の一部をなす。 The circulation path 20 can circulate the working gas contained in the exhaust gas exhausted to the exhaust pipe 18 from the exhaust side to the intake side of the combustion chamber CC and supply it to the combustion chamber CC again. The circulation path 20 includes the intake port 11b and the exhaust port 11c described above, and a circulation passage 21 that connects the other end of the intake port 11b and the other end of the exhaust port 11c. As a result, the circulation path 20 and the combustion chamber CC basically form a closed space. The circulation passage 21 is formed in a cylindrical shape and allows fluid to pass therethrough. The intake pipe 17 and the exhaust pipe 18 described above form part of the circulation passage 21.
 この作動ガス循環型エンジン1は、循環経路20と燃焼室CCとからなる閉塞された空間内に作動ガスが充填される。作動ガス循環型エンジン1は、この作動ガスを循環経路20の吸気管17、吸気ポート11bから燃焼室CC内、燃焼室CC内から循環経路20の排気ポート11c、排気管18、そして、この排気ポート11c、排気管18から循環通路21を介して再び吸気管17、吸気ポート11bへと循環させる。つまり、循環経路20は、燃焼室CCの吸気側(吸気ポート11b側)と排気側(排気ポート11c側)とを燃焼室CCの外部で接続し、作動ガスを大気へと放出することなく再び燃焼室CCに供給する。さらに言えば、循環経路20は、両端が燃焼室CCに連通すると共に一端からは水蒸気と作動ガスとを含む排気ガスが燃焼室CCから流入し、他端からは燃焼室CCが吸気する酸化剤と作動ガスとが燃焼室CCに対して流出可能である。ここでは、作動ガス循環型エンジン1は、吸気バルブ15が開弁した際に、循環通路21の酸化剤、作動ガスが吸気管17、吸気ポート11bを介して燃焼室CCに供給される。また、作動ガス循環型エンジン1は、排気バルブ16が開弁した際に、燃焼室CC内の排気ガスが排気ポート11c、排気管18を介して循環通路21に排出される。 This working gas circulation engine 1 is filled with working gas in a closed space composed of the circulation path 20 and the combustion chamber CC. The working gas circulation engine 1 circulates the working gas through the intake pipe 17 of the circulation path 20, the intake port 11b into the combustion chamber CC, the exhaust port 11c of the circulation path 20 from the combustion chamber CC, the exhaust pipe 18, and the exhaust gas. The air is circulated from the port 11c and the exhaust pipe 18 to the intake pipe 17 and the intake port 11b through the circulation passage 21 again. That is, the circulation path 20 connects the intake side (intake port 11b side) and the exhaust side (exhaust port 11c side) of the combustion chamber CC outside the combustion chamber CC, and again without releasing the working gas to the atmosphere. Supply to combustion chamber CC. Furthermore, the circulator 20 has both ends communicating with the combustion chamber CC, an exhaust gas containing water vapor and working gas flows from one end into the combustion chamber CC, and an oxidant that the combustion chamber CC takes in from the other end. And the working gas can flow out to the combustion chamber CC. Here, in the working gas circulation engine 1, when the intake valve 15 is opened, the oxidant and working gas in the circulation passage 21 are supplied to the combustion chamber CC via the intake pipe 17 and the intake port 11b. Further, in the working gas circulation engine 1, when the exhaust valve 16 is opened, the exhaust gas in the combustion chamber CC is discharged to the circulation passage 21 through the exhaust port 11c and the exhaust pipe 18.
 さらに具体的には、循環経路20の循環通路21は、例えば、第1循環通路21aと、第2循環通路21bと、第3循環通路21cとを含んで構成されている。第1循環通路21aは、吸気ポート11bの他端と酸化剤供給装置30における後述の酸化剤供給手段32の排出口32aとを繋ぐものである。また、第2循環通路21bは、排気ポート11cの他端と後述する本発明の凝縮手段としての凝縮器60の排気ガス導入口60aとを繋ぐものである。なお、後述する本発明の蒸発手段としての熱交換器90は、この第2循環通路21b中に設けられている。また、第3循環通路21cは、この凝縮器60の作動ガス排出口60bと酸化剤供給手段32の作動ガス導入口32bとを繋ぐものである。上述の吸気管17は、第1循環通路21aの一部をなす一方、排気管18は、第2循環通路21bの一部をなす。 More specifically, the circulation path 21 of the circulation path 20 includes, for example, a first circulation path 21a, a second circulation path 21b, and a third circulation path 21c. The first circulation passage 21 a connects the other end of the intake port 11 b and a discharge port 32 a of an oxidant supply means 32 described later in the oxidant supply device 30. The second circulation passage 21b connects the other end of the exhaust port 11c and an exhaust gas inlet 60a of a condenser 60 as a condensing means of the present invention described later. In addition, the heat exchanger 90 as an evaporation means of the present invention described later is provided in the second circulation passage 21b. Further, the third circulation passage 21 c connects the working gas discharge port 60 b of the condenser 60 and the working gas introduction port 32 b of the oxidant supply means 32. The intake pipe 17 described above forms part of the first circulation passage 21a, while the exhaust pipe 18 forms part of the second circulation passage 21b.
 ここで、循環経路20と燃焼室CCとからなる閉塞された空間内に充填される作動ガスとしては、空気より比熱比の高いガスが用いられる。作動ガスは、例えば、単原子ガスが用いられる。ここでは、本実施形態の作動ガスは、空気よりも比熱比の高いものであって、例えば、単原子ガスであるアルゴン(Ar)やヘリウム(He)等の希ガスが用いられる。本実施形態では、作動ガスは、上述のようにアルゴン(Ar)を用いるものとして説明する。 Here, a gas having a higher specific heat ratio than air is used as the working gas filled in the closed space formed by the circulation path 20 and the combustion chamber CC. As the working gas, for example, a monoatomic gas is used. Here, the working gas of the present embodiment has a higher specific heat ratio than air, and for example, a rare gas such as argon (Ar) or helium (He) that is a monoatomic gas is used. In the present embodiment, the working gas is described as using argon (Ar) as described above.
 酸化剤供給装置30は、循環経路20の吸気管17、吸気ポート11bを介して燃焼室CCに酸化剤を供給するものであり、酸化剤貯留タンク31と、酸化剤供給手段32と、酸化剤供給通路33と、レギュレータ34と、酸化剤流量計35とを含んで構成される。 The oxidant supply device 30 supplies oxidant to the combustion chamber CC via the intake pipe 17 and the intake port 11b of the circulation path 20, and includes an oxidant storage tank 31, an oxidant supply means 32, an oxidant. A supply passage 33, a regulator 34, and an oxidant flow meter 35 are included.
 酸化剤貯留タンク31は、酸化剤を高圧の状態で貯留するものである。酸化剤供給手段32は、酸化剤貯留タンク31に貯留された酸化剤を循環通路21に供給するものである。酸化剤供給通路33は、酸化剤貯留タンク31と酸化剤供給手段32とを繋ぐものである。レギュレータ34及び酸化剤流量計35は、この酸化剤供給通路33上に設けられる。 The oxidant storage tank 31 stores the oxidant in a high pressure state. The oxidant supply means 32 supplies the oxidant stored in the oxidant storage tank 31 to the circulation passage 21. The oxidant supply passage 33 connects the oxidant storage tank 31 and the oxidant supply means 32. The regulator 34 and the oxidant flow meter 35 are provided on the oxidant supply passage 33.
 ここで、本実施形態の酸化剤供給手段32としては、酸化剤供給通路33から流入してきた酸化剤と、作動ガス導入口32bを介して循環通路21から流入してきた作動ガスとを混合し、混合後の酸化剤と作動ガスとを排出口32aから循環通路21の下流側(吸気ポート11b側)に流す酸化剤混合手段を用いる。したがって、本実施形態の酸化剤供給装置30は、酸化剤を単に循環通路21へと供給するだけではなく、循環通路21を通る作動ガスと混ぜ合わせて循環通路21に送り込ませることができる。この結果、酸化剤は、吸気バルブ15の開弁に伴い吸気ポート11bを介して作動ガスと共に燃焼室CCに供給されることになる。なお、酸化剤供給手段32は、上記の構成に限らず、電子制御装置50によって制御され、酸化剤を循環経路20、例えば、循環通路21や吸気ポート11bに噴射して供給する、いわゆる、酸化剤噴射弁を用いてもよい。 Here, as the oxidant supply means 32 of the present embodiment, the oxidant flowing from the oxidant supply passage 33 and the working gas flowing from the circulation passage 21 through the working gas introduction port 32b are mixed, An oxidant mixing means is used for flowing the mixed oxidant and working gas from the discharge port 32a to the downstream side of the circulation passage 21 (the intake port 11b side). Therefore, the oxidant supply device 30 of the present embodiment can not only supply the oxidant to the circulation passage 21 but also mix it with the working gas passing through the circulation passage 21 and send it to the circulation passage 21. As a result, the oxidant is supplied to the combustion chamber CC together with the working gas via the intake port 11b when the intake valve 15 is opened. The oxidant supply means 32 is not limited to the above-described configuration, and is controlled by the electronic control unit 50 so that the oxidant is injected and supplied to the circulation path 20, for example, the circulation path 21 or the intake port 11b. An agent injection valve may be used.
 レギュレータ34は、酸化剤供給通路33におけるレギュレータ34よりも下流側(エンジン本体10側)の圧力を電子制御装置50の指令に従った目標圧力に調整するものである。言い換えれば、このレギュレータ34は、酸化剤供給通路33における酸化剤の流量を制御するものである。また、酸化剤流量計35は、酸化剤供給通路33における酸化剤の流量を計測する手段であって、レギュレータ34で調整された酸化剤の流量の計測を行う。この酸化剤流量計35の計測信号は、電子制御装置50に送信される。 The regulator 34 adjusts the pressure downstream of the regulator 34 in the oxidant supply passage 33 (on the engine body 10 side) to a target pressure in accordance with a command from the electronic control unit 50. In other words, the regulator 34 controls the flow rate of the oxidant in the oxidant supply passage 33. The oxidant flow meter 35 is a means for measuring the flow rate of the oxidant in the oxidant supply passage 33 and measures the flow rate of the oxidant adjusted by the regulator 34. The measurement signal of the oxidant flow meter 35 is transmitted to the electronic control unit 50.
 ここで、この酸化剤供給装置30が供給する酸化剤としては、上述のように酸素(O)が用いられる。つまり、本実施形態の酸化剤貯留タンク31は、酸化剤としての酸素を例えば70MPa程度の高圧で貯留し、酸化剤供給手段32は、この高圧の酸素(O)を循環通路21に供給する。 Here, oxygen (O 2 ) is used as the oxidant supplied by the oxidant supply device 30 as described above. That is, the oxidant storage tank 31 of the present embodiment stores oxygen as an oxidant at a high pressure of about 70 MPa, for example, and the oxidant supply means 32 supplies this high-pressure oxygen (O 2 ) to the circulation passage 21. .
 燃料供給装置40は、燃焼室CCに燃料を供給するものであり、燃料貯留タンク41と、燃料噴射手段42と、燃料供給通路43と、レギュレータ44と、燃料流量計45と、サージタンク46とを含んで構成される。 The fuel supply device 40 supplies fuel to the combustion chamber CC, and includes a fuel storage tank 41, a fuel injection means 42, a fuel supply passage 43, a regulator 44, a fuel flow meter 45, a surge tank 46, and the like. It is comprised including.
 燃料貯留タンク41は、燃料を高圧の状態で貯留するものである。燃料噴射手段42は、燃料貯留タンク41に貯留された燃料を燃焼室CCに噴射するものである。燃料供給通路43は、燃料貯留タンク41と燃料噴射手段42を繋ぐものである。レギュレータ44、燃料流量計45及びサージタンク46は、この燃料供給通路43上に設けられる。レギュレータ44と、燃料流量計45と、サージタンク46とは、燃料供給通路43における燃料の供給方向に対して、上流側(燃料貯留タンク41側)から下流側(燃料噴射手段42側)に向かってレギュレータ44、燃料流量計45、サージタンク46の順で設けられている。 The fuel storage tank 41 stores fuel in a high pressure state. The fuel injection means 42 injects the fuel stored in the fuel storage tank 41 into the combustion chamber CC. The fuel supply passage 43 connects the fuel storage tank 41 and the fuel injection means 42. The regulator 44, the fuel flow meter 45, and the surge tank 46 are provided on the fuel supply passage 43. The regulator 44, the fuel flow meter 45, and the surge tank 46 are directed from the upstream side (the fuel storage tank 41 side) to the downstream side (the fuel injection means 42 side) with respect to the fuel supply direction in the fuel supply passage 43. The regulator 44, the fuel flow meter 45, and the surge tank 46 are provided in this order.
 ここで、本実施形態の燃料噴射手段42は、燃料を燃焼室CC内に直接噴射可能なようにシリンダヘッド11に設けられる。この燃料噴射手段42は、電子制御装置50によって制御される、いわゆる、燃料噴射弁である。電子制御装置50は、例えば、運転者がこの作動ガス循環型エンジン1に要求する駆動力(要求エンジン負荷)やエンジン回転数等の運転状態に応じて燃料の噴射時期や噴射量、言い換えれば供給量を制御する。 Here, the fuel injection means 42 of the present embodiment is provided in the cylinder head 11 so that the fuel can be directly injected into the combustion chamber CC. The fuel injection means 42 is a so-called fuel injection valve controlled by the electronic control unit 50. The electronic control unit 50, for example, the fuel injection timing or the injection amount, in other words, the supply according to the driving state (requested engine load) required by the driver for the working gas circulation engine 1 and the operating state such as the engine speed. Control the amount.
 なお、運転者がこの作動ガス循環型エンジン1に要求する駆動力(要求エンジン負荷)は、例えば、作動ガス循環型エンジン1を搭載する車両のアクセル開度などに基づいて設定される。電子制御装置50は、例えば、作動ガス循環型エンジン1のエンジン回転数と要求する駆動力とに基づいて、現在のエンジン回転数において、作動ガス循環型エンジン1に要求する駆動力を得ることができる水素の供給量を決定する。作動ガス循環型エンジン1のエンジン回転数は、例えばクランク角センサ51に基づいて検出することができる。クランク角センサ51は、例えば、作動ガス循環型エンジン1のクランクシャフト19の回転角度であるクランク角度を検出するものである。クランク角センサ51は、検出信号を電子制御装置50に送信する。電子制御装置50は、例えば、検出されたクランク角度に基づいて各気筒における吸気行程、圧縮行程、膨張行程、排気行程を判別すると共に、作動ガス循環型エンジン1の回転速度としてエンジン回転数(rpm)を算出する。なおここで、エンジン回転数は、言い換えれば、クランクシャフト19の回転速度に対応し、このクランクシャフト19の回転速度が高くなれば、クランクシャフト19の回転数であるエンジン回転数も高くなる。 Note that the driving force (requested engine load) required by the driver for the working gas circulation engine 1 is set based on, for example, the accelerator opening degree of the vehicle on which the working gas circulation engine 1 is mounted. For example, the electronic control unit 50 can obtain the driving force required for the working gas circulation engine 1 at the current engine speed based on the engine speed of the working gas circulation engine 1 and the requested driving force. Determine how much hydrogen can be supplied. The engine speed of the working gas circulation engine 1 can be detected based on, for example, a crank angle sensor 51. The crank angle sensor 51 detects, for example, a crank angle that is a rotation angle of the crankshaft 19 of the working gas circulation engine 1. The crank angle sensor 51 transmits a detection signal to the electronic control unit 50. For example, the electronic control unit 50 determines an intake stroke, a compression stroke, an expansion stroke, and an exhaust stroke in each cylinder based on the detected crank angle, and the engine speed (rpm) as the rotational speed of the working gas circulation engine 1. ) Is calculated. Here, the engine speed corresponds to the rotational speed of the crankshaft 19 in other words, and if the rotational speed of the crankshaft 19 increases, the engine rotational speed that is the rotational speed of the crankshaft 19 also increases.
 レギュレータ44は、燃料供給通路43におけるレギュレータ44よりも下流側(燃料流量計45及びサージタンク46側)の圧力を設定圧力に調整するものである。また、燃料流量計45は、燃料供給通路43における燃料の流量を計測する手段であって、レギュレータ44で調整された燃料の流量の計測を行う。この燃料流量計45の計測信号は、電子制御装置50に送信される。また、サージタンク46は、燃料噴射手段42による燃料の噴射時に燃料供給通路43内に発生する脈動の低減を図るものである。 The regulator 44 adjusts the pressure downstream of the regulator 44 in the fuel supply passage 43 (on the fuel flow meter 45 and surge tank 46 side) to the set pressure. The fuel flow meter 45 is a means for measuring the fuel flow rate in the fuel supply passage 43 and measures the fuel flow rate adjusted by the regulator 44. The measurement signal of the fuel flow meter 45 is transmitted to the electronic control device 50. The surge tank 46 is intended to reduce pulsation generated in the fuel supply passage 43 when fuel is injected by the fuel injection means 42.
 ここで、この燃料供給装置40が供給する燃料としては、燃焼により水蒸気を生成するものが用いられ、本実施形態では、上述のように水素(H)が用いられる。つまり、本実施形態の燃料貯留タンク41は、燃料としての水素を例えば70MPa程度の高圧で貯留し、燃料噴射手段42は、この高圧の水素を燃焼室CCに噴射する。 Here, as the fuel supplied by the fuel supply device 40, one that generates water vapor by combustion is used, and in the present embodiment, hydrogen (H 2 ) is used as described above. That is, the fuel storage tank 41 of the present embodiment stores hydrogen as fuel at a high pressure of, for example, about 70 MPa, and the fuel injection means 42 injects this high pressure hydrogen into the combustion chamber CC.
 本実施形態の作動ガス循環型エンジン1は、燃焼室CC内に燃料としての水素と酸化剤としての酸素を供給し、水素を拡散燃焼させるものとして例示する。すなわち、上記のように構成される作動ガス循環型エンジン1は、燃焼室CC内に形成された高温の圧縮ガス(酸素(O)及びアルゴン(Ar))の中に高圧の水素(H)を噴射することにより、この水素の一部が自己着火し、水素と圧縮ガス(酸素)とが拡散混合しながら燃焼する。この燃焼室CC内での水素の燃焼によって、燃焼室CCの中では、水素と酸素(O)が反応して水蒸気(HO)が生成されると共に、比熱比の大きいアルゴン(Ar)が熱膨張を起こす。この結果、この作動ガス循環型エンジン1は、水素の拡散燃焼とアルゴンの熱膨張とによってピストン13が押し下げられ、これにより動力を発生する。 The working gas circulation engine 1 of this embodiment is exemplified as one in which hydrogen as a fuel and oxygen as an oxidant are supplied into the combustion chamber CC to diffuse and burn hydrogen. That is, the working gas circulation engine 1 configured as described above includes high-pressure hydrogen (H 2 ) in high-temperature compressed gas (oxygen (O 2 ) and argon (Ar)) formed in the combustion chamber CC. ) Is self-ignited, and hydrogen and compressed gas (oxygen) are combusted while being diffusely mixed. By combustion of hydrogen in the combustion chamber CC, hydrogen and oxygen (O 2 ) react in the combustion chamber CC to generate water vapor (H 2 O), and argon (Ar) having a large specific heat ratio. Causes thermal expansion. As a result, in the working gas circulation engine 1, the piston 13 is pushed down by the diffusion combustion of hydrogen and the thermal expansion of argon, thereby generating power.
 そして、作動ガス循環型エンジン1は、水素の燃焼とアルゴンの熱膨張とが一通り終わった際(例えば、ピストン13が下死点近くに位置している際)、排気バルブ16の開弁に伴って、燃焼室CC内から水蒸気とアルゴンとを含む排気ガスが排気ポート11cを介して排気管18に排出される。ここで、排出された排気ガス中のアルゴンは、エンジン本体10の熱効率を高めるために、循環経路20を介して燃焼室CCの排気側から吸気側に循環させ再び吸気側から燃焼室CCに供給する必要がある。しかしながら、同時に排出された排気ガス中の水蒸気は、3原子からなる分子(3原子分子)であり、単原子からなるアルゴンよりも比熱比が小さいので、アルゴンと共に燃焼室CCへ循環させてしまうと、エンジン本体10の熱効率を低下させるおそれがある。このため、この作動ガス循環型エンジン1は、排気ガスの中に含まれる水蒸気を取り除く手段を循環経路20上に設けている。 The working gas circulation engine 1 opens the exhaust valve 16 when the combustion of hydrogen and the thermal expansion of argon are completed (for example, when the piston 13 is located near the bottom dead center). Accordingly, exhaust gas containing water vapor and argon is discharged from the combustion chamber CC to the exhaust pipe 18 through the exhaust port 11c. Here, the argon in the exhaust gas discharged is circulated from the exhaust side to the intake side of the combustion chamber CC via the circulation path 20 and supplied to the combustion chamber CC from the intake side again in order to increase the thermal efficiency of the engine body 10. There is a need to. However, since the water vapor in the exhaust gas discharged at the same time is a molecule composed of three atoms (triatomic molecule) and has a specific heat ratio smaller than that of argon composed of a single atom, if it is circulated to the combustion chamber CC together with argon. There is a risk that the thermal efficiency of the engine body 10 may be reduced. For this reason, this working gas circulation engine 1 is provided with a means on the circulation path 20 for removing water vapor contained in the exhaust gas.
 具体的には、作動ガス循環型エンジン1は、循環経路20を流動する排気ガスの中に含まれる水蒸気を取り除く手段として、凝縮手段としての凝縮器60を備える。さらに、この作動ガス循環型エンジン1は、冷却水循環路61と、冷却水ポンプ62と、ラジエータ63とを備える。 Specifically, the working gas circulation engine 1 includes a condenser 60 as a condensing means as means for removing water vapor contained in the exhaust gas flowing through the circulation path 20. The working gas circulation engine 1 further includes a cooling water circulation path 61, a cooling water pump 62, and a radiator 63.
 凝縮器60は、循環経路20に設けられ排気ガス中に含まれる水蒸気を凝縮して凝縮水(HO)とするものである。凝縮器60は、循環通路21上の第2循環通路21bと第3循環通路21cとの間に設けられる。つまり、凝縮器60は、循環通路21上の酸化剤供給手段32よりも排気側に設けられる。また、凝縮器60は、冷却水循環路61が内部を通るようにして接続されている。 The condenser 60 is provided in the circulation path 20 to condense the water vapor contained in the exhaust gas into condensed water (H 2 O). The condenser 60 is provided between the second circulation passage 21b and the third circulation passage 21c on the circulation passage 21. That is, the condenser 60 is provided on the exhaust side of the oxidant supply means 32 on the circulation passage 21. The condenser 60 is connected so that the cooling water circulation path 61 passes through the inside.
 冷却水循環路61は、凝縮器60に熱交換媒体としての冷却水を循環させるものであり、冷却水が流動可能である。この冷却水循環路61は、閉じられた環状の経路になっており、内部に冷却水が充填されている。 The cooling water circulation path 61 circulates cooling water as a heat exchange medium through the condenser 60, and the cooling water can flow. The cooling water circulation path 61 is a closed annular path and is filled with cooling water.
 冷却水ポンプ62は、冷却水循環路61の経路上に設けられており、冷却水循環路61の冷却水は、この冷却水ポンプ62が駆動することで冷却水循環路61を循環することができる。 The cooling water pump 62 is provided on the cooling water circulation path 61, and the cooling water in the cooling water circulation path 61 can be circulated through the cooling water circulation path 61 by driving the cooling water pump 62.
 ラジエータ63は、冷却水循環路61の経路上に設けられており、冷却水循環路61を循環する冷却水を冷却可能なものである。本実施形態のラジエータ63は、放熱手段として作用し、この作動ガス循環型エンジン1を搭載する車両の走行風などにより冷却水循環路61を循環する冷却水を冷却可能である。 The radiator 63 is provided on the cooling water circulation path 61 and can cool the cooling water circulating in the cooling water circulation path 61. The radiator 63 of the present embodiment acts as a heat radiating means, and can cool the cooling water circulating through the cooling water circulation path 61 by the traveling wind of the vehicle on which the working gas circulation engine 1 is mounted.
 したがって、この凝縮器60は、冷却水循環路61を循環しラジエータ63により冷却された冷却水が内部に循環、供給されることで、この冷却水と循環経路20を流れる排気ガスとを熱交換させ排気ガスを冷却することにより、排気ガスに含まれる水蒸気(HO)を液化、凝縮して凝縮水とし排気ガスから分離する。すなわち、凝縮器60は、排気ガスをアルゴンと凝縮水とに分離することができる。このとき、凝縮器60にて循環経路20の排気ガスと熱交換をすることで熱を吸収し温度が上昇した冷却水は、冷却水循環路61を循環し再びラジエータ63を通過する際に放熱することで温度が低下し、すなわち、冷却される。つまり、冷却水循環路61を循環する冷却水は、凝縮器60にて吸収した熱をラジエータ63で放熱する。 Therefore, the condenser 60 circulates through the cooling water circulation path 61 and is circulated and supplied with the cooling water cooled by the radiator 63, thereby heat-exchanging the cooling water and the exhaust gas flowing through the circulation path 20. By cooling the exhaust gas, water vapor (H 2 O) contained in the exhaust gas is liquefied and condensed to be condensed water and separated from the exhaust gas. That is, the condenser 60 can separate the exhaust gas into argon and condensed water. At this time, the cooling water whose temperature has risen due to heat exchange by exchanging heat with the exhaust gas in the circulation path 20 in the condenser 60 is radiated when circulating through the cooling water circulation path 61 and again passing through the radiator 63. As a result, the temperature is lowered, that is, cooled. That is, the cooling water circulating in the cooling water circulation path 61 radiates the heat absorbed by the condenser 60 by the radiator 63.
 そして、凝縮器60によって分離されたアルゴンは、凝縮器60の作動ガス排出口60bを介して第3循環通路21cに排出される。一方、凝縮器60によって分離された凝縮水は、凝縮器60の凝縮水排出口60cを介して凝縮水排出通路64に排出され、循環経路20の系外、ここでは後述する凝縮水貯留手段としての凝縮水貯留タンク70に排出される。 Then, the argon separated by the condenser 60 is discharged to the third circulation passage 21c through the working gas discharge port 60b of the condenser 60. On the other hand, the condensed water separated by the condenser 60 is discharged to the condensed water discharge passage 64 through the condensed water discharge port 60c of the condenser 60, and is outside the system of the circulation path 20, here as condensed water storage means described later. The condensed water storage tank 70 is discharged.
 なお、この凝縮器60とラジエータ63とは、エンジン運転中に想定し得る最も高温の排気ガスが燃焼室CCから排出された際に、その排気ガス中の水蒸気が液化・凝縮される温度にまで排気ガス温度を下げることのできる容量(換言すれば排気ガスの冷却性能)に設定される。 The condenser 60 and the radiator 63 are configured to reach a temperature at which the water vapor in the exhaust gas is liquefied and condensed when the hottest exhaust gas that can be assumed during engine operation is discharged from the combustion chamber CC. The capacity capable of lowering the exhaust gas temperature (in other words, the exhaust gas cooling performance) is set.
 ここで、燃焼室CCから排出された排気ガスの中には、水蒸気やアルゴンだけでなく、水素又は酸素が含まれていることがある。例えば、酸素に対して水素の燃焼室CCへの供給量の方が所定よりも多いときには、未燃焼の水素が残り、そのまま循環経路20へと排出される。また、水素に対して酸素の燃焼室CCへの供給量の方が所定よりも多いときには、酸素が残り、そのまま循環経路20へと排出される。このため、排気ガス中の水素や酸素は、凝縮器60で排気ガス中の水蒸気が分離された後のアルゴンと共に凝縮器60の作動ガス排出口60bから第3循環通路21cに排出される。したがって、排気ガス中の水素や酸素もアルゴンと同様に循環経路20を循環し再び燃焼室CCに供給される。 Here, the exhaust gas discharged from the combustion chamber CC may contain not only water vapor and argon but also hydrogen or oxygen. For example, when the supply amount of hydrogen to the combustion chamber CC is larger than a predetermined amount relative to oxygen, unburned hydrogen remains and is discharged to the circulation path 20 as it is. Further, when the supply amount of oxygen to the combustion chamber CC is larger than a predetermined amount with respect to hydrogen, oxygen remains and is discharged to the circulation path 20 as it is. For this reason, hydrogen and oxygen in the exhaust gas are discharged from the working gas discharge port 60b of the condenser 60 to the third circulation passage 21c together with argon after the water vapor in the exhaust gas is separated by the condenser 60. Accordingly, hydrogen and oxygen in the exhaust gas circulate through the circulation path 20 similarly to argon and are supplied again to the combustion chamber CC.
 そこで、作動ガス循環型エンジン1は、循環経路20を排気側から吸気側に循環するガス(循環ガス)中の水素又は酸素の量を検出し、水素又は酸素が燃焼室CCに到達する時期を見計らって、燃料供給装置40からの水素の噴射量又は酸化剤供給装置30からの酸素の供給量を調節している。これにより、作動ガス循環型エンジン1は、燃焼室CC内における水素又は酸素の過多を防ぐことができる。 Therefore, the working gas circulation engine 1 detects the amount of hydrogen or oxygen in the gas (circulation gas) circulating in the circulation path 20 from the exhaust side to the intake side, and determines when the hydrogen or oxygen reaches the combustion chamber CC. As a matter of course, the injection amount of hydrogen from the fuel supply device 40 or the supply amount of oxygen from the oxidant supply device 30 is adjusted. Thereby, the working gas circulation engine 1 can prevent excessive hydrogen or oxygen in the combustion chamber CC.
 具体的には、作動ガス循環型エンジン1は、循環経路20を循環する循環ガス中の燃料の濃度を検出する燃料濃度検出手段、ここでは循環ガス中の水素濃度を検出する水素濃度検出手段であって、具体的には水素濃度センサ52と、循環ガス中の酸化剤の濃度を検出する酸化剤濃度検出手段、ここでは循環ガス中の酸素濃度を検出する酸素濃度検出手段であって、具体的には酸素濃度センサ53とを備えている。水素濃度センサ52と酸素濃度センサ53とは、各々検出信号を電子制御装置50に送信する。したがって、電子制御装置50は、その各検出信号から循環ガス中の水素又は酸素の残存量を把握し、その水素又は酸素が燃焼室CCに到達する時期を見計らって、燃料噴射手段42の水素の噴射量又はレギュレータ34の目標圧力(つまり酸素の供給量)を制御する。 Specifically, the working gas circulation engine 1 is a fuel concentration detection means for detecting the concentration of fuel in the circulation gas circulating through the circulation path 20, here, a hydrogen concentration detection means for detecting the hydrogen concentration in the circulation gas. Specifically, a hydrogen concentration sensor 52 and an oxidant concentration detection means for detecting the concentration of the oxidant in the circulation gas, here an oxygen concentration detection means for detecting the oxygen concentration in the circulation gas, Specifically, an oxygen concentration sensor 53 is provided. The hydrogen concentration sensor 52 and the oxygen concentration sensor 53 each transmit a detection signal to the electronic control unit 50. Therefore, the electronic control unit 50 grasps the remaining amount of hydrogen or oxygen in the circulating gas from the respective detection signals, estimates the time when the hydrogen or oxygen reaches the combustion chamber CC, and determines the amount of hydrogen in the fuel injection means 42. The injection amount or the target pressure of the regulator 34 (that is, the supply amount of oxygen) is controlled.
 上記のように構成される作動ガス循環型エンジン1は、燃焼室CC内での水素の燃焼に伴って比熱比の大きいアルゴンが熱膨張を起こすことでピストン13が押し下げられ、このピストン13がシリンダボア12a内で往復運動を繰り返すことにより、吸気行程、圧縮行程、燃焼行程、排気行程を1つのサイクルとしてこのサイクルを繰り返す。ピストン13の往復運動は、コネクティングロッド14によってクランクシャフト19に伝達され、コネクティングロッド14とクランクシャフト19との作用により往復運動が回転運動に変換され、クランクシャフト19が回転する。この間、電子制御装置50は、クランクシャフト19の回転位置や、車両の運転席に設けられるアクセルペダル(不図示)の操作量であるアクセル開度、循環ガス中の水素又は酸素の残存量等の運転状態に応じて、燃料噴射手段42の水素の噴射量又はレギュレータ34の目標圧力(つまり酸素の供給量)を制御する。 In the working gas circulation engine 1 configured as described above, the piston 13 is pushed down by the thermal expansion of argon having a large specific heat ratio accompanying the combustion of hydrogen in the combustion chamber CC. By repeating the reciprocating motion within 12a, this cycle is repeated with the intake stroke, compression stroke, combustion stroke, and exhaust stroke as one cycle. The reciprocating motion of the piston 13 is transmitted to the crankshaft 19 by the connecting rod 14, and the reciprocating motion is converted into rotational motion by the action of the connecting rod 14 and the crankshaft 19, and the crankshaft 19 rotates. During this time, the electronic control unit 50 determines the rotational position of the crankshaft 19, the accelerator opening that is the operation amount of an accelerator pedal (not shown) provided in the driver's seat of the vehicle, the remaining amount of hydrogen or oxygen in the circulating gas, and the like. The hydrogen injection amount of the fuel injection means 42 or the target pressure of the regulator 34 (that is, the oxygen supply amount) is controlled according to the operating state.
 また、作動ガス循環型エンジン1は、クランクシャフト19の回転に伴って吸気バルブ15や排気バルブ16が往復運動し、循環経路20と燃焼室CCとの連通と遮断とを繰り返すことにより、吸排気を行ない上記の4つの行程を繰り返す。 In addition, the working gas circulation engine 1 reciprocates the intake valve 15 and the exhaust valve 16 as the crankshaft 19 rotates, and repeats communication and disconnection between the circulation path 20 and the combustion chamber CC. And repeat the above four steps.
 すなわち、作動ガス循環型エンジン1は、吸気行程において、吸気バルブ15が開弁する一方、排気バルブ16が閉弁すると共に、ピストン13が上死点側から下死点側に移動することにより、循環経路20の吸気管17、吸気ポート11bを介して燃焼室CCに酸素とアルゴンとが吸気される。 That is, in the working gas circulation engine 1, in the intake stroke, the intake valve 15 is opened, the exhaust valve 16 is closed, and the piston 13 is moved from the top dead center side to the bottom dead center side. Oxygen and argon are sucked into the combustion chamber CC via the intake pipe 17 and the intake port 11b of the circulation path 20.
 次に、作動ガス循環型エンジン1は、圧縮行程において、吸気バルブ15が閉弁し吸気バルブ15と排気バルブ16の両方が閉弁状態となると共に、ピストン13が下死点側から上死点側に移動することにより、燃焼室CC内の酸素、アルゴンが圧縮され温度が上昇する。 Next, in the working gas circulation engine 1, in the compression stroke, the intake valve 15 is closed, both the intake valve 15 and the exhaust valve 16 are closed, and the piston 13 is moved from the bottom dead center to the top dead center. By moving to the side, oxygen and argon in the combustion chamber CC are compressed and the temperature rises.
 次に、作動ガス循環型エンジン1は、燃焼行程において、燃焼室CC内に形成された高温の圧縮ガス(酸素及びアルゴン)の中に高圧の水素を噴射することにより、この水素の一部が自己着火し、水素と圧縮ガス(酸素)とが拡散混合しながら燃焼する。そして、水素が燃焼すると、これに伴って比熱比の大きいアルゴンが熱膨張を起こし、この水素の拡散燃焼とアルゴンの熱膨張とによってピストン13が押し下げられ、これにより、作動ガス循環型エンジン1は、動力を発生する。 Next, the working gas circulation engine 1 injects high-pressure hydrogen into high-temperature compressed gas (oxygen and argon) formed in the combustion chamber CC in the combustion stroke, so that a part of the hydrogen is injected. It self-ignites and burns while diffusing and mixing hydrogen and compressed gas (oxygen). When hydrogen burns, argon having a large specific heat ratio causes thermal expansion, and the piston 13 is pushed down by the diffusion combustion of hydrogen and the thermal expansion of argon, whereby the working gas circulation engine 1 Generate power.
 次に、作動ガス循環型エンジン1は、排気行程において、吸気バルブ15が閉弁状態を維持する一方、排気バルブ16が開弁すると共に、ピストン13が下死点側から上死点側に移動することにより、水蒸気とアルゴンとを含む排気ガスが燃焼室CC内から循環経路20の排気ポート11cを介して排気管18に排出される。 Next, in the working gas circulation engine 1, in the exhaust stroke, the intake valve 15 is kept closed, the exhaust valve 16 is opened, and the piston 13 is moved from the bottom dead center side to the top dead center side. As a result, the exhaust gas containing water vapor and argon is discharged from the combustion chamber CC to the exhaust pipe 18 via the exhaust port 11c of the circulation path 20.
 そして、作動ガス循環型エンジン1は、水蒸気とアルゴンとを含む排気ガスが燃焼室CC内から循環経路20に排出され、この排気ガスが燃焼室CCに向けて循環経路20を循環する際には、凝縮器60にて排気ガス中の水蒸気が液化・凝縮され分離される。これにより、作動ガス循環型エンジン1は、比熱比の小さい水蒸気が燃焼室CCに供給されず、比熱比の大きい作動ガスとしてのアルゴンが燃焼室CCへと再び供給されるので、作動ガスによる熱効率の高い運転を行うことができる。 In the working gas circulation engine 1, exhaust gas containing water vapor and argon is discharged from the combustion chamber CC to the circulation path 20, and when this exhaust gas circulates in the circulation path 20 toward the combustion chamber CC. In the condenser 60, the water vapor in the exhaust gas is liquefied, condensed and separated. As a result, the working gas circulation engine 1 does not supply steam with a small specific heat ratio to the combustion chamber CC, and again supplies argon as a working gas with a large specific heat ratio to the combustion chamber CC. High driving can be performed.
 ところで、この作動ガス循環型エンジン1は、上述したように、排気ガスを循環ガスとして燃焼室CCに向けて循環させる際に、凝縮器60において排気ガスの中の水蒸気を取り除く。そして、作動ガス循環型エンジン1は、比熱比の小さい水蒸気を燃焼室CCに供給せず、比熱比の大きい作動ガスとしてのアルゴンを燃焼室CCへ再び供給することで、熱効率の高い運転を行っている。このとき、この作動ガス循環型エンジン1は、凝縮器60によって分離された凝縮水を凝縮水排出口60cから凝縮水排出通路64に排出し循環経路20の系外に排水し、単純に凝縮水貯留タンク70に貯留するだけでは凝縮水貯留タンク70の大きさに限界があるため搭載性が悪化するなど種々の問題が生じうるおそれがあることから、この凝縮水を適正に処理する必要がある。 Incidentally, as described above, the working gas circulation engine 1 removes water vapor in the exhaust gas in the condenser 60 when the exhaust gas is circulated toward the combustion chamber CC as a circulation gas. The working gas circulation engine 1 does not supply water vapor with a small specific heat ratio to the combustion chamber CC, but again supplies argon as a working gas with a large specific heat ratio to the combustion chamber CC, thereby performing an operation with high thermal efficiency. ing. At this time, the working gas circulation engine 1 discharges the condensed water separated by the condenser 60 from the condensed water discharge port 60c to the condensed water discharge passage 64, drains it outside the system of the circulation path 20, and simply condensate water. Since the size of the condensed water storage tank 70 is limited only by being stored in the storage tank 70, various problems such as deterioration of the mountability may occur. Therefore, it is necessary to appropriately process this condensed water. .
 例えば、作動ガス循環型エンジン1は、燃焼後の高温の排気ガスが流れる排気管18を覆うようにして凝縮水を貯留するための凝縮水貯留タンクを設けて排気熱を利用してこの凝縮水を蒸発させてから処理することで、凝縮水を適正に処理することもできるが、この場合、搭載性の面でさらなる向上の余地がある。すなわち、作動ガス循環型エンジン1は、上記のように排気管18を覆うようにして凝縮水貯留タンクを設けて排気熱を利用してこの凝縮水を蒸発させる場合、凝縮水貯留タンクに貯留された凝縮水と排気管18の外面とを接触させるために排気管18近傍の限られた搭載スペースに凝縮水貯留タンクを配置しなければならい。このため、作動ガス循環型エンジン1は、凝縮水貯留タンクの搭載における自由度が少なくなり、例えば、十分な凝縮水貯留タンクの容量を確保するために作動ガス循環型エンジン1の大型化をまねいたり逆に十分な凝縮水貯留タンクの容量を確保できなかったりするおそれがある。 For example, the working gas circulation engine 1 is provided with a condensate water storage tank for storing condensate water so as to cover the exhaust pipe 18 through which high-temperature exhaust gas after combustion flows. Although the condensed water can be appropriately treated by treating after evaporating the water, there is room for further improvement in terms of mountability. That is, the working gas circulation engine 1 is stored in the condensed water storage tank when the condensed water storage tank is provided so as to cover the exhaust pipe 18 as described above and the condensed water is evaporated using the exhaust heat. In order to bring the condensed water into contact with the outer surface of the exhaust pipe 18, the condensed water storage tank must be disposed in a limited mounting space near the exhaust pipe 18. For this reason, the working gas circulation engine 1 has less freedom in mounting the condensed water storage tank. For example, to ensure a sufficient capacity of the condensed water storage tank, the working gas circulation engine 1 is made larger. On the other hand, there is a risk that sufficient condensate storage tank capacity cannot be secured.
 そこで、本実施形態の作動ガス循環型エンジン1は、図1に示すように、凝縮水貯留手段としての凝縮水貯留タンク70に貯留される凝縮水を圧送手段としての圧送部80により大気圧よりも高い圧力で蒸発手段としての熱交換器90に圧送し、この熱交換器90により圧送された凝縮水を排気ガスの排気熱を利用して蒸発させることで、凝縮水を適正に処理している。 Therefore, the working gas circulation engine 1 of the present embodiment, as shown in FIG. 1, causes the condensed water stored in the condensed water storage tank 70 as the condensed water storage means to be discharged from the atmospheric pressure by the pressure feeding unit 80 as the pressure feeding means. The condensed water is pumped to the heat exchanger 90 as the evaporation means at a high pressure, and the condensed water pumped by the heat exchanger 90 is evaporated using the exhaust heat of the exhaust gas, so that the condensed water is appropriately processed. Yes.
 凝縮水貯留タンク70は、凝縮水を貯留可能なものである。すなわち、凝縮水貯留タンク70は、凝縮器60によって分離された凝縮水を貯留可能なものであり、凝縮水排出通路64に接続されている。したがって、凝縮器60によって分離された凝縮水は、凝縮器60の凝縮水排出口60cを介して凝縮水排出通路64に排出され、この凝縮水貯留タンク70に排水される。 The condensed water storage tank 70 can store condensed water. In other words, the condensed water storage tank 70 can store the condensed water separated by the condenser 60 and is connected to the condensed water discharge passage 64. Therefore, the condensed water separated by the condenser 60 is discharged to the condensed water discharge passage 64 via the condensed water discharge port 60 c of the condenser 60 and discharged to the condensed water storage tank 70.
 圧送部80は、凝縮水貯留タンク70に貯留される凝縮水を大気圧よりも高い圧力で圧送するものである。本実施形態の圧送部80は、凝縮水経路81と、凝縮水ポンプ82とを有する。 The pressure feeding unit 80 pumps the condensed water stored in the condensed water storage tank 70 at a pressure higher than the atmospheric pressure. The pumping unit 80 of this embodiment includes a condensed water path 81 and a condensed water pump 82.
 凝縮水経路81は、内部を凝縮水が流動可能なものである。凝縮水経路81は、凝縮水貯留タンク70と後述の熱交換器90とを凝縮水が流動可能に接続する。ここでは、凝縮水経路81は、上述の凝縮水排出通路64と、大気開放通路83とを含んで構成される。 Condensed water path 81 allows condensed water to flow inside. The condensed water path 81 connects the condensed water storage tank 70 and a heat exchanger 90 described later so that condensed water can flow. Here, the condensed water path 81 is configured to include the above-described condensed water discharge path 64 and the atmosphere opening path 83.
 凝縮水排出通路64は、上述したように凝縮器60の凝縮水排出口60cと凝縮水貯留タンク70とを接続するものであり、一端が凝縮器60の凝縮水排出口60cに接続され、他端が凝縮水貯留タンク70内部の凝縮水を貯留する空間部に開口する。これにより、凝縮器60によって分離された凝縮水は、凝縮水排出口60c、凝縮水排出通路64を介して凝縮水貯留タンク70に排出され、この凝縮水貯留タンク70に貯留される。 As described above, the condensed water discharge passage 64 connects the condensed water discharge port 60c of the condenser 60 and the condensed water storage tank 70, and one end is connected to the condensed water discharge port 60c of the condenser 60. The end opens to a space for storing condensed water inside the condensed water storage tank 70. Thereby, the condensed water separated by the condenser 60 is discharged to the condensed water storage tank 70 via the condensed water discharge port 60 c and the condensed water discharge passage 64, and stored in the condensed water storage tank 70.
 大気開放通路83は、凝縮水貯留タンク70の内部を後述する熱交換器90を介して大気に開放するものであり、一端が凝縮水貯留タンク70内部の凝縮水を貯留する空間部に開口し、他端が大気に開口する。後述する熱交換器90は、この大気開放通路83に設けられる。これにより、後述するように、凝縮水貯留タンク70から大気開放通路83を介して熱交換器90に圧送された凝縮水は、熱交換器90にて蒸発し水蒸気となり、この水蒸気は、大気開放通路83の他端から大気に開放される。 The atmosphere opening passage 83 opens the inside of the condensed water storage tank 70 to the atmosphere via a heat exchanger 90 to be described later, and one end opens to a space for storing condensed water inside the condensed water storage tank 70. The other end opens to the atmosphere. A heat exchanger 90 described later is provided in the atmosphere opening passage 83. As a result, as will be described later, the condensed water pumped from the condensed water storage tank 70 to the heat exchanger 90 via the atmosphere release passage 83 evaporates in the heat exchanger 90 to become water vapor, and this water vapor is released to the atmosphere. The other end of the passage 83 is opened to the atmosphere.
 つまり、凝縮水経路81は、全体として、凝縮水排出通路64側の一端が凝縮器60の凝縮水排出口60cに接続し、大気開放通路83側の他端が大気に開放された経路をなし、凝縮水排出通路64と大気開放通路83との間に凝縮水貯留タンク70が設けられ、大気開放通路83上に熱交換器90が設けられる。 That is, the condensed water path 81 as a whole is a path in which one end on the condensed water discharge passage 64 side is connected to the condensed water discharge port 60c of the condenser 60 and the other end on the atmosphere opening passage 83 side is opened to the atmosphere. The condensed water storage tank 70 is provided between the condensed water discharge passage 64 and the atmosphere release passage 83, and the heat exchanger 90 is provided on the atmosphere release passage 83.
 凝縮水ポンプ82は、凝縮水経路81に設けられ凝縮水を加圧し凝縮水貯留タンク70側から熱交換器90側に圧送するものである。本実施形態の凝縮水ポンプ82は、凝縮水経路81のうちの大気開放通路83上に設けられている。凝縮水ポンプ82は、大気開放通路83において、凝縮水貯留タンク70内部に位置する大気開放通路83の開口と、後述する熱交換器90との間に設けられている。 The condensate pump 82 is provided in the condensate path 81 and pressurizes the condensate and pumps it from the condensate storage tank 70 side to the heat exchanger 90 side. The condensed water pump 82 of the present embodiment is provided on the atmosphere opening passage 83 in the condensed water path 81. The condensed water pump 82 is provided in the atmosphere opening passage 83 between the opening of the atmosphere opening passage 83 located inside the condensed water storage tank 70 and a heat exchanger 90 described later.
 凝縮水ポンプ82は、凝縮水貯留タンク70内部に位置する大気開放通路83の開口を介して凝縮水貯留タンク70に貯留される凝縮水を大気開放通路83に吸引し、この凝縮水を大気圧よりも高い圧力に加圧して圧送する。凝縮水ポンプ82は、凝縮水経路81の大気開放通路83内の凝縮水の圧力を大気圧よりも高い圧力に加圧した上で凝縮水貯留タンク70側から熱交換器90側に圧送する。したがって、大気開放通路83を凝縮水ポンプ82により大気圧よりも高い圧力で圧送される凝縮水(後述する熱交換器90で蒸発した後は水蒸気)は、凝縮水貯留タンク70側から大気側に一方向に流れ、逆流することが防止される。なお、この凝縮水ポンプ82は、例えば、電子制御装置50によりその駆動が制御されることで凝縮水の圧送量を調節することができる。 The condensed water pump 82 sucks condensed water stored in the condensed water storage tank 70 into the atmosphere opening passage 83 through an opening of the atmosphere opening passage 83 located inside the condensed water storage tank 70, and this condensed water is atmospheric pressure. Pressurize to a higher pressure. The condensed water pump 82 pressurizes the pressure of the condensed water in the atmosphere open passage 83 of the condensed water path 81 to a pressure higher than the atmospheric pressure, and then pumps the condensed water from the condensed water storage tank 70 side to the heat exchanger 90 side. Therefore, the condensed water pumped by the condensed water pump 82 at a pressure higher than the atmospheric pressure (water vapor after being evaporated by the heat exchanger 90 described later) from the condensed water storage tank 70 side to the atmosphere side. It flows in one direction and is prevented from flowing back. In addition, this condensed water pump 82 can adjust the pumping amount of condensed water by the drive being controlled by the electronic control apparatus 50, for example.
 熱交換器90は、圧送部80により圧送された凝縮水を排気ガスの排気熱により蒸発させるものである。熱交換器90は、排気ガスと凝縮水とを熱交換させることで、排気ガスの排気熱によりこの凝縮水を蒸発させる。この熱交換器90は、循環経路20に設けられる。本実施形態の熱交換器90は、循環通路21のうちの第2循環通路21b上に設けられる。すなわち、熱交換器90は、第2循環通路21bにおいて、排気ポート11cと凝縮器60との間に設けられ、内部に排気ガスを導入する排気ガス導入口90aが第2循環通路21bの排気ポート11c側に接続され、内部から排気ガスを排出する排気ガス排出口90bが第2循環通路21bの凝縮器60側に接続される。そして、熱交換器90は、凝縮水経路81の大気開放通路83が内部を通るようにして接続されている。言い換えれば、凝縮水経路81は、熱交換器90の内部を通るようにして設けられる。 The heat exchanger 90 evaporates the condensed water pumped by the pumping unit 80 by the exhaust heat of the exhaust gas. The heat exchanger 90 evaporates the condensed water by the exhaust heat of the exhaust gas by exchanging heat between the exhaust gas and the condensed water. The heat exchanger 90 is provided in the circulation path 20. The heat exchanger 90 of the present embodiment is provided on the second circulation passage 21 b in the circulation passage 21. That is, the heat exchanger 90 is provided between the exhaust port 11c and the condenser 60 in the second circulation passage 21b, and the exhaust gas introduction port 90a for introducing the exhaust gas therein is provided in the exhaust port of the second circulation passage 21b. An exhaust gas discharge port 90b that is connected to the 11c side and discharges exhaust gas from the inside is connected to the condenser 60 side of the second circulation passage 21b. The heat exchanger 90 is connected so that the atmosphere opening passage 83 of the condensed water passage 81 passes through the inside. In other words, the condensed water path 81 is provided so as to pass through the inside of the heat exchanger 90.
 したがって、熱交換器90は、第2循環通路21bを流れる排気ガスと、大気開放通路83を凝縮水ポンプ82により圧送されて流れる凝縮水とが熱交換することで、排気ガスの排気熱によりこの凝縮水を蒸発させることができる。ここでは、熱交換器90は、循環経路20を循環する作動ガスの循環方向に対して凝縮器60より上流側の排気ガス、すなわち、燃焼後の高温の排気ガスの排気熱により凝縮水を蒸発させることができる。 Therefore, the heat exchanger 90 exchanges heat between the exhaust gas flowing through the second circulation passage 21b and the condensed water that is pumped through the atmosphere opening passage 83 by the condensed water pump 82, and this heat is generated by the exhaust heat of the exhaust gas. The condensed water can be evaporated. Here, the heat exchanger 90 evaporates the condensed water by the exhaust gas upstream of the condenser 60 with respect to the circulation direction of the working gas circulating in the circulation path 20, that is, the exhaust heat of the high-temperature exhaust gas after combustion. Can be made.
 上記のように構成される作動ガス循環型エンジン1は、凝縮器60によって分離された凝縮水が凝縮水排出口60c、凝縮水排出通路64を介して凝縮水貯留タンク70に排出され、この凝縮水貯留タンク70に貯留される。凝縮水貯留タンク70に貯留された凝縮水は、凝縮水ポンプ82が駆動することで凝縮水貯留タンク70内部に位置する大気開放通路83の開口を介して大気開放通路83に吸引され大気圧よりも高い圧力に加圧されて熱交換器90に向けて圧送される。そして、大気開放通路83を熱交換器90に向けて圧送された凝縮水は、熱交換器90に至る。 In the working gas circulation engine 1 configured as described above, the condensed water separated by the condenser 60 is discharged to the condensed water storage tank 70 via the condensed water discharge port 60c and the condensed water discharge passage 64. It is stored in the water storage tank 70. The condensed water stored in the condensed water storage tank 70 is sucked into the atmospheric open passage 83 through the opening of the atmospheric open passage 83 located inside the condensed water storage tank 70 when the condensed water pump 82 is driven. Is pressurized to a high pressure and fed toward the heat exchanger 90. Then, the condensed water pressure-fed toward the heat exchanger 90 through the atmosphere opening passage 83 reaches the heat exchanger 90.
 そして、大気開放通路83を凝縮水ポンプ82により圧送されて流れ熱交換器90に至った凝縮水は、この熱交換器90にて、第2循環通路21bを流れ熱交換器90内部に導入された排気ガスと熱交換することで、この排気ガスの排気熱を吸収し温度が上昇し、この結果、蒸発し水蒸気となる。そして、熱交換器90で凝縮水が蒸発することで発生する水蒸気は、大気開放通路83を熱交換器90側から大気側に一方向に流れ、大気開放通路83の開口から大気に開放される。 Then, the condensed water that is pumped by the condensed water pump 82 through the atmosphere opening passage 83 and reaches the heat exchanger 90 flows through the second circulation passage 21b and is introduced into the heat exchanger 90 by the heat exchanger 90. By exchanging heat with the exhaust gas, the heat of the exhaust gas is absorbed and the temperature rises. As a result, it evaporates and becomes water vapor. The water vapor generated by the evaporation of the condensed water in the heat exchanger 90 flows in one direction from the heat exchanger 90 side to the atmosphere side through the atmosphere opening passage 83 and is released from the opening of the atmosphere opening passage 83 to the atmosphere. .
 この結果、作動ガス循環型エンジン1は、凝縮水貯留タンク70の凝縮水を熱交換器90で排気ガスの排気熱を利用して蒸発させて水蒸気として大気に放出することで凝縮器60によって分離された凝縮水を適正に処理することができるので、凝縮水貯留タンク70の容量を相対的に小さくすることができ、作動ガス循環型エンジン1の車両への搭載性を向上することができる。 As a result, the working gas circulation engine 1 is separated by the condenser 60 by evaporating the condensed water in the condensed water storage tank 70 by using the exhaust heat of the exhaust gas in the heat exchanger 90 and releasing it into the atmosphere as water vapor. Since the condensed water thus treated can be appropriately processed, the capacity of the condensed water storage tank 70 can be relatively reduced, and the mounting property of the working gas circulation engine 1 on the vehicle can be improved.
 また、この作動ガス循環型エンジン1は、凝縮水貯留タンク70に貯留される凝縮水を圧送部80により熱交換器90に圧送しこの凝縮水を蒸発させることから、例えば、凝縮水貯留タンク70に貯留された凝縮水と第2循環通路21bをなす排気管18の外面とを直接接触させる必要がなく、排気管18近傍の限られた搭載スペースに凝縮水貯留タンク70を配置する必要がない。この結果、この作動ガス循環型エンジン1は、凝縮水貯留タンク70の搭載場所の自由度を向上させることができる。したがって、この作動ガス循環型エンジン1は、例えば、十分な凝縮水貯留タンク70の容量を確保するために作動ガス循環型エンジン1の大型化をまねいたり逆に十分な凝縮水貯留タンク70の容量を確保できなかったりすることを防止することができる。さらに、この作動ガス循環型エンジン1は、凝縮水が直接的に第2循環通路21bをなす排気管18に接触していないので、排気管18が局所的に温度低下することを防止することができ、この結果、排気管18に熱ひずみが生じることを抑制することができ、よって、排気管18の耐久性を向上することができる。 Further, the working gas circulation engine 1 pumps the condensed water stored in the condensed water storage tank 70 to the heat exchanger 90 by the pumping unit 80 and evaporates the condensed water. Therefore, it is not necessary to directly contact the condensed water stored in the exhaust pipe 18 and the outer surface of the exhaust pipe 18 forming the second circulation passage 21b, and it is not necessary to arrange the condensed water storage tank 70 in a limited mounting space near the exhaust pipe 18. . As a result, this working gas circulation engine 1 can improve the degree of freedom of the place where the condensed water storage tank 70 is mounted. Therefore, this working gas circulation engine 1 may, for example, increase the size of the working gas circulation engine 1 in order to ensure a sufficient capacity of the condensed water storage tank 70, or conversely, a sufficient capacity of the condensed water storage tank 70. Can not be secured. Further, in this working gas circulation engine 1, since the condensed water is not in direct contact with the exhaust pipe 18 forming the second circulation passage 21b, it is possible to prevent the exhaust pipe 18 from locally lowering the temperature. As a result, it is possible to suppress the occurrence of thermal distortion in the exhaust pipe 18, thereby improving the durability of the exhaust pipe 18.
 またこのとき、作動ガス循環型エンジン1は、凝縮水貯留タンク70に貯留される凝縮水を圧送部80により大気圧よりも高い圧力で熱交換器90に圧送し熱交換器90で発生した水蒸気を大気に放出することから、大気開放通路83を流れる凝縮水及び熱交換器90で蒸発した後は水蒸気が凝縮水貯留タンク70側から熱交換器90を介して大気側に一方向に流れるようにすることができ、凝縮水、水蒸気が大気開放通路83内を逆流することを防止することができる。この結果、作動ガス循環型エンジン1は、凝縮水貯留タンク70に貯留される凝縮水を圧送部80により熱交換器90に圧送しこの凝縮水を蒸発させ、確実に大気に放出することができる。 At this time, the working gas circulation engine 1 pumps the condensed water stored in the condensed water storage tank 70 to the heat exchanger 90 at a pressure higher than the atmospheric pressure by the pumping unit 80 and generates water vapor generated in the heat exchanger 90. From the condensed water storage tank 70 side through the heat exchanger 90 to the atmosphere side in one direction after the condensed water and the heat exchanger 90 evaporate. It is possible to prevent the condensed water and water vapor from flowing back through the atmosphere opening passage 83. As a result, the working gas circulation engine 1 can pump the condensed water stored in the condensed water storage tank 70 to the heat exchanger 90 by the pumping unit 80, evaporate the condensed water, and reliably release it to the atmosphere. .
 さらに、この作動ガス循環型エンジン1は、熱交換器90が循環経路20を循環する作動ガスの循環方向に対して凝縮器60より上流側の第2循環通路21bに設けられることから、熱交換器90が凝縮器60に到達する前の排気ガスの排気熱を凝縮水に吸収させることができるので、凝縮器60に導入される前の排気ガスの温度を低下させることができる。この結果、作動ガス循環型エンジン1は、凝縮器60に導入される排気ガスの温度を低下させることができることから、排気ガス中の水蒸気が液化・凝縮される温度にまで排気ガス温度を下げることのできる凝縮器60、ラジエータ63の容量を小さくすることができるので、凝縮器60、ラジエータ63を小型化することができる。つまり、この作動ガス循環型エンジン1は、凝縮器60に導入される排気ガスの温度を低下させることができることから、凝縮器60で冷却水が排気ガスから奪う熱量が少なくてすみ、よって、凝縮器60、ラジエータ63の容量を小さくすることができる。言い換えれば、この作動ガス循環型エンジン1は、比較的容量の小さい凝縮器60、ラジエータ63によって排気ガスから水蒸気を分離することができ作動ガスの平均比熱比の低下を防止することができることから、作動ガス循環型エンジン1を小型化し搭載性を向上した上で高効率運転を維持することができる。 Furthermore, this working gas circulation engine 1 is provided in the second circulation passage 21b upstream of the condenser 60 with respect to the circulation direction of the working gas in which the heat exchanger 90 circulates in the circulation path 20, so that heat exchange is performed. Since the exhaust heat of the exhaust gas before the condenser 90 reaches the condenser 60 can be absorbed by the condensed water, the temperature of the exhaust gas before being introduced into the condenser 60 can be lowered. As a result, since the working gas circulation engine 1 can lower the temperature of the exhaust gas introduced into the condenser 60, the exhaust gas temperature is lowered to a temperature at which the water vapor in the exhaust gas is liquefied and condensed. Since the capacities of the condenser 60 and the radiator 63 that can be reduced can be reduced, the condenser 60 and the radiator 63 can be reduced in size. In other words, since the working gas circulation engine 1 can reduce the temperature of the exhaust gas introduced into the condenser 60, the amount of heat that the cooling water takes from the exhaust gas in the condenser 60 can be reduced. The capacity of the device 60 and the radiator 63 can be reduced. In other words, the working gas circulation engine 1 can separate the water vapor from the exhaust gas by the condenser 60 and the radiator 63 having a relatively small capacity, and can prevent a decrease in the average specific heat ratio of the working gas. The highly efficient operation can be maintained while the working gas circulation engine 1 is downsized and mountability is improved.
 さらに言い換えれば、この作動ガス循環型エンジン1は、例えば凝縮器60に対するラジエータ63とは別個に凝縮器、ラジエータ等を設けることなく、熱交換器90における排気ガスと凝縮水との熱交換により排気ガスの温度を低下させることができるので、この点においても作動ガス循環型エンジン1を小型化することができ、この結果、作動ガス循環型エンジン1の車両への搭載性を向上することができる。なお、作動ガス循環型エンジン1では、熱交換器90にて排気ガスと凝縮水とが熱交換することで結果的に生じた凝縮水は、例えば、第2循環通路21b、排気ガス導入口60a、凝縮器60、凝縮水排出口60c及び凝縮水排出通路64を介して凝縮水貯留タンク70に排出してもよいし、これとは別系統の凝縮水排出通路(不図示)を介して凝縮水貯留タンク70に排出するようにしてもよい。 In other words, this working gas circulation engine 1 is exhausted by exchanging heat between the exhaust gas and the condensed water in the heat exchanger 90 without providing a condenser, a radiator, etc. separately from the radiator 63 for the condenser 60, for example. Since the temperature of the gas can be lowered, the working gas circulation engine 1 can be downsized also in this respect, and as a result, the mounting property of the working gas circulation engine 1 on the vehicle can be improved. . In the working gas circulation engine 1, the condensate resulting from the heat exchange between the exhaust gas and the condensed water in the heat exchanger 90 is, for example, the second circulation passage 21 b and the exhaust gas inlet 60 a. , It may be discharged to the condensed water storage tank 70 via the condenser 60, the condensed water discharge port 60c and the condensed water discharge passage 64, or condensed via a condensed water discharge passage (not shown) of a separate system. You may make it discharge to the water storage tank 70. FIG.
 以上で説明した本発明の実施形態に係る作動ガス循環型エンジン1によれば、酸化剤としての酸素と、この酸素との燃焼により水蒸気を生成する燃料としての水素と、空気より比熱比の高いアルゴンとが供給され、水素の燃焼に伴ってアルゴンが膨張可能であると共に水素の燃焼後の排気ガスとして水蒸気とアルゴンとを排気可能な燃焼室CCと、排気ガス中に含まれるアルゴンを燃焼室CCの排気側から吸気側に循環させ再び燃焼室CCに供給可能な循環経路20と、循環経路20に設けられ排気ガス中に含まれる水蒸気を凝縮して凝縮水とする凝縮器60と、凝縮水を貯留可能な凝縮水貯留タンク70と、凝縮水貯留タンク70に貯留される凝縮水を大気圧よりも高い圧力で圧送する圧送部80と、圧送部80により圧送された凝縮水を排気ガスの排気熱により蒸発させる熱交換器90とを備える。 According to the working gas circulation engine 1 according to the embodiment of the present invention described above, oxygen as an oxidant, hydrogen as a fuel that generates water vapor by combustion with this oxygen, and a specific heat ratio higher than that of air. Argon is supplied and can expand as the hydrogen burns, and the combustion chamber CC is capable of exhausting water vapor and argon as the exhaust gas after the hydrogen combustion, and the argon contained in the exhaust gas is the combustion chamber. A circulation path 20 that can be circulated from the exhaust side of the CC to the intake side and supplied to the combustion chamber CC again, a condenser 60 that is provided in the circulation path 20 and that condenses water vapor contained in the exhaust gas into condensed water, The condensed water storage tank 70 capable of storing water, the pumping unit 80 for pumping the condensed water stored in the condensed water storage tank 70 at a pressure higher than the atmospheric pressure, and the condensed water pumped by the pumping unit 80 The exhaust heat of the exhaust gas and a heat exchanger 90 to evaporate.
 したがって、作動ガス循環型エンジン1は、凝縮水貯留タンク70に貯留される凝縮水を圧送部80により大気圧よりも高い圧力で熱交換器90に圧送し、熱交換器90によりこの圧送された凝縮水を排気ガスの排気熱を利用して蒸発させることから、凝縮水貯留タンク70に貯留されている凝縮水を水蒸気として大気に放出することができ、この結果、例えば、作動ガス循環型エンジン1の車両への搭載性を向上し、凝縮器60によって分離された凝縮水を適正に処理することができる。 Therefore, the working gas circulation engine 1 pumps the condensed water stored in the condensed water storage tank 70 to the heat exchanger 90 at a pressure higher than the atmospheric pressure by the pressure feeding unit 80, and the pressure is fed by the heat exchanger 90. Since the condensed water is evaporated using the exhaust heat of the exhaust gas, the condensed water stored in the condensed water storage tank 70 can be discharged to the atmosphere as water vapor. As a result, for example, a working gas circulation engine 1 can be mounted on the vehicle, and the condensed water separated by the condenser 60 can be appropriately treated.
 さらに、以上で説明した本発明の実施形態に係る作動ガス循環型エンジン1によれば、酸化剤は、酸素であり、燃料は、水素である。したがって、作動ガス循環型エンジン1は、酸素と水素との燃焼によって発生する水蒸気を凝縮器60によって凝縮水として分離し、この凝縮水を凝縮水貯留タンク70に一旦貯留した上で、圧送部80と熱交換器90とにより水蒸気として大気に放出し、適正に処理することができる。 Furthermore, according to the working gas circulation engine 1 according to the embodiment of the present invention described above, the oxidant is oxygen and the fuel is hydrogen. Therefore, the working gas circulation engine 1 separates the water vapor generated by the combustion of oxygen and hydrogen as condensed water by the condenser 60, temporarily stores the condensed water in the condensed water storage tank 70, and then presses the pressure feeding unit 80. And the heat exchanger 90 can be discharged into the atmosphere as water vapor and processed appropriately.
 さらに、以上で説明した本発明の実施形態に係る作動ガス循環型エンジン1によれば、熱交換器90は、循環経路20を循環する作動ガスの循環方向に対して凝縮器60より上流側の排気ガスの排気熱により凝縮水を蒸発させる。したがって、作動ガス循環型エンジン1は、熱交換器90が循環経路20を循環する作動ガスの循環方向に対して凝縮器60より上流側の排気ガスの排気熱により凝縮水を蒸発させることから、比較的に高温の排気ガスの排気熱により凝縮水を効率的に蒸発させることができる。さらに、作動ガス循環型エンジン1は、凝縮器60に到達する前の排気ガスの排気熱を凝縮水に吸収させることができるので、凝縮器60に導入される排気ガスの温度を低下させることができ、凝縮器60、ラジエータ63の容量を小さくすることができる。この結果、作動ガス循環型エンジン1は、凝縮器60、ラジエータ63を小型化することができ、凝縮器60によって分離された凝縮水を適正に処理した上で搭載性をさらに向上することができる。 Further, according to the working gas circulation engine 1 according to the embodiment of the present invention described above, the heat exchanger 90 is located upstream of the condenser 60 with respect to the circulation direction of the working gas circulating in the circulation path 20. The condensed water is evaporated by the exhaust heat of the exhaust gas. Accordingly, the working gas circulation engine 1 evaporates the condensed water by the exhaust heat of the exhaust gas upstream of the condenser 60 with respect to the circulation direction of the working gas through which the heat exchanger 90 circulates in the circulation path 20. The condensed water can be efficiently evaporated by the exhaust heat of the relatively high temperature exhaust gas. Furthermore, since the working gas circulation engine 1 can absorb the exhaust heat of the exhaust gas before reaching the condenser 60 into the condensed water, the temperature of the exhaust gas introduced into the condenser 60 can be reduced. The capacity of the condenser 60 and the radiator 63 can be reduced. As a result, the working gas circulation engine 1 can reduce the size of the condenser 60 and the radiator 63, and can further improve the mountability after properly treating the condensed water separated by the condenser 60. .
 さらに、以上で説明した本発明の実施形態に係る作動ガス循環型エンジン1によれば、圧送部80は、凝縮水貯留タンク70と熱交換器90とを凝縮水が流動可能に接続する凝縮水経路81と、凝縮水経路81に設けられこの凝縮水経路81の凝縮水を加圧し凝縮水貯留タンク70側から熱交換器90側に圧送する凝縮水ポンプ82とを有する。したがって、作動ガス循環型エンジン1は、凝縮水貯留タンク70に貯留される凝縮水を凝縮水ポンプ82により大気圧よりも高い圧力で凝縮水経路81を介して熱交換器90に圧送し熱交換器90で発生した水蒸気を大気に放出することから、凝縮水経路81を流れる凝縮水(熱交換器90で蒸発した後は水蒸気)が逆流することを確実に防止することができる。この結果、作動ガス循環型エンジン1は、凝縮水貯留タンク70に貯留される凝縮水を圧送部80により熱交換器90に圧送しこの凝縮水を蒸発させ、確実に大気に放出することができる。 Furthermore, according to the working gas circulation engine 1 according to the embodiment of the present invention described above, the pressure feeding unit 80 connects the condensed water storage tank 70 and the heat exchanger 90 so that the condensed water can flow. A condensate water pump 82 is provided in the condensate water path 81 and pressurizes the condensate water in the condensate water path 81 and pumps it from the condensate water storage tank 70 side to the heat exchanger 90 side. Therefore, the working gas circulation engine 1 pumps the condensed water stored in the condensed water storage tank 70 to the heat exchanger 90 via the condensed water path 81 at a pressure higher than the atmospheric pressure by the condensed water pump 82 to exchange heat. Since the water vapor generated in the vessel 90 is released to the atmosphere, it is possible to reliably prevent the condensed water flowing through the condensed water path 81 (water vapor after being evaporated in the heat exchanger 90) from flowing backward. As a result, the working gas circulation engine 1 can pump the condensed water stored in the condensed water storage tank 70 to the heat exchanger 90 by the pumping unit 80, evaporate the condensed water, and reliably release it to the atmosphere. .
 なお、以上の説明では、熱交換器90は、第2循環通路21bに設けられ循環経路20を循環する作動ガスの循環方向に対して凝縮器60より上流側の排気ガスの排気熱により凝縮水を蒸発させるものとして説明するがこれに限らない。熱交換器90は、循環通路21において、排気ガスの排気熱から凝縮水を十分に蒸発させることができる程度の熱量を得ることができる部分であれば、例えば凝縮器60の下流側に設けられていてもよい。ただし、燃焼後の排気ガスの排気熱は、燃焼室CCの排気ポート11c側に近いほど相対的に高温となることから、熱交換器90は、循環通路21において、比較的に燃焼室CCの排気ポート11c側に近い位置に設けられることが好ましい。熱交換器90は、例えば、凝縮器60の作動ガス排出口60bより上流側に設けられることが好ましく、さらに言えば、以上で説明したように凝縮器60の排気ガス導入口60aより上流側に設けられることがさらに好ましい。 In the above description, the heat exchanger 90 is condensed water by the exhaust heat of the exhaust gas upstream of the condenser 60 with respect to the circulation direction of the working gas provided in the second circulation passage 21b and circulating in the circulation path 20. However, the present invention is not limited to this. The heat exchanger 90 is provided, for example, on the downstream side of the condenser 60 in the circulation passage 21 as long as it can obtain a heat quantity sufficient to evaporate the condensed water from the exhaust heat of the exhaust gas. It may be. However, since the exhaust heat of the exhaust gas after combustion becomes relatively high as it becomes closer to the exhaust port 11c side of the combustion chamber CC, the heat exchanger 90 is relatively in the combustion chamber CC in the circulation passage 21. It is preferable to be provided at a position close to the exhaust port 11c side. For example, the heat exchanger 90 is preferably provided on the upstream side of the working gas discharge port 60b of the condenser 60, and more specifically, on the upstream side of the exhaust gas introduction port 60a of the condenser 60 as described above. More preferably, it is provided.
 また、凝縮水経路81をなす大気開放通路83は、熱交換器90より凝縮水貯留タンク70側の一部が凝縮器60内部を通るようにしてもよい。この場合、凝縮器60の内部において、冷却水循環路61と大気開放通路83とが互いに独立した別系統となっていればよい。この場合、作動ガス循環型エンジン1は、大気開放通路83を熱交換器90側に向かって移動する凝縮水が凝縮器60において排気ガスの排気熱を吸収することで、熱交換器90に到達する前に予熱されるので、熱交換器90は、凝縮器60にて予熱された凝縮水を効率的に蒸発させることができる。 Further, the atmosphere opening passage 83 that forms the condensed water path 81 may be configured such that a part of the condensed water storage tank 70 side from the heat exchanger 90 passes inside the condenser 60. In this case, the cooling water circulation path 61 and the air release path 83 need only be separate from each other inside the condenser 60. In this case, the working gas circulation engine 1 reaches the heat exchanger 90 because the condensed water moving toward the heat exchanger 90 in the atmosphere opening passage 83 absorbs the exhaust heat of the exhaust gas in the condenser 60. Therefore, the heat exchanger 90 can efficiently evaporate the condensed water preheated in the condenser 60.
 また、圧送部80の凝縮水ポンプ82は、大気開放通路83以外に設けられていてもよい。 Further, the condensed water pump 82 of the pressure feeding unit 80 may be provided other than the atmosphere opening passage 83.
 図2は、本発明の変形例1に係る作動ガス循環型エンジンの模式的な概略構成図である。 FIG. 2 is a schematic configuration diagram of a working gas circulation engine according to Modification 1 of the present invention.
 本変形例に係る作動ガス循環型エンジン1Aは、図2に示すように、圧送手段としての圧送部80Aを備え、この圧送部80Aは、凝縮水経路81と、凝縮水ポンプ82Aとを有する。凝縮水経路81は、凝縮水排出通路64と、大気開放通路83とを含んで構成される。そして、凝縮水ポンプ82Aは、凝縮水経路81に設けられ凝縮水を加圧し凝縮水貯留タンク70A側から熱交換器90側に圧送するものである。本変形例の凝縮水ポンプ82Aは、凝縮水経路81のうちの凝縮水排出通路64上に設けられている。 As shown in FIG. 2, the working gas circulation engine 1A according to the present modification includes a pumping unit 80A as a pumping unit, and the pumping unit 80A includes a condensed water path 81 and a condensed water pump 82A. The condensed water path 81 includes a condensed water discharge path 64 and an atmosphere opening path 83. The condensed water pump 82A is provided in the condensed water path 81, pressurizes condensed water, and pumps the condensed water from the condensed water storage tank 70A side to the heat exchanger 90 side. The condensed water pump 82 </ b> A of this modification is provided on the condensed water discharge passage 64 in the condensed water path 81.
 そして、本変形例の凝縮水貯留手段としての凝縮水貯留タンク70Aは、凝縮水を貯留する空間部が密閉状態とされている。したがって、凝縮水ポンプ82Aは、凝縮水排出通路64内の凝縮水を内部空間が密閉状態とされた凝縮水貯留タンク70A側に向けて押し込むようにして圧送することで、凝縮水貯留タンク70A内部の圧力を大気圧よりも高い圧力に加圧し、凝縮水貯留タンク70Aに貯留される凝縮水を、大気開放通路83を介して熱交換器90側に向けて圧送することができる。 And the condensate water storage tank 70A as the condensate storage means of this modification has a sealed space for storing condensate. Therefore, the condensed water pump 82A pumps the condensed water in the condensed water discharge passage 64 so as to push it toward the condensed water storage tank 70A side in which the internal space is sealed, so that the inside of the condensed water storage tank 70A. Can be pressurized to a pressure higher than atmospheric pressure, and the condensed water stored in the condensed water storage tank 70 </ b> A can be pumped toward the heat exchanger 90 side through the atmosphere opening passage 83.
 この場合であっても、作動ガス循環型エンジン1Aは、凝縮水貯留タンク70Aに貯留される凝縮水を圧送部80Aにより大気圧よりも高い圧力で熱交換器90に圧送し、熱交換器90によりこの圧送された凝縮水を排気ガスの排気熱を利用して蒸発させることから、凝縮水貯留タンク70Aに貯留されている凝縮水を水蒸気として大気に放出することができ、この結果、例えば、作動ガス循環型エンジン1Aの車両への搭載性を向上し、凝縮器60によって分離された凝縮水を適正に処理することができる。 Even in this case, the working gas circulation engine 1A pumps the condensed water stored in the condensed water storage tank 70A to the heat exchanger 90 at a pressure higher than the atmospheric pressure by the pumping unit 80A. The condensed water thus pumped is evaporated using the exhaust heat of the exhaust gas, so that the condensed water stored in the condensed water storage tank 70A can be discharged to the atmosphere as water vapor. The mounting property of the working gas circulation engine 1A on the vehicle can be improved, and the condensed water separated by the condenser 60 can be appropriately treated.
 そして、この場合であっても、作動ガス循環型エンジン1Aは、凝縮水貯留タンク70Aに貯留される凝縮水を凝縮水ポンプ82Aにより大気圧よりも高い圧力で凝縮水経路81を介して熱交換器90に圧送し熱交換器90で発生した水蒸気を大気に放出することから、凝縮水経路81を流れる凝縮水及び水蒸気が逆流することを防止することができる。この結果、作動ガス循環型エンジン1は、凝縮水貯留タンク70Aに貯留される凝縮水を圧送部80Aにより熱交換器90に圧送しこの凝縮水を蒸発させ、確実に大気に放出することができる。 Even in this case, the working gas circulation engine 1A exchanges heat of the condensed water stored in the condensed water storage tank 70A through the condensed water path 81 at a pressure higher than the atmospheric pressure by the condensed water pump 82A. Since the water vapor generated by the heat exchanger 90 is pumped to the vessel 90 and released to the atmosphere, it is possible to prevent the condensed water and water vapor flowing through the condensed water passage 81 from flowing backward. As a result, the working gas circulation engine 1 can pump the condensed water stored in the condensed water storage tank 70A to the heat exchanger 90 by the pumping section 80A, evaporate the condensed water, and reliably release it to the atmosphere. .
(実施形態2)
 図3は、本発明の実施形態2に係る作動ガス循環型エンジンの模式的な概略構成図、図4は、本発明の変形例2に係る作動ガス循環型エンジンの模式的な概略構成図である。実施形態2に係る作動ガス循環型エンジンは、実施形態1に係る作動ガス循環型エンジンと略同様の構成であるが圧送手段の構成が実施形態1に係る作動ガス循環型エンジンとは異なる。その他、上述した実施形態と共通する構成、作用、効果については、重複した説明はできるだけ省略するとともに、同一の符号を付す。
(Embodiment 2)
FIG. 3 is a schematic schematic configuration diagram of a working gas circulation engine according to Embodiment 2 of the present invention, and FIG. 4 is a schematic schematic configuration diagram of a working gas circulation engine according to Modification 2 of the present invention. is there. The working gas circulation engine according to the second embodiment has substantially the same configuration as the working gas circulation engine according to the first embodiment, but the structure of the pressure feeding means is different from that of the working gas circulation engine according to the first embodiment. In addition, about the structure, effect | action, and effect which are common in embodiment mentioned above, while overlapping description is abbreviate | omitted as much as possible, the same code | symbol is attached | subjected.
 本実施形態に係る作動ガス循環型エンジン201は、図3に示すように、圧送手段としての圧送部280を備える。圧送部280は、凝縮水貯留タンク270に貯留される凝縮水を大気圧よりも高い圧力で圧送するものである。圧送部280は、凝縮水経路81を有し、この凝縮水経路81は、凝縮水排出通路64と、大気開放通路83とを含んで構成される。 The working gas circulation engine 201 according to the present embodiment includes a pressure feeding unit 280 as pressure feeding means, as shown in FIG. The pumping unit 280 pumps the condensed water stored in the condensed water storage tank 270 at a pressure higher than the atmospheric pressure. The pumping unit 280 includes a condensed water passage 81, and the condensed water passage 81 includes a condensed water discharge passage 64 and an air release passage 83.
 凝縮水経路81は、全体として、凝縮水排出通路64側の一端が凝縮器60の凝縮水排出口60cに接続し、大気開放通路83側の他端が大気に開放された経路をなし、凝縮水排出通路64と大気開放通路83との間に凝縮水貯留手段としての凝縮水貯留タンク270が設けられ、大気開放通路83上に熱交換器90が設けられる。 As a whole, the condensed water path 81 has a path in which one end on the condensed water discharge passage 64 side is connected to the condensed water discharge port 60c of the condenser 60 and the other end on the atmosphere opening path 83 side is opened to the atmosphere. A condensed water storage tank 270 as condensed water storage means is provided between the water discharge passage 64 and the atmosphere release passage 83, and a heat exchanger 90 is provided on the atmosphere release passage 83.
 ここで、本実施形態の圧送部280は、以上で説明した凝縮水ポンプ82(図1参照)や凝縮水ポンプ82A(図2参照)を備えていない点で圧送部80(図1参照)や圧送部80A(図2参照)とは異なる。 Here, the pumping unit 280 of the present embodiment does not include the condensed water pump 82 (see FIG. 1) and the condensed water pump 82A (see FIG. 2) described above, and the pumping unit 80 (see FIG. 1) This is different from the pressure feeding unit 80A (see FIG. 2).
 そして、本実施形態の凝縮水貯留タンク270は、以上で説明した凝縮水貯留タンク70A(図2参照)と同様に、凝縮水を貯留する空間部が密閉状態とされている。 And the condensed water storage tank 270 of this embodiment has the space part which stores condensed water sealed like the condensed water storage tank 70A (refer FIG. 2) demonstrated above.
 したがって、本実施形態の圧送部280の凝縮水経路81は、凝縮水貯留タンク270と熱交換器90とを凝縮水が流動可能に接続すると共に、凝縮水を貯留する空間部が密閉状態とされた凝縮水貯留タンク270を介して循環経路20と連通する。つまり、凝縮水経路81は、凝縮水を貯留する空間部が密閉状態とされた凝縮水貯留タンク270を介して、凝縮器60にて循環経路20の循環通路21と連通する構成となっている。 Therefore, the condensed water path 81 of the pumping unit 280 of this embodiment connects the condensed water storage tank 270 and the heat exchanger 90 so that the condensed water can flow, and the space for storing the condensed water is sealed. The condensed water storage tank 270 communicates with the circulation path 20. That is, the condensed water path 81 is configured to communicate with the circulation path 21 of the circulation path 20 through the condenser 60 via the condensed water storage tank 270 in which the space for storing condensed water is sealed. .
 そして、圧送部280は、凝縮水貯留タンク270を密閉状態とした上で、循環経路20の循環通路21の圧力、すなわち、循環通路21内のガスの圧力を利用して、凝縮水経路81の凝縮水を加圧し凝縮水貯留タンク270側から熱交換器90側に圧送する。圧送部280は、循環経路20の循環通路21の圧力が大気圧よりも高くなることで、凝縮水経路81の凝縮水を加圧し凝縮水貯留タンク270側から熱交換器90側に圧送することができる。つまり、圧送部280は、大気圧よりも高い循環経路20の循環通路21の圧力により凝縮水排出通路64内の凝縮水を密閉状態とされた凝縮水貯留タンク270側に向けて押し込むようにして圧送することで、凝縮水貯留タンク270内部の圧力を大気圧よりも高い圧力に加圧し、凝縮水貯留タンク270に貯留される凝縮水を、大気開放通路83を介して熱交換器90側に向けて圧送することができる。 The pressure feeding unit 280 uses the pressure of the circulation passage 21 of the circulation path 20, that is, the pressure of the gas in the circulation path 21, after the condensed water storage tank 270 is sealed, The condensed water is pressurized and fed from the condensed water storage tank 270 side to the heat exchanger 90 side. The pressure feeding unit 280 pressurizes the condensed water in the condensed water path 81 and pumps it from the condensed water storage tank 270 side to the heat exchanger 90 side when the pressure in the circulation path 21 of the circulation path 20 becomes higher than the atmospheric pressure. Can do. In other words, the pressure feeding unit 280 pushes the condensed water in the condensed water discharge passage 64 toward the condensed water storage tank 270 that is in a sealed state by the pressure of the circulation passage 21 of the circulation path 20 higher than the atmospheric pressure. By pressure-feeding, the pressure inside the condensed water storage tank 270 is increased to a pressure higher than the atmospheric pressure, and the condensed water stored in the condensed water storage tank 270 is transferred to the heat exchanger 90 side via the atmosphere opening passage 83. Can be pumped toward.
 ここで、循環経路20の循環通路21内の圧力は、循環経路20全体を大気圧より高くする必要はなく、例えば、凝縮器60から凝縮水を排出する部分の近傍、すなわち、凝縮水排出口60cの近傍を大気圧より高くすればよい。 Here, the pressure in the circulation path 21 of the circulation path 20 does not need to be higher than the atmospheric pressure in the entire circulation path 20, for example, in the vicinity of a portion where condensed water is discharged from the condenser 60, that is, a condensed water discharge port. What is necessary is just to make the vicinity of 60c higher than atmospheric pressure.
 以上で説明した本発明の実施形態に係る作動ガス循環型エンジン201によれば、作動ガス循環型エンジン201は、凝縮水貯留タンク270に貯留される凝縮水を圧送部280により大気圧よりも高い圧力で熱交換器90に圧送し、熱交換器90によりこの圧送された凝縮水を排気ガスの排気熱を利用して蒸発させることから、凝縮水貯留タンク270に貯留されている凝縮水を水蒸気として大気に放出することができ、この結果、例えば、作動ガス循環型エンジン201の車両への搭載性を向上し、凝縮器60によって分離された凝縮水を適正に処理することができる。 According to the working gas circulation engine 201 according to the embodiment of the present invention described above, the working gas circulation engine 201 causes the condensed water stored in the condensed water storage tank 270 to be higher than the atmospheric pressure by the pumping unit 280. The condensate stored in the condensate storage tank 270 is steamed because the condensed water pumped by the heat exchanger 90 is evaporated using the exhaust heat of the exhaust gas. As a result, for example, the mounting property of the working gas circulation engine 201 on the vehicle can be improved, and the condensed water separated by the condenser 60 can be appropriately treated.
 さらに、以上で説明した本発明の実施形態に係る作動ガス循環型エンジン201によれば、圧送部280は、凝縮水貯留タンク270と熱交換器90とを凝縮水が流動可能に接続すると共に、凝縮水を貯留する空間部が密閉状態とされた凝縮水貯留タンク270を介して循環経路20と連通する凝縮水経路81を有し、大気圧よりも高い循環経路20のガスの圧力により凝縮水経路81の凝縮水を加圧し凝縮水貯留タンク270側から熱交換器90側に圧送する。したがって、作動ガス循環型エンジン201は、凝縮水貯留タンク270に貯留される凝縮水を大気圧よりも高い循環経路20のガスの圧力により凝縮水経路81を介して熱交換器90に圧送し熱交換器90で発生した水蒸気を大気に放出することから、凝縮水経路81を流れる凝縮水(熱交換器90で蒸発した後は水蒸気)が逆流することを確実に防止することができる。この結果、作動ガス循環型エンジン1は、凝縮水貯留タンク270に貯留される凝縮水を圧送部280により熱交換器90に圧送しこの凝縮水を蒸発させ、確実に大気に放出することができる。そして、作動ガス循環型エンジン201は、圧送部280が凝縮水貯留タンク270を密閉状態とした上で、循環経路20内のガスの圧力を利用して、凝縮水経路81の凝縮水を加圧し凝縮水貯留タンク270側から熱交換器90側に圧送することから、例えば、上述したような凝縮水ポンプ82(図1参照)や凝縮水ポンプ82A(図2参照)を備える必要がないので、作動ガス循環型エンジン201を小型化することができ、作動ガス循環型エンジン201の車両への搭載性をさらに向上することができる。 Furthermore, according to the working gas circulation engine 201 according to the embodiment of the present invention described above, the pressure feeding unit 280 connects the condensed water storage tank 270 and the heat exchanger 90 so that the condensed water can flow, A condensed water path 81 communicates with the circulation path 20 via a condensed water storage tank 270 in which the space for storing the condensed water is hermetically sealed, and the condensed water is caused by the gas pressure in the circulation path 20 higher than the atmospheric pressure. The condensed water in the path 81 is pressurized and fed from the condensed water storage tank 270 side to the heat exchanger 90 side. Therefore, the working gas circulation engine 201 pumps the condensed water stored in the condensed water storage tank 270 to the heat exchanger 90 via the condensed water path 81 by the pressure of the gas in the circulation path 20 higher than the atmospheric pressure. Since the water vapor generated in the exchanger 90 is released to the atmosphere, it is possible to reliably prevent the condensed water flowing through the condensed water path 81 (water vapor after being evaporated in the heat exchanger 90) from flowing backward. As a result, the working gas circulation engine 1 can pump the condensed water stored in the condensed water storage tank 270 to the heat exchanger 90 by the pumping unit 280, evaporate the condensed water, and reliably release it to the atmosphere. . The working gas circulation engine 201 pressurizes the condensed water in the condensed water path 81 using the pressure of the gas in the circulation path 20 after the pressure feeding unit 280 has sealed the condensed water storage tank 270 in a sealed state. Since it is pumped from the condensed water storage tank 270 side to the heat exchanger 90 side, for example, there is no need to provide the condensed water pump 82 (see FIG. 1) and the condensed water pump 82A (see FIG. 2) as described above. The working gas circulation engine 201 can be reduced in size, and the mounting property of the working gas circulation engine 201 on the vehicle can be further improved.
 なお、以上で説明した作動ガス循環型エンジン201の圧送部280は、さらに作動ガス貯留手段、調節手段を備えていてもよい。 In addition, the pumping unit 280 of the working gas circulation engine 201 described above may further include working gas storage means and adjustment means.
 図4は、本発明の変形例2に係る作動ガス循環型エンジンの模式的な概略構成図である。 FIG. 4 is a schematic configuration diagram of a working gas circulation engine according to the second modification of the present invention.
 本変形例に係る作動ガス循環型エンジン201Aは、図4に示すように、圧送手段としての圧送部280Aを備える。凝縮水貯留タンク270は、上述したように凝縮水を貯留する空間部が密閉状態とされている。そして、本変形例の圧送部280Aは、上述した圧送部280とほぼ同様の構成であるが、さらに、作動ガス貯留手段としての高圧タンク284Aと、調節手段としての圧力調節弁285Aとを含んで構成される点で、上述した圧送部280とは異なる。 As shown in FIG. 4, the working gas circulation engine 201A according to this modification includes a pressure feeding unit 280A as pressure feeding means. As described above, the condensed water storage tank 270 has a sealed space for storing condensed water. The pumping unit 280A of the present modification has substantially the same configuration as the above-described pumping unit 280, but further includes a high-pressure tank 284A as a working gas storage unit and a pressure regulating valve 285A as a regulating unit. It differs from the above-mentioned pumping part 280 by the point comprised.
 高圧タンク284Aは、循環経路20から分岐して設けられ、例えば、循環経路20内のガスの圧力と比べて相対的に高圧の作動ガスを貯留するものである。高圧タンク284Aは、循環経路20の循環通路21、ここでは、第3循環通路21cから分岐する分岐通路286A上に設けられる。高圧タンク284Aは、その内部が分岐通路286Aを介して第3循環通路21cの内部と連通する。 The high-pressure tank 284A is provided to be branched from the circulation path 20, and stores, for example, a working gas having a relatively high pressure compared to the gas pressure in the circulation path 20. The high-pressure tank 284A is provided on the circulation passage 21 of the circulation passage 20, here, the branch passage 286A branched from the third circulation passage 21c. The inside of the high-pressure tank 284A communicates with the inside of the third circulation passage 21c via the branch passage 286A.
 圧力調節弁285Aは、高圧タンク284Aと循環経路20の循環通路21、ここでは、第3循環通路21cとの間の作動ガスの流出入を調節するものである。圧力調節弁285Aは、分岐通路286Aに設けられ、弁体の開閉動作が実行され分岐通路286Aの開度が調節され分岐通路286Aの通路面積が調節されることで、高圧タンク284Aと第3循環通路21cとの間の作動ガスの流出入を調節することができる。 The pressure regulating valve 285A regulates the inflow / outflow of the working gas between the high pressure tank 284A and the circulation passage 21 of the circulation path 20, in this case, the third circulation path 21c. The pressure regulating valve 285A is provided in the branch passage 286A, and the opening and closing operation of the valve body is executed, the opening degree of the branch passage 286A is adjusted, and the passage area of the branch passage 286A is adjusted, so that the high pressure tank 284A and the third circulation are provided. The inflow and outflow of the working gas to and from the passage 21c can be adjusted.
 この結果、作動ガス循環型エンジン201Aは、電子制御装置50により圧力調節弁285Aの開度が調節され高圧タンク284Aと第3循環通路21cとの間の作動ガスの流出入が調節されることで、循環経路20の循環通路21内のガスの圧力を大気圧よりも高くすることができ、これにより、圧送部280Aは、循環経路20の循環通路21内のガスの圧力を利用して、凝縮水経路81の凝縮水を加圧し凝縮水貯留タンク270側から熱交換器90側に圧送することができる。また、圧送部280Aは、電子制御装置50により圧力調節弁285Aの開度が調節され高圧タンク284Aと第3循環通路21cとの間の作動ガスの流出入が調節され循環経路20の循環通路21内のガスの圧力が制御されることで、凝縮水の圧送量を調節することができる。 As a result, in the working gas circulation engine 201A, the opening degree of the pressure regulating valve 285A is adjusted by the electronic control unit 50, and the flow of working gas between the high pressure tank 284A and the third circulation passage 21c is adjusted. The pressure of the gas in the circulation passage 21 of the circulation path 20 can be made higher than the atmospheric pressure, so that the pressure feeding unit 280A condenses using the pressure of the gas in the circulation path 21 of the circulation path 20. The condensed water in the water path 81 can be pressurized and fed from the condensed water storage tank 270 side to the heat exchanger 90 side. Further, in the pressure feeding unit 280A, the opening degree of the pressure regulating valve 285A is adjusted by the electronic control unit 50, and the inflow / outflow of the working gas between the high pressure tank 284A and the third circulation passage 21c is regulated, so By controlling the pressure of the gas inside, the pumping amount of the condensed water can be adjusted.
 以上で説明した本発明の変形例に係る作動ガス循環型エンジン201Aによれば、圧送部280Aは、循環経路20から分岐して設けられ相対的に高圧の作動ガスを貯留する高圧タンク284Aと、高圧タンク284Aと循環経路20との間の作動ガスの流出入を調節する圧力調節弁285Aとを有するように構成してもよい。この場合、電子制御装置50により圧力調節弁285Aの開度が調節されることで、循環経路20の内のガスの圧力を大気圧よりも高くすることができ、これにより、圧送部280Aは、循環経路20内のガスの圧力を利用して、凝縮水経路81の凝縮水を加圧し凝縮水貯留タンク270側から熱交換器90側に圧送することができる。そして、この場合、圧送部280Aは、例えば、燃焼室CC内での酸素と水素の燃焼状態、言い換えれば、酸素、水素の供給量を制御しなくても、圧力調節弁285Aの開度を調節し高圧タンク284Aと第3循環通路21cとの間の作動ガスの流出入を調節することで、循環経路20の内のガスの圧力を調節することができ、例えば、凝縮水ポンプ82(図1参照)や凝縮水ポンプ82A(図2参照)を備えない構成であっても、燃焼室CC内での酸素と水素の燃焼状態を変動させることなく凝縮水の圧送量を調節することができる。 According to the working gas circulation engine 201A according to the modification of the present invention described above, the pressure feeding unit 280A is branched from the circulation path 20 and stores a relatively high pressure working gas 284A. You may comprise so that it may have the pressure control valve 285A which adjusts the inflow / outflow of the working gas between the high pressure tank 284A and the circulation path 20. In this case, the pressure of the gas in the circulation path 20 can be made higher than the atmospheric pressure by adjusting the opening degree of the pressure control valve 285A by the electronic control unit 50, whereby the pressure feeding unit 280A By using the pressure of the gas in the circulation path 20, the condensed water in the condensed water path 81 can be pressurized and fed from the condensed water storage tank 270 side to the heat exchanger 90 side. In this case, for example, the pressure feeding unit 280A regulates the opening degree of the pressure regulating valve 285A without controlling the combustion state of oxygen and hydrogen in the combustion chamber CC, in other words, without controlling the supply amount of oxygen and hydrogen. The pressure of the gas in the circulation path 20 can be adjusted by adjusting the flow of the working gas between the high-pressure tank 284A and the third circulation passage 21c, for example, the condensed water pump 82 (FIG. 1). And the condensate pump 82A (see FIG. 2) can be adjusted without changing the combustion state of oxygen and hydrogen in the combustion chamber CC.
(実施形態3)
 図5は、本発明の実施形態3に係る作動ガス循環型エンジンの模式的な概略構成図、図6は、本発明の実施形態3に係る作動ガス循環型エンジンの圧送量制御を説明するフローチャートである。実施形態3に係る作動ガス循環型エンジンは、実施形態1に係る作動ガス循環型エンジンと略同様の構成であるが圧送量制御手段を備える点で実施形態1に係る作動ガス循環型エンジンとは異なる。その他、上述した実施形態と共通する構成、作用、効果については、重複した説明はできるだけ省略するとともに、同一の符号を付す。
(Embodiment 3)
FIG. 5 is a schematic schematic configuration diagram of a working gas circulation engine according to the third embodiment of the present invention, and FIG. 6 is a flowchart for explaining pressure feed amount control of the working gas circulation engine according to the third embodiment of the present invention. It is. The working gas circulation engine according to the third embodiment has substantially the same configuration as the working gas circulation engine according to the first embodiment, but is different from the working gas circulation engine according to the first embodiment in that it includes a pressure feed amount control unit. Different. In addition, about the structure, effect | action, and effect which are common in embodiment mentioned above, while overlapping description is abbreviate | omitted as much as possible, the same code | symbol is attached | subjected.
 本実施形態に係る作動ガス循環型エンジン301は、図5に示すように、機能概念的に、電子制御装置(ECU)50に圧送量制御手段としての圧送量制御部351が設けられている。 As shown in FIG. 5, the working gas circulation engine 301 according to the present embodiment is functionally conceptually provided with a pumping amount control unit 351 as a pumping amount control unit in an electronic control unit (ECU) 50.
 ここで、電子制御装置50は、マイクロコンピュータを中心として構成され処理部50a、記憶部50b及び入出力部50cを有し、これらは互いに接続され、互いに信号の受け渡しが可能になっている。入出力部50cには作動ガス循環型エンジン301を含む車両の各部を駆動する不図示の駆動回路、上述した各種センサが接続されており、この入出力部50cは、これらのセンサ等との間で信号の入出力を行なう。また、記憶部50bには、作動ガス循環型エンジン301の各部を制御するコンピュータプログラムが格納されている。この記憶部50bは、ハードディスク装置や光磁気ディスク装置、またはフラッシュメモリ等の不揮発性のメモリ(CD-ROM等のような読み出しのみが可能な記憶媒体)や、RAM(Random Access Memory)のような揮発性のメモリ、あるいはこれらの組み合わせにより構成することができる。処理部50aは、不図示のメモリ及びCPU(Central Processing Unit)により構成されており、少なくとも上述の圧送量制御部351を有している。電子制御装置50による各種制御は、各部に設けられたセンサによる検出結果に基づいて、処理部50aが前記コンピュータプログラムを当該処理部50aに組み込まれたメモリに読み込んで演算し、演算の結果に応じて制御信号を送ることにより実行される。その際に処理部50aは、適宜記憶部50bへ演算途中の数値を格納し、また格納した数値を取り出して演算を実行する。なお、この作動ガス循環型エンジン301の各部を制御する場合には、前記コンピュータプログラムの代わりに、電子制御装置50とは異なる専用のハードウェアによって制御してもよい。 Here, the electronic control unit 50 is mainly configured of a microcomputer, and includes a processing unit 50a, a storage unit 50b, and an input / output unit 50c, which are connected to each other and can exchange signals with each other. A drive circuit (not shown) for driving each part of the vehicle including the working gas circulation engine 301 and the various sensors described above are connected to the input / output unit 50c. The input / output unit 50c is connected to these sensors and the like. To input and output signals. The storage unit 50b stores a computer program for controlling each unit of the working gas circulation engine 301. The storage unit 50b is a hard disk device, a magneto-optical disk device, a non-volatile memory such as a flash memory (a storage medium that can only be read such as a CD-ROM), or a RAM (Random Access Memory). A volatile memory or a combination thereof can be used. The processing unit 50a is configured by a memory (not shown) and a CPU (Central Processing Unit), and includes at least the above-described pumping amount control unit 351. Various controls by the electronic control unit 50 are performed by the processing unit 50a reading the computer program into a memory incorporated in the processing unit 50a based on the detection results of the sensors provided in the respective units, and depending on the calculation results. This is executed by sending a control signal. At that time, the processing unit 50a appropriately stores a numerical value in the middle of the calculation in the storage unit 50b, and extracts the stored numerical value to execute the calculation. In addition, when controlling each part of this working gas circulation engine 301, you may control by the dedicated hardware different from the electronic controller 50 instead of the said computer program.
 そして、圧送量制御部351は、凝縮水ポンプ82の駆動を制御することで、圧送部80における凝縮水の圧送量を調節するものである。本実施形態の圧送量制御部351は、凝縮器60によって分離された凝縮水の発生量に基づいて凝縮水ポンプ82の駆動を制御し凝縮水の圧送量を制御する。 And the pumping amount control part 351 adjusts the pumping quantity of the condensed water in the pumping part 80 by controlling the drive of the condensate pump 82. The pumping amount control unit 351 of the present embodiment controls the driving of the condensed water pump 82 based on the amount of condensed water generated separated by the condenser 60 to control the pumping amount of condensed water.
 ここで、本実施形態の作動ガス循環型エンジン301は、流量検出手段としての流量センサ54を備えている。流量センサ54は、凝縮水貯留手段への凝縮水の流量を検出するものである。本実施形態の流量センサ54は、凝縮水経路81をなす凝縮水排出通路64に設けられており、凝縮水排出通路64にて、凝縮器60から凝縮水排出口60c、凝縮水排出通路64を介して凝縮水貯留タンク70に排出される凝縮水の流量を検出する。流量センサ54は、検出信号を電子制御装置50に送信する。圧送量制御部351は、この流量センサ54が検出した凝縮水の流量に基づいて凝縮器60によって分離された凝縮水の発生量を検出、取得する。 Here, the working gas circulation engine 301 of this embodiment includes a flow rate sensor 54 as a flow rate detection means. The flow rate sensor 54 detects the flow rate of the condensed water to the condensed water storage means. The flow rate sensor 54 of the present embodiment is provided in the condensed water discharge passage 64 that forms the condensed water passage 81. In the condensed water discharge passage 64, the condensed water discharge port 60 c and the condensed water discharge passage 64 are connected from the condenser 60. The flow rate of the condensed water discharged to the condensed water storage tank 70 is detected. The flow sensor 54 transmits a detection signal to the electronic control device 50. The pumping amount control unit 351 detects and acquires the generation amount of the condensed water separated by the condenser 60 based on the flow rate of the condensed water detected by the flow sensor 54.
 そして、圧送量制御部351は、取得した凝縮水の発生量に基づいて、凝縮水ポンプ82の駆動を制御し凝縮水の圧送量を制御する。さらに具体的には、圧送量制御部351は、凝縮水ポンプ82による凝縮水の圧送量が取得した凝縮水の発生量とほぼ同等になるように圧送量を制御する。なお、圧送量制御部351は、凝縮水の発生量に対応する値として、流量センサ54が検出した凝縮水の流量をそのまま用いてもよい。すなわち、圧送量制御部351は、流量センサ54が検出した凝縮水の流量に基づいて圧送部80による凝縮水の圧送量を制御することで、結果的に凝縮水の発生量に基づいて圧送部80による凝縮水の圧送量を制御することができる。 And the pumping amount control part 351 controls the drive of the condensed water pump 82 based on the acquired amount of condensed water, and controls the pumping amount of condensed water. More specifically, the pumping amount control unit 351 controls the pumping amount so that the condensate pumping amount by the condensate pump 82 is substantially equal to the acquired condensed water generation amount. The pumping amount control unit 351 may use the flow rate of the condensed water detected by the flow sensor 54 as it is as a value corresponding to the amount of condensed water generated. That is, the pumping amount control unit 351 controls the pumping amount of the condensed water by the pumping unit 80 based on the flow rate of the condensed water detected by the flow sensor 54, and as a result, the pumping unit based on the amount of condensed water generated. The amount of condensed water pumped by 80 can be controlled.
 この結果、作動ガス循環型エンジン301は、凝縮水の発生量に基づいて、圧送量制御部351が凝縮水ポンプ82の駆動を制御し、凝縮水の圧送量が凝縮水の発生量とほぼ同等になるように凝縮水ポンプ82による圧送量を制御することから、凝縮水の発生量に応じた圧送量で、凝縮水貯留タンク70の凝縮水を熱交換器90に向けて圧送し、蒸発させることができるので、凝縮水貯留タンク70に貯留しておく凝縮水の量を少なくすることができる。したがって、作動ガス循環型エンジン301は、凝縮水貯留タンク70に貯留しておく凝縮水の量を少なくすることができることから、凝縮器60によって分離された凝縮水を適正に処理した上で、凝縮水貯留タンク70の容量を小さくすることができ、よって、作動ガス循環型エンジン301の車両への搭載性をさらに向上することができる。 As a result, in the working gas circulation engine 301, the pumping amount controller 351 controls the driving of the condensate pump 82 based on the amount of condensed water generated, and the amount of condensed water pumped is almost equal to the amount of condensed water generated. Therefore, the condensed water in the condensed water storage tank 70 is pumped toward the heat exchanger 90 and evaporated with a pumping amount corresponding to the amount of condensed water generated. Therefore, the amount of condensed water stored in the condensed water storage tank 70 can be reduced. Therefore, since the working gas circulation engine 301 can reduce the amount of condensed water stored in the condensed water storage tank 70, the condensed water is appropriately treated after the condensed water separated by the condenser 60 is processed. The capacity of the water storage tank 70 can be reduced, so that the mounting property of the working gas circulation engine 301 on the vehicle can be further improved.
 次に、図6のフローチャートを参照して本実施形態に係る作動ガス循環型エンジン301の圧送量制御を説明する。なお、この制御ルーチンは、数msないし数十ms毎の制御周期で繰り返し実行される。 Next, the control of the pumping amount of the working gas circulation engine 301 according to this embodiment will be described with reference to the flowchart of FIG. This control routine is repeatedly executed at a control cycle of several ms to several tens of ms.
 まず、電子制御装置50の圧送量制御部351は、流量センサ54が検出した凝縮水の流量に基づいて凝縮器60によって分離された凝縮水の発生量を検出、取得する(S100)。 First, the pumping amount control unit 351 of the electronic control device 50 detects and acquires the generation amount of the condensed water separated by the condenser 60 based on the flow rate of the condensed water detected by the flow sensor 54 (S100).
 次に、圧送量制御部351は、S100にて取得した凝縮水の発生量と、凝縮水ポンプ82による現在の凝縮水の圧送量とを比較し、凝縮水の発生量が現在の凝縮水の圧送量より多いか否かを判定する(S101)。 Next, the pumping amount control unit 351 compares the amount of condensed water generated acquired in S100 with the current amount of condensed water pumped by the condensed water pump 82, and the amount of condensed water generated is the current amount of condensed water. It is determined whether the amount is greater than the pumping amount (S101).
 圧送量制御部351は、凝縮水の発生量が現在の凝縮水の圧送量より多いと判定した場合(S101:Yes)、凝縮水ポンプ82の駆動を制御し凝縮水の圧送量を予め設定された所定量分だけ増加させて(S102)、現在の制御周期を終了し、次の制御周期に移行する。 When it is determined that the amount of condensed water generated is greater than the current amount of condensed water pumped (S101: Yes), the pumping amount controller 351 controls the driving of the condensed water pump 82 to set the pumping amount of the condensed water in advance. The predetermined amount is increased (S102), the current control cycle is terminated, and the process proceeds to the next control cycle.
 圧送量制御部351は、凝縮水の発生量が現在の凝縮水の圧送量以下であると判定した場合(S101:No)、凝縮水ポンプ82の駆動を制御し凝縮水の圧送量を予め設定された所定量分だけ減少させて(S103)、現在の制御周期を終了し、次の制御周期に移行する。 When it is determined that the amount of condensed water generated is less than or equal to the current amount of condensed water pumped (S101: No), the pumping amount control unit 351 controls the driving of the condensed water pump 82 to preset the pumping amount of condensed water. The predetermined amount is decreased (S103), the current control cycle is terminated, and the process proceeds to the next control cycle.
 以上で説明した本発明の実施形態に係る作動ガス循環型エンジン301によれば、作動ガス循環型エンジン301は、凝縮水貯留タンク70に貯留される凝縮水を圧送部80により大気圧よりも高い圧力で熱交換器90に圧送し、熱交換器90によりこの圧送された凝縮水を排気ガスの排気熱を利用して蒸発させることから、凝縮水貯留タンク70に貯留されている凝縮水を水蒸気として大気に放出することができ、この結果、例えば、作動ガス循環型エンジン301の車両への搭載性を向上し、凝縮器60によって分離された凝縮水を適正に処理することができる。 According to the working gas circulation engine 301 according to the embodiment of the present invention described above, the working gas circulation engine 301 causes the condensed water stored in the condensed water storage tank 70 to be higher than the atmospheric pressure by the pumping unit 80. The condensate stored in the condensate storage tank 70 is steamed because the condensed water pumped by the heat exchanger 90 is evaporated using the exhaust heat of the exhaust gas. As a result, for example, the mounting property of the working gas circulation engine 301 on the vehicle can be improved, and the condensed water separated by the condenser 60 can be appropriately treated.
 さらに、以上で説明した本発明の実施形態に係る作動ガス循環型エンジン301によれば、凝縮水の発生量に基づいて圧送部80による凝縮水の圧送量を制御する圧送量制御部351を備える。したがって、作動ガス循環型エンジン301は、凝縮水の発生量に基づいて圧送量制御部351が圧送部80の凝縮水ポンプ82の駆動を制御し圧送部80の凝縮水ポンプ82による凝縮水の圧送量を制御することから、凝縮水の発生量に応じた圧送量で、凝縮水貯留タンク70の凝縮水を熱交換器90に向けて圧送し、蒸発させることができるので、凝縮水貯留タンク70に貯留しておく凝縮水の量を少なくすることができる。この結果、作動ガス循環型エンジン301は、凝縮器60によって分離された凝縮水を適正に処理した上で、凝縮水貯留タンク70の容量を小さくすることができ、よって、作動ガス循環型エンジン301の車両への搭載性をさらに向上することができる。また、作動ガス循環型エンジン301は、凝縮水の発生量に基づいて圧送部80による圧送量を制御することから、熱交換器90において排気ガスから凝縮水に吸収させる熱量も凝縮水の発生量に基づいて制御することもできるので、凝縮器60での凝縮水の発生量自体を適正化することもできる。 Furthermore, the working gas circulation engine 301 according to the embodiment of the present invention described above includes the pumping amount control unit 351 that controls the pumping amount of the condensed water by the pumping unit 80 based on the generation amount of the condensed water. . Therefore, in the working gas circulation engine 301, the pumping amount control unit 351 controls the driving of the condensate pump 82 of the pumping unit 80 based on the amount of condensed water generated, and the condensate pumping of the condensed water by the condensate pump 82 of the pumping unit 80 is performed. Since the amount is controlled, the condensed water in the condensed water storage tank 70 can be pressure-fed and evaporated toward the heat exchanger 90 with a pumping amount corresponding to the amount of condensed water generated. The amount of condensate stored in can be reduced. As a result, the working gas circulation engine 301 can appropriately reduce the capacity of the condensed water storage tank 70 after properly treating the condensed water separated by the condenser 60. Can be further improved. Further, since the working gas circulation engine 301 controls the pumping amount by the pumping unit 80 based on the amount of condensed water generated, the amount of heat absorbed by the condensed water from the exhaust gas in the heat exchanger 90 is also the amount of condensed water generated. Therefore, the amount of condensed water generated in the condenser 60 itself can be optimized.
 さらに、以上で説明した本発明の実施形態に係る作動ガス循環型エンジン301によれば、圧送量制御部351は、圧送部80による圧送量が凝縮水の発生量と同等になるように圧送部80による圧送量を制御する。したがって、作動ガス循環型エンジン301は、圧送量制御部351が凝縮水の圧送量が凝縮水の発生量とほぼ同等になるように圧送部80による圧送量を制御することから、凝縮水貯留タンク70に貯留しておく凝縮水の量を最小限にとどめることができる。 Furthermore, according to the working gas circulation engine 301 according to the embodiment of the present invention described above, the pumping amount control unit 351 includes the pumping unit such that the pumping amount by the pumping unit 80 is equal to the amount of condensed water generated. The pumping amount by 80 is controlled. Therefore, the working gas circulation engine 301 controls the pumping amount by the pumping unit 80 so that the pumping amount control unit 351 controls the pumping amount of the condensed water to be substantially equal to the amount of condensed water generated. The amount of condensed water stored in 70 can be minimized.
 さらに、以上で説明した本発明の実施形態に係る作動ガス循環型エンジン301によれば、凝縮水貯留タンク70への凝縮水の流量を検出する流量センサ54を備え、圧送量制御部351は、流量センサ54が検出した凝縮水の流量に基づいて圧送部80による圧送量を制御する。したがって、作動ガス循環型エンジン301は、流量センサ54が検出する凝縮水貯留タンク70への凝縮水の実際の流量に基づいて、凝縮水の発生量あるいは凝縮水の発生量に対応する値を検出、取得することから、正確な凝縮水の発生量を取得することができ、この正確な凝縮水の発生量あるいは凝縮水の発生量に対応する値に基づいて圧送部80による圧送量を正確に制御することができる。 Furthermore, according to the working gas circulation engine 301 according to the embodiment of the present invention described above, the flow rate sensor 54 that detects the flow rate of the condensed water to the condensed water storage tank 70 is provided, and the pumping amount control unit 351 includes: The pumping amount by the pumping unit 80 is controlled based on the flow rate of the condensed water detected by the flow sensor 54. Therefore, the working gas circulation engine 301 detects the amount of condensed water or a value corresponding to the amount of condensed water based on the actual flow rate of condensed water to the condensed water storage tank 70 detected by the flow sensor 54. Therefore, the accurate amount of condensed water generated can be acquired, and the amount of pumping by the pumping unit 80 can be accurately determined based on this exact amount of condensed water generated or a value corresponding to the amount of condensed water generated. Can be controlled.
 なお、以上の説明では、圧送量制御部351は、圧送部80の凝縮水ポンプ82の駆動を制御することで、圧送部80における凝縮水の圧送量を調節するものとして説明したが、この圧送量制御部351は、実施形態2の作動ガス循環型エンジン201(図3参照)が備える圧送部280(図3参照)における凝縮水の圧送量を調節する場合には、燃焼室CC内での酸素と水素の燃焼状態、言い換えれば、酸素、水素の供給量を制御し、循環経路20の循環通路21内のガスの圧力を制御することで、圧送部280による凝縮水の圧送量を制御することができる。また、圧送量制御部351は、変形例2の作動ガス循環型エンジン201A(図4参照)が備える圧送部280A(図4参照)における凝縮水の圧送量を調節する場合には、圧力調節弁285A(図4参照)の開度を制御し高圧タンク284Aと第3循環通路21cとの間の作動ガスの流出入を制御し循環経路20の循環通路21内のガスの圧力を制御することで、圧送部280Aによる凝縮水の圧送量を制御することができる。 In the above description, the pumping amount control unit 351 has been described as adjusting the pumping amount of the condensed water in the pumping unit 80 by controlling the driving of the condensed water pump 82 of the pumping unit 80. When adjusting the amount of condensed water pumped in the pumping unit 280 (see FIG. 3) included in the working gas circulation engine 201 (see FIG. 3) of the second embodiment, the amount control unit 351 The oxygen and hydrogen combustion state, in other words, the supply amount of oxygen and hydrogen is controlled, and the pressure of the gas in the circulation passage 21 of the circulation path 20 is controlled, thereby controlling the pumping amount of the condensed water by the pumping unit 280. be able to. In addition, the pressure feed amount control unit 351 is configured to adjust the pressure feed amount of the condensed water in the pressure feed unit 280A (see FIG. 4) included in the working gas circulation engine 201A (see FIG. 4) of the second modification. By controlling the opening of 285A (see FIG. 4), controlling the flow of working gas between the high-pressure tank 284A and the third circulation passage 21c, and controlling the pressure of the gas in the circulation passage 21 of the circulation passage 20. The amount of condensed water pumped by the pumping unit 280A can be controlled.
(実施形態4)
 図7は、本発明の実施形態4に係る作動ガス循環型エンジンの模式的な概略構成図、図8は、本発明の実施形態4に係る作動ガス循環型エンジンの圧送量マップを示す図、図9は、本発明の実施形態4に係る作動ガス循環型エンジンの圧送量制御を説明するフローチャートである。実施形態4に係る作動ガス循環型エンジンは、実施形態3に係る作動ガス循環型エンジンと略同様の構成であるが流量検出手段にかえて水位検出手段を備える点で実施形態3に係る作動ガス循環型エンジンとは異なる。その他、上述した実施形態と共通する構成、作用、効果については、重複した説明はできるだけ省略するとともに、同一の符号を付す。
(Embodiment 4)
FIG. 7 is a schematic schematic configuration diagram of a working gas circulation engine according to Embodiment 4 of the present invention, and FIG. 8 is a diagram illustrating a pressure feed amount map of the working gas circulation engine according to Embodiment 4 of the present invention. FIG. 9 is a flowchart for explaining the control of the pumping amount of the working gas circulation engine according to the fourth embodiment of the present invention. The working gas circulation engine according to the fourth embodiment has substantially the same configuration as the working gas circulation engine according to the third embodiment, but the working gas according to the third embodiment is provided with a water level detection means instead of the flow rate detection means. It is different from the circulation type engine. In addition, about the structure, effect | action, and effect which are common in embodiment mentioned above, while overlapping description is abbreviate | omitted as much as possible, the same code | symbol is attached | subjected.
 本実施形態に係る作動ガス循環型エンジン401は、図7に示すように、機能概念的に、電子制御装置(ECU)50に圧送量制御手段としての圧送量制御部451が設けられている。 As shown in FIG. 7, the working gas circulation engine 401 according to the present embodiment is functionally conceptually provided with a pumping amount control unit 451 as a pumping amount control unit in an electronic control unit (ECU) 50.
 そして、圧送量制御部451は、凝縮水ポンプ82の駆動を制御することで、圧送部80における凝縮水の圧送量を調節するものである。本実施形態の圧送量制御部451は、凝縮器60によって分離された凝縮水の発生量に基づいて凝縮水ポンプ82の駆動を制御し凝縮水の圧送量を制御する。 And the pumping amount control part 451 controls the pumping amount of the condensed water in the pumping part 80 by controlling the drive of the condensed water pump 82. The pumping amount control unit 451 of this embodiment controls the driving of the condensed water pump 82 based on the amount of condensed water generated separated by the condenser 60 and controls the pumping amount of condensed water.
 ここで、本実施形態の作動ガス循環型エンジン401は、水位検出手段としての水位センサ55を備えている。水位センサ55は、凝縮水貯留タンク70に貯留されている凝縮水の水位を検出するものである。水位センサ55は、凝縮水貯留タンク70の内部に設けられており、凝縮水貯留タンク70の底部から凝縮水の水面までの高さ、すなわち、凝縮水貯留タンク70の水位を検出する。水位センサ55は、検出信号を電子制御装置50に送信する。圧送量制御部451は、この水位センサ55が検出した凝縮水貯留タンク70の水位に基づいて凝縮器60によって分離された凝縮水の発生量を検出、取得する。すなわち、圧送量制御部451は、現在の制御周期において水位センサ55が検出した凝縮水貯留タンク70の水位と、前回の制御周期において水位センサ55が検出した凝縮水貯留タンク70の水位とを比較し、これらの差分を演算することで、凝縮器60によって分離された凝縮水の発生量を算出し取得する。 Here, the working gas circulation engine 401 of this embodiment includes a water level sensor 55 as water level detection means. The water level sensor 55 detects the water level of the condensed water stored in the condensed water storage tank 70. The water level sensor 55 is provided inside the condensed water storage tank 70 and detects the height from the bottom of the condensed water storage tank 70 to the water level of the condensed water, that is, the water level of the condensed water storage tank 70. The water level sensor 55 transmits a detection signal to the electronic control unit 50. The pumping amount control unit 451 detects and acquires the generation amount of condensed water separated by the condenser 60 based on the water level of the condensed water storage tank 70 detected by the water level sensor 55. That is, the pumping amount control unit 451 compares the water level of the condensed water storage tank 70 detected by the water level sensor 55 in the current control cycle with the water level of the condensed water storage tank 70 detected by the water level sensor 55 in the previous control cycle. Then, by calculating these differences, the amount of condensed water separated by the condenser 60 is calculated and acquired.
 そして、圧送量制御部451は、取得した凝縮水の発生量に基づいて、凝縮水ポンプ82の駆動を制御し凝縮水の圧送量を制御する。圧送量制御部451は、上述した実施形態3の圧送量制御部351(図5参照)と同様に、圧送部80の凝縮水ポンプ82による凝縮水の圧送量が取得された凝縮水の発生量とほぼ同等になるように圧送量を制御するようにしてもよいが、ここでは、圧送量制御部451が取得した凝縮水の発生量と、現在の制御周期において水位センサ55が検出した凝縮水貯留タンク70の凝縮水の水位とに基づいて、圧送部80の凝縮水ポンプ82の駆動を制御し凝縮水の圧送量を制御するように構成するとよい。 And the pumping amount control part 451 controls the drive of the condensed water pump 82 based on the acquired amount of condensed water, and controls the pumping amount of condensed water. The pumping amount control unit 451 is the same as the pumping amount control unit 351 (see FIG. 5) of the third embodiment described above, and the amount of condensed water generated by acquiring the condensate pumping amount by the condensed water pump 82 of the pumping unit 80. However, here, the amount of condensed water generated by the pumping amount control unit 451 and the condensed water detected by the water level sensor 55 in the current control cycle are controlled. Based on the level of the condensed water in the storage tank 70, the drive of the condensed water pump 82 of the pressure feeding unit 80 may be controlled to control the amount of condensed water pumped.
 本実施形態の圧送量制御部451は、例えば、図8に示す圧送量マップm01に基づいて、圧送部80による凝縮水の圧送量を求める。この圧送量マップm01は、横軸が凝縮水貯留タンク70の水位、縦軸が凝縮水の発生量を示す。圧送量マップm01は、凝縮水貯留タンク70の水位、凝縮水の発生量と圧送部80による凝縮水の圧送量との関係を記述したものである。この圧送量マップm01では、圧送部80による凝縮水の圧送量は、凝縮水貯留タンク70の水位の増加にともなって増加し、凝縮水の発生量の増加にともなって増加する。圧送量マップm01は、記憶部50bに格納されている。圧送量制御部451は、この圧送量マップm01に基づいて、取得した凝縮水の発生量と、水位センサ55が検出した凝縮水貯留タンク70の凝縮水の水位とから圧送部80による凝縮水の圧送量を求める。 The pumping amount control unit 451 of the present embodiment obtains the pumping amount of the condensed water by the pumping unit 80 based on, for example, the pumping amount map m01 illustrated in FIG. In this pumping amount map m01, the horizontal axis indicates the water level of the condensed water storage tank 70, and the vertical axis indicates the amount of condensed water generated. The pumping amount map m01 describes the relationship between the water level of the condensed water storage tank 70, the amount of condensed water generated, and the amount of condensed water pumped by the pumping unit 80. In this pumping amount map m01, the amount of condensed water pumped by the pumping unit 80 increases as the water level of the condensed water storage tank 70 increases, and increases as the amount of condensed water generated increases. The pumping amount map m01 is stored in the storage unit 50b. Based on this pumping amount map m01, the pumping amount control unit 451 determines the condensed water generated by the pumping unit 80 from the acquired amount of condensed water and the level of condensed water in the condensed water storage tank 70 detected by the water level sensor 55. Find the pumping amount.
 なお、本実施形態では、圧送量制御部451は、圧送量マップm01を用いて圧送部80による凝縮水の圧送量を求めたが、本実施形態はこれに限定されない。圧送量制御部451は、例えば、圧送量マップm01に相当する数式に基づいて圧送部80による凝縮水の圧送量を求めてもよい。以下で説明する種々のマップについても同様である。 In addition, in this embodiment, although the pumping amount control part 451 calculated | required the pumping amount of the condensed water by the pumping part 80 using the pumping amount map m01, this embodiment is not limited to this. For example, the pumping amount control unit 451 may determine the pumping amount of the condensed water by the pumping unit 80 based on a mathematical expression corresponding to the pumping amount map m01. The same applies to various maps described below.
 この結果、作動ガス循環型エンジン401は、取得した凝縮水の発生量に基づいて、圧送量制御部451が凝縮水ポンプ82の駆動を制御し、凝縮水ポンプ82による圧送量を制御することから、凝縮水の発生量に応じた圧送量で、凝縮水貯留タンク70の凝縮水を熱交換器90に向けて圧送し、蒸発させることができるので、凝縮水貯留タンク70に貯留しておく凝縮水の量を少なくすることができる。したがって、作動ガス循環型エンジン401は、凝縮水貯留タンク70に貯留しておく凝縮水の量を少なくすることができることから、凝縮器60によって分離された凝縮水を適正に処理した上で、凝縮水貯留タンク70の容量を小さくすることができ、よって、作動ガス循環型エンジン401の車両への搭載性をさらに向上することができる。 As a result, in the working gas circulation engine 401, the pumping amount control unit 451 controls the driving of the condensate pump 82 based on the acquired amount of condensed water, and controls the pumping amount by the condensate pump 82. Since the condensed water in the condensed water storage tank 70 can be pumped toward the heat exchanger 90 and evaporated with a pumping amount corresponding to the amount of condensed water generated, the condensation stored in the condensed water storage tank 70 The amount of water can be reduced. Therefore, since the working gas circulation engine 401 can reduce the amount of condensed water stored in the condensed water storage tank 70, the condensed water is properly treated after the condensed water separated by the condenser 60 is processed. The capacity of the water storage tank 70 can be reduced, so that the mounting property of the working gas circulation engine 401 on the vehicle can be further improved.
 また、作動ガス循環型エンジン401は、水位センサ55が検出した凝縮水貯留タンク70の凝縮水の水位に基づいて圧送量制御部451が凝縮水の発生量を検出、取得することから、凝縮水貯留タンク70の凝縮水の水位を適正な水位に維持しつつ、凝縮水の発生量に応じた圧送量で凝縮水貯留タンク70の凝縮水を圧送することができるので、例えば凝縮水貯留タンク70の凝縮水の枯渇を防止することができ、凝縮水ポンプ82が気体を吸い込んでしまうことを防止することができる。例えば、作動ガス循環型エンジン401は、仮に凝縮水の発生量が一定であるとした場合に水位センサ55が検出した凝縮水貯留タンク70の凝縮水の水位が相対的に上昇してきた際には、これに応じて圧送量制御部451が圧送部80による凝縮水の圧送量を相対的に増加させ、水位センサ55が検出した凝縮水貯留タンク70の凝縮水の水位が相対的に下降してきた際には、これに応じて圧送量制御部451が圧送部80による凝縮水の圧送量を相対的に減少させることで、凝縮水貯留タンク70の凝縮水の水位を確実に適正な水位に維持することができる。 Further, the working gas circulation engine 401 detects the amount of condensed water generated and detected by the pumping amount control unit 451 based on the level of condensed water in the condensed water storage tank 70 detected by the water level sensor 55. The condensed water in the condensed water storage tank 70 can be pumped with a pumping amount corresponding to the amount of condensed water generated while maintaining the water level of the condensed water in the storage tank 70 at an appropriate water level. It is possible to prevent the condensed water from being depleted, and to prevent the condensed water pump 82 from sucking gas. For example, the working gas circulation engine 401 has a relatively high level of condensed water in the condensed water storage tank 70 detected by the water level sensor 55, assuming that the amount of condensed water generated is constant. Accordingly, the pumping amount control unit 451 relatively increases the pumping amount of the condensed water by the pumping unit 80, and the water level of the condensed water in the condensed water storage tank 70 detected by the water level sensor 55 has relatively decreased. In response to this, the pumping amount control unit 451 relatively decreases the pumping amount of the condensed water by the pumping unit 80, thereby reliably maintaining the water level of the condensed water in the condensate water storage tank 70 at an appropriate level. can do.
 なお、圧送量制御部451は、凝縮水の発生量に対応する値として、水位センサ55が検出した凝縮水貯留タンク70の凝縮水の水位をそのまま用いてもよい。すなわち、圧送量制御部451は、水位センサ55が検出した凝縮水貯留タンク70の凝縮水の水位に基づいて圧送部80による凝縮水の圧送量を制御することで、結果的に凝縮水の発生量に基づいて圧送部80による凝縮水の圧送量を制御することができる。 Note that the pumping amount control unit 451 may use the level of the condensed water in the condensed water storage tank 70 detected by the water level sensor 55 as a value corresponding to the amount of condensed water generated. That is, the pumping amount control unit 451 controls the amount of condensed water pumped by the pumping unit 80 based on the level of condensed water in the condensed water storage tank 70 detected by the water level sensor 55, resulting in generation of condensed water. Based on the amount, the pumping amount of the condensed water by the pumping unit 80 can be controlled.
 次に、図9のフローチャートを参照して本実施形態に係る作動ガス循環型エンジン401の圧送量制御を説明する。なお、この制御ルーチンは、数msないし数十ms毎の制御周期で繰り返し実行される。 Next, with reference to the flowchart of FIG. 9, the control of the pumping amount of the working gas circulation engine 401 according to this embodiment will be described. This control routine is repeatedly executed at a control cycle of several ms to several tens of ms.
 まず、電子制御装置50の圧送量制御部451は、水位センサ55が検出した凝縮水貯留タンク70の凝縮水の水位を取得する(S200)。 First, the pumping amount control unit 451 of the electronic control device 50 acquires the water level of the condensed water in the condensed water storage tank 70 detected by the water level sensor 55 (S200).
 次に、圧送量制御部451は、前回の制御周期において水位センサ55が検出した凝縮水貯留タンク70の水位と、今回の制御周期において水位センサ55が検出した凝縮水貯留タンク70の水位とを比較し、これらの差分を演算することで、凝縮器60によって分離された凝縮水の発生量を算出し取得する(S201)。 Next, the pumping amount control unit 451 determines the water level of the condensed water storage tank 70 detected by the water level sensor 55 in the previous control cycle and the water level of the condensed water storage tank 70 detected by the water level sensor 55 in the current control cycle. By comparing and calculating these differences, the amount of condensed water separated by the condenser 60 is calculated and acquired (S201).
 次に、圧送量制御部451は、例えば、圧送量マップm01に基づいて、S200で水位センサ55が検出した現在の凝縮水貯留タンク70の凝縮水の水位とS201で取得した凝縮水の発生量とから圧送部80による凝縮水の圧送量を求める(S202)。 Next, the pumping amount control unit 451, for example, based on the pumping amount map m01, the current condensate water level in the condensate storage tank 70 detected by the water level sensor 55 in S200 and the amount of condensate generation acquired in S201. From this, the pumping amount of the condensed water by the pumping unit 80 is obtained (S202).
 そして、圧送量制御部451は、S202で算出した圧送部80による凝縮水の圧送量に基づいて、圧送部80の凝縮水ポンプ82の駆動を制御し、凝縮水ポンプ82による圧送量を変更し(S203)、現在の制御周期を終了し、次の制御周期に移行する。 Then, the pumping amount control unit 451 controls the driving of the condensed water pump 82 of the pumping unit 80 based on the pumping amount of the condensed water by the pumping unit 80 calculated in S202, and changes the pumping amount by the condensed water pump 82. (S203), the current control cycle is terminated, and the process proceeds to the next control cycle.
 以上で説明した本発明の実施形態に係る作動ガス循環型エンジン401によれば、作動ガス循環型エンジン401は、凝縮水貯留タンク70に貯留される凝縮水を圧送部80により大気圧よりも高い圧力で熱交換器90に圧送し、熱交換器90によりこの圧送された凝縮水を排気ガスの排気熱を利用して蒸発させることから、凝縮水貯留タンク70に貯留されている凝縮水を水蒸気として大気に放出することができ、この結果、例えば、作動ガス循環型エンジン401の車両への搭載性を向上し、凝縮器60によって分離された凝縮水を適正に処理することができる。 According to the working gas circulation engine 401 according to the embodiment of the present invention described above, the working gas circulation engine 401 is configured to cause the condensed water stored in the condensed water storage tank 70 to be higher than the atmospheric pressure by the pumping unit 80. The condensate stored in the condensate storage tank 70 is steamed because the condensed water pumped by the heat exchanger 90 is evaporated using the exhaust heat of the exhaust gas. As a result, for example, the mounting property of the working gas circulation engine 401 on the vehicle can be improved, and the condensed water separated by the condenser 60 can be appropriately treated.
 さらに、以上で説明した本発明の実施形態に係る作動ガス循環型エンジン401によれば、作動ガス循環型エンジン401は、取得した凝縮水の発生量に基づいて、圧送量制御部451が圧送部80の凝縮水ポンプ82の駆動を制御し圧送部80の凝縮水ポンプ82による凝縮水の圧送量を制御することから、凝縮水の発生量に応じた圧送量で、凝縮水貯留タンク70の凝縮水を熱交換器90に向けて圧送し、蒸発させることができるので、凝縮水貯留タンク70に貯留しておく凝縮水の量を少なくすることができる。この結果、作動ガス循環型エンジン401は、凝縮器60によって分離された凝縮水を適正に処理した上で、凝縮水貯留タンク70の容量を小さくすることができ、よって、作動ガス循環型エンジン401の車両への搭載性をさらに向上することができる。 Further, according to the working gas circulation engine 401 according to the embodiment of the present invention described above, the working gas circulation engine 401 is configured so that the pumping amount control unit 451 is based on the acquired amount of condensed water. Since the condensate pump 82 is controlled to control the pumping amount of the condensate water by the condensate pump 82 of the pumping unit 80, the condensate of the condensate storage tank 70 can be condensed with a pumping amount corresponding to the amount of condensed water generated. Since water can be pumped toward the heat exchanger 90 and evaporated, the amount of condensed water stored in the condensed water storage tank 70 can be reduced. As a result, the working gas circulation engine 401 can appropriately reduce the capacity of the condensed water storage tank 70 after properly treating the condensed water separated by the condenser 60. Can be further improved.
 さらに、以上で説明した本発明の実施形態に係る作動ガス循環型エンジン401によれば、凝縮水貯留タンク70に貯留されている凝縮水の水位を検出する水位センサ55を備え、圧送量制御部451は、水位センサ55が検出した凝縮水の水位に基づいて圧送部80の凝縮水ポンプ82による凝縮水の圧送量を制御する。したがって、作動ガス循環型エンジン401は、水位センサ55が検出した凝縮水貯留タンク70の凝縮水の水位に基づいて、凝縮水の発生量あるいは凝縮水の発生量に対応する値を検出、取得することから、凝縮水貯留タンク70の凝縮水の水位を適正な水位に維持しつつ、凝縮水の発生量に応じた圧送量で凝縮水貯留タンク70の凝縮水を圧送することができる。 Furthermore, according to the working gas circulation engine 401 according to the embodiment of the present invention described above, the pressure level control unit includes the water level sensor 55 that detects the water level of the condensed water stored in the condensed water storage tank 70. 451 controls the amount of condensed water pumped by the condensed water pump 82 of the pumping unit 80 based on the water level of the condensed water detected by the water level sensor 55. Therefore, the working gas circulation engine 401 detects and acquires the amount of condensed water or a value corresponding to the amount of condensed water based on the level of condensed water in the condensed water storage tank 70 detected by the water level sensor 55. Therefore, the condensed water in the condensed water storage tank 70 can be pumped with a pumping amount corresponding to the amount of condensed water generated while maintaining the water level of the condensed water in the condensed water storage tank 70 at an appropriate level.
(実施形態5)
 図10は、本発明の実施形態5に係る作動ガス循環型エンジンの模式的な概略構成図、図11は、本発明の実施形態5に係る作動ガス循環型エンジンの圧送量マップを示す図、図12は、本発明の実施形態5に係る作動ガス循環型エンジンの応答遅れ時間マップを示す図、図13は、本発明の実施形態5に係る作動ガス循環型エンジンの圧送量制御を説明するフローチャート、図14は、本発明の変形例3に係る作動ガス循環型エンジンの模式的な概略構成図である。実施形態5に係る作動ガス循環型エンジンは、実施形態3、4に係る作動ガス循環型エンジンと略同様の構成であるが酸化剤又は燃料の供給量に基づいて圧送量を制御する点で実施形態3、4に係る作動ガス循環型エンジンとは異なる。その他、上述した実施形態と共通する構成、作用、効果については、重複した説明はできるだけ省略するとともに、同一の符号を付す。
(Embodiment 5)
FIG. 10 is a schematic schematic configuration diagram of a working gas circulation engine according to Embodiment 5 of the present invention, and FIG. 11 is a diagram illustrating a pressure feed amount map of the working gas circulation engine according to Embodiment 5 of the present invention. FIG. 12 is a view showing a response delay time map of the working gas circulation engine according to the fifth embodiment of the present invention, and FIG. 13 explains the pressure feed amount control of the working gas circulation engine according to the fifth embodiment of the present invention. FIG. 14 is a schematic schematic configuration diagram of a working gas circulation engine according to the third modification of the present invention. The working gas circulation engine according to the fifth embodiment has substantially the same configuration as the working gas circulation engine according to the third and fourth embodiments, but is implemented in that the pumping amount is controlled based on the supply amount of oxidant or fuel. This is different from the working gas circulation engine according to the third and fourth embodiments. In addition, about the structure, effect | action, and effect which are common in embodiment mentioned above, while overlapping description is abbreviate | omitted as much as possible, the same code | symbol is attached | subjected.
 本実施形態に係る作動ガス循環型エンジン501は、図10に示すように、機能概念的に、電子制御装置(ECU)50に圧送量制御手段としての圧送量制御部551が設けられている。 As shown in FIG. 10, the working gas circulation engine 501 according to the present embodiment is functionally conceptually provided with a pumping amount control unit 551 as a pumping amount control unit in an electronic control unit (ECU) 50.
 そして、圧送量制御部551は、凝縮水ポンプ82の駆動を制御することで、圧送部80における凝縮水の圧送量を調節するものである。本実施形態の圧送量制御部551は、凝縮器60によって分離された凝縮水の発生量に基づいて凝縮水ポンプ82の駆動を制御し凝縮水の圧送量を制御する。 The pressure feed amount control unit 551 adjusts the pressure feed amount of the condensed water in the pressure feed unit 80 by controlling the driving of the condensed water pump 82. The pumping amount control unit 551 of the present embodiment controls the driving of the condensed water pump 82 based on the amount of condensed water generated separated by the condenser 60 to control the pumping amount of condensed water.
 ここで、凝縮器60によって分離される凝縮水の発生量は、燃焼室CCにおいて水素と酸素との燃焼により生成される水蒸気の生成量に応じた量となる。さらに燃焼室CCにおいて水素と酸素との燃焼により生成される水蒸気の生成量は、エンジン負荷、言い換えれば、燃焼室CCで燃焼した水素の量、さらに言い換えれば、燃焼室CCに供給される水素又は酸素の供給量に応じた量となる。なお、通常、このような作動ガス循環型エンジン501は、上述したように、例えば、運転者がこの作動ガス循環型エンジン501に要求する駆動力に応じたエンジン負荷を実現することができるような水素の供給量が設定され、これに対して酸素の供給量が設定される。 Here, the amount of condensed water separated by the condenser 60 is an amount corresponding to the amount of water vapor generated by the combustion of hydrogen and oxygen in the combustion chamber CC. Further, the amount of water vapor generated by the combustion of hydrogen and oxygen in the combustion chamber CC is the engine load, in other words, the amount of hydrogen combusted in the combustion chamber CC, in other words, hydrogen supplied to the combustion chamber CC or The amount corresponds to the amount of oxygen supplied. Normally, such a working gas circulation engine 501 can realize an engine load according to the driving force requested by the driver for the working gas circulation engine 501 as described above. A hydrogen supply amount is set, and an oxygen supply amount is set.
 そこで、本実施形態の圧送量制御部551は、エンジン負荷、例えば、燃焼室CCに供給される酸化剤としての酸素又は燃料としての水素の供給量に基づいて圧送部80による凝縮水の圧送量を制御する。ここで、このような作動ガス循環型エンジン501は、例えば、水素の供給量に対して酸素を若干過多に供給し、燃焼室CCに供給された水素を全て燃焼させて運転することがあることから、ここでは圧送量制御部551は、燃焼室CCに供給される水素の供給量に基づいて圧送部80による凝縮水の圧送量を制御する。なお、このような場合であっても、圧送量制御部551は、燃焼室CCに供給される酸素の供給量に基づいて圧送部80による凝縮水の圧送量を制御してもよいし、水素の供給量と酸素の供給量との両方に基づいて圧送部80による凝縮水の圧送量を制御してもよい。 Therefore, the pumping amount control unit 551 of the present embodiment is configured to pump the condensed water by the pumping unit 80 based on the engine load, for example, the supply amount of oxygen as the oxidant or hydrogen as the fuel supplied to the combustion chamber CC. To control. Here, such a working gas circulation engine 501 may be operated, for example, by supplying a little excess of oxygen with respect to the supply amount of hydrogen and burning all the hydrogen supplied to the combustion chamber CC. Therefore, here, the pumping amount control unit 551 controls the pumping amount of the condensed water by the pumping unit 80 based on the supply amount of hydrogen supplied to the combustion chamber CC. Even in such a case, the pumping amount control unit 551 may control the pumping amount of condensed water by the pumping unit 80 based on the supply amount of oxygen supplied to the combustion chamber CC. The pumping amount of the condensed water by the pumping unit 80 may be controlled based on both the supply amount of oxygen and the supply amount of oxygen.
 圧送量制御部551は、実際に燃料噴射手段42から燃焼室CCに噴射された水素の供給量を取得し、この水素の供給量に基づいて凝縮水ポンプ82の駆動を制御し凝縮水の圧送量を制御する。圧送量制御部551は、例えば、燃料噴射手段(燃料噴射弁)42の開弁期間や燃料流量計45が検出する水素の流量に基づいて実際に燃料噴射手段42から燃焼室CCに噴射された水素の供給量を取得すればよい。圧送量制御部551は、凝縮水の発生量に対応する値として、実際に燃料噴射手段42から燃焼室CCに噴射された水素の供給量に基づいて圧送部80による凝縮水の圧送量を制御することで、結果的に凝縮水の発生量に基づいて圧送部80による凝縮水の圧送量を制御することができる。なお、圧送量制御部551は、実際に燃料噴射手段42から燃焼室CCに噴射された水素の供給量に基づいて凝縮水の発生量を推定、取得し、この凝縮水の発生量に基づいて圧送部80による凝縮水の圧送量を制御するようにしてもよい。 The pumping amount control unit 551 acquires the supply amount of hydrogen actually injected from the fuel injection means 42 into the combustion chamber CC, and controls the driving of the condensate pump 82 based on the supply amount of hydrogen to pump condensate water. Control the amount. The pumping amount control unit 551 is actually injected from the fuel injection unit 42 into the combustion chamber CC based on, for example, the opening period of the fuel injection unit (fuel injection valve) 42 or the flow rate of hydrogen detected by the fuel flow meter 45. What is necessary is just to acquire the supply amount of hydrogen. The pumping amount control unit 551 controls the pumping amount of condensed water by the pumping unit 80 based on the supply amount of hydrogen actually injected from the fuel injection means 42 into the combustion chamber CC as a value corresponding to the amount of condensed water generated. As a result, the pumping amount of the condensed water by the pumping unit 80 can be controlled based on the amount of the condensed water generated. The pumping amount control unit 551 estimates and obtains the amount of condensed water generated based on the amount of hydrogen actually injected from the fuel injection means 42 into the combustion chamber CC, and based on the amount of condensed water generated. You may make it control the pumping amount of the condensed water by the pumping part 80. FIG.
 圧送量制御部551は、例えば、図11に示す圧送量マップm02に基づいて、圧送部80による凝縮水の圧送量を求める。この圧送量マップm02は、横軸が水素の供給量、縦軸が凝縮水の圧送量を示す。圧送量マップm02は、実際に燃料噴射手段42から燃焼室CCに噴射された水素の供給量と、圧送部80による凝縮水の圧送量との関係を記述したものである。この圧送量マップm02では、圧送部80による凝縮水の圧送量は、水素の供給量の増加にともなって増加する。圧送量マップm02は、記憶部50bに格納されている。圧送量制御部551は、この圧送量マップm02に基づいて、実際に燃焼室CCに噴射された水素の供給量から圧送部80による凝縮水の圧送量を求める。 The pumping amount control unit 551 obtains the pumping amount of the condensed water by the pumping unit 80 based on, for example, the pumping amount map m02 shown in FIG. In this pumping amount map m02, the horizontal axis indicates the hydrogen supply amount, and the vertical axis indicates the condensate pumping amount. The pumping amount map m02 describes the relationship between the amount of hydrogen actually injected from the fuel injection means 42 into the combustion chamber CC and the pumping amount of condensed water by the pumping unit 80. In this pumping amount map m02, the pumping amount of the condensed water by the pumping unit 80 increases as the hydrogen supply amount increases. The pumping amount map m02 is stored in the storage unit 50b. The pumping amount control unit 551 obtains the pumping amount of condensed water by the pumping unit 80 from the supply amount of hydrogen actually injected into the combustion chamber CC based on the pumping amount map m02.
 なお、実際に燃料噴射手段42から燃焼室CCに噴射された水素の供給量と凝縮水の発生量との関係は、水素の供給量が相対的に増えると凝縮水の発生量も相対的に増え、水素の供給量が相対的に減ると凝縮水の発生量も相対的に減る関係にある。このため、圧送量制御部551は、実際に燃料噴射手段42から燃焼室CCに噴射された水素の供給量に基づいて凝縮水の発生量を推定、取得し、この凝縮水の発生量に基づいて圧送部80による凝縮水の圧送量を制御する場合も、この圧送量マップm02とほぼ同様なマップ(横軸を凝縮水の発生量とした圧送量マップ)を用いればよい。 The relationship between the amount of hydrogen actually injected from the fuel injection means 42 into the combustion chamber CC and the amount of condensed water generated is that the amount of condensed water generated is relatively increased when the amount of hydrogen supplied is relatively increased. As the amount of hydrogen increases and the amount of hydrogen supplied decreases relatively, the amount of condensed water generated also decreases. For this reason, the pumping amount control unit 551 estimates and acquires the amount of condensed water generated based on the amount of hydrogen actually injected from the fuel injection means 42 into the combustion chamber CC, and based on the amount of condensed water generated. Even when the pumping amount of the condensed water by the pumping unit 80 is controlled, a map that is substantially the same as the pumping amount map m02 (a pumping amount map in which the horizontal axis indicates the amount of condensed water generated) may be used.
 ここで、この作動ガス循環型エンジン501では、ある時点で燃焼室CCに供給された水素が燃焼室CCで燃焼し、この燃焼で発生した水蒸気が凝縮器60で分離され凝縮水として凝縮水貯留タンク70に到達するまでにはある程度の時間遅れがある。つまり、作動ガス循環型エンジン501は、燃焼室CCに水素が供給された供給時点と、この供給時点で供給された水素の供給量に応じた凝縮水が実際に凝縮水貯留タンク70に到達する凝縮水到達時点との間には所定の応答遅れ時間が発生する。この供給時点に対する凝縮水の凝縮水到達時点の応答遅れ時間は、循環経路20を流れるガスの流速に応じて変動する。そして、循環経路20を流れるガスの流速は、作動ガス循環型エンジン501のエンジン回転数に応じて変動する。すなわち、循環経路20を流れるガスの流速は、エンジン回転数が増加するにしたがって増加し、エンジン回転数が減少するにしたがって減少する。この結果、供給時点に対する凝縮水の凝縮水到達時点の応答遅れ時間は、エンジン回転数が増加し循環経路20を流れるガスの流速が増加するにしたがって短くなり、エンジン回転数が減少し循環経路20を流れるガスの流速が減少するにしたがって長くなる。 Here, in this working gas circulation engine 501, hydrogen supplied to the combustion chamber CC at a certain time burns in the combustion chamber CC, and water vapor generated by this combustion is separated by the condenser 60 and stored as condensed water. There is a certain time delay before the tank 70 is reached. That is, in the working gas circulation engine 501, the supply time when hydrogen is supplied to the combustion chamber CC, and the condensed water corresponding to the supply amount of hydrogen supplied at this supply time actually reaches the condensed water storage tank 70. A predetermined response delay time occurs between the time when the condensed water is reached. The response delay time at the time when the condensed water reaches the supply time varies depending on the flow velocity of the gas flowing through the circulation path 20. The flow rate of the gas flowing through the circulation path 20 varies according to the engine speed of the working gas circulation engine 501. That is, the flow rate of the gas flowing through the circulation path 20 increases as the engine speed increases, and decreases as the engine speed decreases. As a result, the response delay time of the condensed water arrival time with respect to the supply time becomes shorter as the engine speed increases and the flow velocity of the gas flowing through the circulation path 20 increases, and the engine speed decreases and the circulation path 20 decreases. As the flow rate of the gas flowing through decreases, it becomes longer.
 そこで、本実施形態の圧送量制御部551は、さらに作動ガス循環型エンジン501のエンジン回転数を取得し、このエンジン回転数に基づいて凝縮水ポンプ82の駆動を制御し凝縮水の圧送量を制御することで、上記の供給時点に対する凝縮水の凝縮水到達時点の応答遅れ時間を踏まえた凝縮水の圧送量の制御を行っている。 Therefore, the pumping amount control unit 551 of the present embodiment further acquires the engine speed of the working gas circulation engine 501 and controls the driving of the condensate pump 82 based on the engine speed, thereby controlling the pumping amount of the condensed water. By controlling, the pumping amount of the condensed water is controlled based on the response delay time at the time when the condensed water reaches the condensed water.
 圧送量制御部551は、上述したようにクランク角センサ51が検出するクランク角度に基づいてクランクシャフト19の回転数であるエンジン回転数を算出し取得する。そして、圧送量制御部551は、例えば、図12に示す応答遅れ時間マップm03に基づいて、供給時点に対する凝縮水の凝縮水到達時点の応答遅れ時間を求める。この応答遅れ時間マップm03は、横軸がエンジン回転数、縦軸が応答遅れ時間を示す。応答遅れ時間マップm03は、圧送量制御部551が取得したエンジン回転数と、供給時点に対する凝縮水の凝縮水到達時点の応答遅れ時間との関係を記述したものである。この応答遅れ時間マップm03では、応答遅れ時間は、エンジン回転数の増加にともなって減少する。応答遅れ時間マップm03は、記憶部50bに格納されている。圧送量制御部551は、この応答遅れ時間マップm03に基づいて、エンジン回転数から応答遅れ時間を求める。 The pumping amount control unit 551 calculates and acquires the engine speed, which is the speed of the crankshaft 19, based on the crank angle detected by the crank angle sensor 51 as described above. And the pumping amount control part 551 calculates | requires the response delay time of the condensed water arrival time of the condensed water with respect to a supply time, for example based on the response delay time map m03 shown in FIG. In this response delay time map m03, the horizontal axis indicates the engine speed, and the vertical axis indicates the response delay time. The response delay time map m03 describes the relationship between the engine speed acquired by the pumping amount control unit 551 and the response delay time when the condensed water reaches the condensate relative to the supply time. In this response delay time map m03, the response delay time decreases as the engine speed increases. The response delay time map m03 is stored in the storage unit 50b. The pumping amount control unit 551 obtains a response delay time from the engine speed based on the response delay time map m03.
 そして、圧送量制御部551は、エンジン回転数に基づいて求めた応答遅れ時間の経過後に、実際に燃焼室CCに噴射された水素の供給量に基づいた凝縮水の圧送量となるように圧送部80の凝縮水ポンプ82の駆動を制御する。これにより、本実施形態の作動ガス循環型エンジン501は、燃焼室CCに水素が供給された供給時点と、この供給時点で供給された水素の供給量に応じた凝縮水が凝縮水貯留タンク70に到達する凝縮水到達時点との間の応答遅れ時間を踏まえた凝縮水の圧送量の制御を行うことができ、燃焼室CCへの実際の水素の供給量に応じた圧送部80による凝縮水の圧送量の見込み制御を正確に実行することができる。つまり、本実施形態の作動ガス循環型エンジン501は、実際に燃焼室CCに噴射された水素の供給量に応じて発生する凝縮水の発生量に対して圧送部80による凝縮水の圧送量を応答性よく正確に追従させることができるので、結果的に凝縮水貯留タンク70を小型化することができる。 Then, the pumping amount control unit 551 pumps the condensate so that it becomes the pumping amount of the condensed water based on the supply amount of hydrogen actually injected into the combustion chamber CC after the response delay time obtained based on the engine speed has elapsed. The drive of the condensed water pump 82 of the part 80 is controlled. As a result, the working gas circulation engine 501 of the present embodiment is configured so that the condensed water corresponding to the supply time when hydrogen is supplied to the combustion chamber CC and the supply amount of hydrogen supplied at this supply time is stored in the condensed water storage tank 70. The condensate pumping amount can be controlled based on the response delay time between the condensate arrival time and the condensate water arrival point at which the condensate water is supplied by the pumping unit 80 according to the actual hydrogen supply amount to the combustion chamber CC. The predictive control of the pumping amount can be executed accurately. That is, the working gas circulation engine 501 of the present embodiment is configured to reduce the amount of condensed water pumped by the pumping unit 80 with respect to the amount of condensed water generated according to the amount of hydrogen actually injected into the combustion chamber CC. Since the responsiveness can be followed accurately, the condensed water storage tank 70 can be downsized as a result.
 次に、図13のフローチャートを参照して本実施形態に係る作動ガス循環型エンジン501の圧送量制御を説明する。なお、この制御ルーチンは、数msないし数十ms毎の制御周期で繰り返し実行される。 Next, the control of the pumping amount of the working gas circulation engine 501 according to this embodiment will be described with reference to the flowchart of FIG. This control routine is repeatedly executed at a control cycle of several ms to several tens of ms.
 まず、電子制御装置50の圧送量制御部551は、例えば、燃料噴射手段(燃料噴射弁)42の開弁期間や燃料流量計45が検出する水素の流量に基づいて実際に燃料噴射手段42から燃焼室CCに噴射された水素の供給量を取得する(S300)。 First, the pumping amount control unit 551 of the electronic control unit 50 actually starts from the fuel injection unit 42 based on the valve opening period of the fuel injection unit (fuel injection valve) 42 or the flow rate of hydrogen detected by the fuel flow meter 45, for example. A supply amount of hydrogen injected into the combustion chamber CC is acquired (S300).
 次に、圧送量制御部551は、例えば、圧送量マップm02に基づいて、S300で取得した水素の供給量から圧送部80による凝縮水の圧送量を算出する(S301)。 Next, for example, based on the pumping amount map m02, the pumping amount control unit 551 calculates the pumping amount of condensed water by the pumping unit 80 from the hydrogen supply amount acquired in S300 (S301).
 次に、圧送量制御部551は、クランク角センサ51が検出するクランク角度に基づいてエンジン回転数を算出、取得し、例えば、応答遅れ時間マップm03に基づいて、エンジン回転数から応答遅れ時間を算出する(S302)。 Next, the pumping amount control unit 551 calculates and acquires the engine speed based on the crank angle detected by the crank angle sensor 51, and calculates the response delay time from the engine speed based on the response delay time map m03, for example. Calculate (S302).
 次に、圧送量制御部551は、S302で算出した応答遅れ時間経過後の圧送量として、S301で算出した圧送量を記憶部50bに格納する(S303)。 Next, the pumping amount control unit 551 stores the pumping amount calculated in S301 in the storage unit 50b as the pumping amount after the response delay time calculated in S302 (S303).
 次に、圧送量制御部551は、現時点における圧送量を記憶部50bから呼び出す(S304)。 Next, the pumping amount control unit 551 calls the current pumping amount from the storage unit 50b (S304).
 次に、圧送量制御部551は、S304で呼び出した現時点における圧送量に基づいて、圧送部80の凝縮水ポンプ82の駆動を制御し、凝縮水ポンプ82による圧送量を変更し(S305)、現在の制御周期を終了し、次の制御周期に移行する。 Next, the pumping amount control unit 551 controls the driving of the condensed water pump 82 of the pumping unit 80 based on the current pumping amount called in S304, and changes the pumping amount by the condensed water pump 82 (S305). End the current control cycle and move to the next control cycle.
 以上で説明した本発明の実施形態に係る作動ガス循環型エンジン501によれば、作動ガス循環型エンジン501は、凝縮水貯留タンク70に貯留される凝縮水を圧送部80により大気圧よりも高い圧力で熱交換器90に圧送し、熱交換器90によりこの圧送された凝縮水を排気ガスの排気熱を利用して蒸発させることから、凝縮水貯留タンク70に貯留されている凝縮水を水蒸気として大気に放出することができ、この結果、例えば、作動ガス循環型エンジン501の車両への搭載性を向上し、凝縮器60によって分離された凝縮水を適正に処理することができる。 According to the working gas circulation engine 501 according to the embodiment of the present invention described above, the working gas circulation engine 501 has the condensed water stored in the condensed water storage tank 70 higher than the atmospheric pressure by the pumping unit 80. The condensate stored in the condensate storage tank 70 is steamed because the condensed water pumped by the heat exchanger 90 is evaporated using the exhaust heat of the exhaust gas. As a result, for example, the mounting property of the working gas circulation engine 501 on the vehicle can be improved, and the condensed water separated by the condenser 60 can be appropriately processed.
 さらに、以上で説明した本発明の実施形態に係る作動ガス循環型エンジン501によれば、作動ガス循環型エンジン501は、凝縮水の発生量に基づいて圧送量制御部551が圧送部80の凝縮水ポンプ82の駆動を制御し圧送部80の凝縮水ポンプ82による凝縮水の圧送量を制御することから、凝縮水の発生量に応じた圧送量で、凝縮水貯留タンク70の凝縮水を熱交換器90に向けて圧送し、蒸発させることができるので、凝縮水貯留タンク70に貯留しておく凝縮水の量を少なくすることができる。この結果、作動ガス循環型エンジン501は、凝縮器60によって分離された凝縮水を適正に処理した上で、凝縮水貯留タンク70の容量を小さくすることができ、よって、作動ガス循環型エンジン501の車両への搭載性をさらに向上することができる。 Furthermore, according to the working gas circulation engine 501 according to the embodiment of the present invention described above, the working gas circulation engine 501 is configured such that the pumping amount control unit 551 condenses the pumping unit 80 based on the amount of condensed water generated. Since the driving of the water pump 82 is controlled and the amount of condensed water pumped by the condensed water pump 82 of the pressure feeding unit 80 is controlled, the condensed water in the condensed water storage tank 70 is heated with the amount of pumping according to the amount of condensed water generated. Since it can be pumped toward the exchanger 90 and evaporated, the amount of condensed water stored in the condensed water storage tank 70 can be reduced. As a result, the working gas circulation engine 501 can reduce the capacity of the condensed water storage tank 70 after properly treating the condensed water separated by the condenser 60, and thus the working gas circulation engine 501. Can be further improved.
 さらに、以上で説明した本発明の実施形態に係る作動ガス循環型エンジン501によれば、圧送量制御部551は、燃焼室CCに供給される酸素又は水素、ここでは水素の供給量に基づいて圧送部80による凝縮水の圧送量を制御する。したがって、作動ガス循環型エンジン501は、例えば、上述した流量センサ54(図5参照)や水位センサ55(図7参照)などの実際に発生した凝縮水の発生量を直接的に検出するセンサを備えなくても、圧送量制御部551が凝縮水の発生量に対応する値として、実際に燃料噴射手段42から燃焼室CCに噴射された水素の供給量に基づいて圧送部80による凝縮水の圧送量を制御することで、結果的に凝縮水の発生量に基づいて圧送部80による凝縮水の圧送量を制御することができる。この結果、作動ガス循環型エンジン501は、この作動ガス循環型エンジン501を構成する部品点数を抑制することができ、作動ガス循環型エンジン501の製造コストを抑制することができる。 Furthermore, according to the working gas circulation engine 501 according to the embodiment of the present invention described above, the pumping amount control unit 551 is based on oxygen or hydrogen supplied to the combustion chamber CC, here, the supply amount of hydrogen. The pumping amount of the condensed water by the pumping unit 80 is controlled. Therefore, the working gas circulation engine 501 is a sensor that directly detects the amount of condensed water actually generated, such as the flow rate sensor 54 (see FIG. 5) and the water level sensor 55 (see FIG. 7) described above. Even if it is not provided, the condensate water by the pressure feed unit 80 is based on the supply amount of hydrogen actually injected from the fuel injection means 42 into the combustion chamber CC as a value corresponding to the amount of condensed water generated by the pressure feed amount control unit 551. By controlling the pumping amount, as a result, the pumping amount of the condensed water by the pumping unit 80 can be controlled based on the amount of condensed water generated. As a result, the working gas circulation engine 501 can suppress the number of parts constituting the working gas circulation engine 501 and can reduce the manufacturing cost of the working gas circulation engine 501.
 さらに、以上で説明した本発明の実施形態に係る作動ガス循環型エンジン501によれば、圧送量制御部551は、エンジン負荷及びエンジン回転数に基づいて圧送部80による凝縮水の圧送量を制御する。したがって、作動ガス循環型エンジン501は、圧送量制御部551がエンジン負荷、エンジン回転数に基づいて圧送部80による凝縮水の圧送量を制御することで、エンジン回転数に応じた応答遅れ時間の経過後に、エンジン負荷、例えば、水素の供給量に基づいた凝縮水の圧送量となるように圧送部80の凝縮水ポンプ82の駆動を制御することができるので、実際のエンジン負荷、例えば、実際に燃焼室CCに噴射された水素の供給量に応じて発生する凝縮水の発生量に対して、圧送部80による凝縮水の圧送量を応答性よく正確に追従させることができるので、結果的に凝縮水貯留タンク70を小型化することができる。 Furthermore, according to the working gas circulation engine 501 according to the embodiment of the present invention described above, the pumping amount control unit 551 controls the pumping amount of the condensed water by the pumping unit 80 based on the engine load and the engine speed. To do. Therefore, the working gas circulation engine 501 has a response delay time corresponding to the engine speed by the pumping amount control unit 551 controlling the pumping amount of the condensed water by the pumping unit 80 based on the engine load and the engine speed. After the elapse of time, the driving of the condensate pump 82 of the pumping unit 80 can be controlled so that the engine load, for example, the condensate pumping amount based on the hydrogen supply amount, can be controlled. As a result, the amount of condensed water pumped by the pumping section 80 can be accurately followed with high response to the amount of condensed water generated according to the amount of hydrogen injected into the combustion chamber CC. Moreover, the condensed water storage tank 70 can be reduced in size.
 なお、以上の説明では、圧送量制御部551は、例えば、燃料噴射手段(燃料噴射弁)42の開弁期間や燃料流量計45が検出する水素の流量に基づいて実際に燃料噴射手段42から燃焼室CCに噴射された水素の供給量を取得するものとして説明したがこれに限らない。 In the above description, the pumping amount control unit 551 is actually connected to the fuel injection means 42 based on the valve opening period of the fuel injection means (fuel injection valve) 42 or the hydrogen flow rate detected by the fuel flow meter 45. Although it demonstrated as what acquires the supply amount of the hydrogen injected into the combustion chamber CC, it is not restricted to this.
 図14は、本発明の変形例3に係る作動ガス循環型エンジンの模式的な概略構成図である。 FIG. 14 is a schematic configuration diagram of a working gas circulation engine according to the third modification of the present invention.
 本変形例に係る作動ガス循環型エンジン501Aは、図14に示すように、圧力検出手段としての圧力センサ56Aを備える。圧力センサ56Aは、燃料貯留タンク41に設けられており、この燃料貯留タンク41内の圧力を検出するものである。圧力センサ56Aは、検出信号を電子制御装置50に送信する。 The working gas circulation engine 501A according to this modification includes a pressure sensor 56A as pressure detecting means, as shown in FIG. The pressure sensor 56 </ b> A is provided in the fuel storage tank 41 and detects the pressure in the fuel storage tank 41. The pressure sensor 56 </ b> A transmits a detection signal to the electronic control device 50.
 そして、圧送量制御部551は、この圧力センサ56Aが検出する燃料貯留タンク41内の圧力に基づいて実際に燃料噴射手段42から燃焼室CCに噴射された水素の供給量を算出し取得するようにしてもよい。すなわち、圧送量制御部551は、圧力センサ56Aが検出する燃料貯留タンク41内の圧力の変動量、さらに言えば、減少量に基づいて、実際に燃料噴射手段42から燃焼室CCに噴射された水素の供給量を算出することができる。この場合であっても作動ガス循環型エンジン501Aは、例えば、上述した流量センサ54(図5参照)や水位センサ55(図7参照)などの実際に発生した凝縮水の発生量を直接的に検出するセンサを備えなくても、圧送量制御部551が凝縮水の発生量に対応する値として、実際に燃料噴射手段42から燃焼室CCに噴射された水素の供給量に基づいて圧送部80による凝縮水の圧送量を制御することで、結果的に凝縮水の発生量に基づいて圧送部80による凝縮水の圧送量を制御することができる。 Then, the pumping amount control unit 551 calculates and acquires the supply amount of hydrogen actually injected from the fuel injection means 42 into the combustion chamber CC based on the pressure in the fuel storage tank 41 detected by the pressure sensor 56A. It may be. That is, the pumping amount control unit 551 is actually injected from the fuel injection means 42 into the combustion chamber CC based on the fluctuation amount of the pressure in the fuel storage tank 41 detected by the pressure sensor 56A, that is, the reduction amount. The supply amount of hydrogen can be calculated. Even in this case, the working gas circulation engine 501A directly determines the amount of condensed water actually generated, such as the flow rate sensor 54 (see FIG. 5) and the water level sensor 55 (see FIG. 7) described above. Even if a sensor for detecting the pressure is not provided, the pressure feed control unit 551 determines the value corresponding to the amount of condensed water generated based on the supply amount of hydrogen actually injected from the fuel injection means 42 into the combustion chamber CC. As a result, the amount of condensed water pumped by the pumping unit 80 can be controlled based on the amount of condensed water generated.
(実施形態6)
 図15は、本発明の実施形態6に係る作動ガス循環型エンジンの模式的な概略構成図である。実施形態6に係る作動ガス循環型エンジンは、実施形態1に係る作動ガス循環型エンジンと略同様の構成であるが廃熱回収手段を備える点で実施形態1に係る作動ガス循環型エンジンとは異なる。その他、上述した実施形態と共通する構成、作用、効果については、重複した説明はできるだけ省略するとともに、同一の符号を付す。
(Embodiment 6)
FIG. 15 is a schematic configuration diagram of a working gas circulation engine according to Embodiment 6 of the present invention. The working gas circulation engine according to the sixth embodiment has substantially the same configuration as the working gas circulation engine according to the first embodiment, but is different from the working gas circulation engine according to the first embodiment in that it includes waste heat recovery means. Different. In addition, about the structure, effect | action, and effect which are common in embodiment mentioned above, while overlapping description is abbreviate | omitted as much as possible, the same code | symbol is attached | subjected.
 本実施形態に係る作動ガス循環型エンジン601は、図15に示すように、廃熱回収手段としての膨張機610を備える。 The working gas circulation engine 601 according to the present embodiment includes an expander 610 as waste heat recovery means, as shown in FIG.
 膨張機610は、熱交換器90により凝縮水を蒸発させることで発生する水蒸気のエネルギを運動エネルギとして回収するものである。 The expander 610 collects the energy of water vapor generated by evaporating condensed water by the heat exchanger 90 as kinetic energy.
 膨張機610は、凝縮水経路81をなす大気開放通路83に設けられる。膨張機610は、大気開放通路83の熱交換器90と大気側の開口との間に設けられる。これにより、膨張機610は、大気開放通路83を介して熱交換器90で発生した水蒸気が導入される。 The expander 610 is provided in the atmosphere opening passage 83 that forms the condensed water passage 81. The expander 610 is provided between the heat exchanger 90 in the atmosphere opening passage 83 and the opening on the atmosphere side. As a result, the expander 610 is introduced with water vapor generated in the heat exchanger 90 through the atmosphere opening passage 83.
 そして、膨張機610は、この水蒸気を膨張させて仕事をさせることで、すなわち、水蒸気の膨張により出力回転部材611を回転させることで、水蒸気のエネルギを出力回転部材611の回転運動エネルギに変換する。つまり、膨張機610は、熱交換器90で生じた水蒸気のエネルギを回収して機械エネルギへと変換し、出力回転部材611の回転出力として出力する。出力回転部材611は、例えば、クランクシャフト19や発電機(不図示)の回転軸に接続され、出力回転部材611の回転出力は、このクランクシャフト19や発電機(不図示)の回転軸に伝達される。 The expander 610 expands the water vapor to work, that is, rotates the output rotation member 611 by the expansion of the water vapor, thereby converting the energy of the water vapor into the rotational kinetic energy of the output rotation member 611. . That is, the expander 610 recovers the energy of water vapor generated in the heat exchanger 90, converts it into mechanical energy, and outputs the mechanical energy as the rotational output of the output rotating member 611. The output rotation member 611 is connected to, for example, a rotation shaft of a crankshaft 19 or a generator (not shown), and the rotation output of the output rotation member 611 is transmitted to the rotation shaft of the crankshaft 19 or a generator (not shown). Is done.
 上記のように構成される作動ガス循環型エンジン601は、膨張機610が熱交換器90で発生した水蒸気のエネルギを運動エネルギとして回収し、回収した出力回転部材611の回転出力をクランクシャフト19や発電機(不図示)の回転軸に伝達することで、例えば、作動ガス循環型エンジン601全体に要求される出力を得るためのエンジン本体10によるエンジン出力を相対的に小さくすることができるので、燃料消費率を抑制することができ、航続距離を伸ばすことができる。そして、作動ガス循環型エンジン601は、作動ガス循環型エンジン601全体に要求される出力を得るためのエンジン本体10によるエンジン出力を相対的に小さくすることができることで、例えば、作動ガス循環型エンジン601全体に要求される出力を得るためのエンジン本体10によるエンジン出力を相対的に小さくすることができるので、水素と酸素との燃焼により発生する水蒸気の発生量を抑制することができ、ひいては、凝縮水の発生量を抑制することができる。この結果、作動ガス循環型エンジン601は、凝縮器60、ラジエータ63、凝縮水貯留タンク70の容量を相対的に小さくすることができ、作動ガス循環型エンジン601の車両への搭載性を向上することができる。 The working gas circulation engine 601 configured as described above collects the energy of water vapor generated by the expander 610 in the heat exchanger 90 as kinetic energy, and uses the recovered rotational output of the output rotating member 611 as the crankshaft 19 or the like. By transmitting to the rotating shaft of the generator (not shown), for example, the engine output by the engine body 10 for obtaining the output required for the working gas circulation engine 601 as a whole can be relatively reduced. The fuel consumption rate can be suppressed, and the cruising range can be extended. The working gas circulation engine 601 can relatively reduce the engine output by the engine body 10 to obtain the output required for the working gas circulation engine 601 as a whole. For example, the working gas circulation engine 601 Since the engine output by the engine body 10 for obtaining the output required for the entire 601 can be made relatively small, the amount of water vapor generated by the combustion of hydrogen and oxygen can be suppressed. The amount of condensed water generated can be suppressed. As a result, the working gas circulation engine 601 can relatively reduce the capacities of the condenser 60, the radiator 63, and the condensed water storage tank 70, thereby improving the mountability of the working gas circulation engine 601 on the vehicle. be able to.
 以上で説明した本発明の実施形態に係る作動ガス循環型エンジン601によれば、作動ガス循環型エンジン601は、凝縮水貯留タンク70に貯留される凝縮水を圧送部80により大気圧よりも高い圧力で熱交換器90に圧送し、熱交換器90によりこの圧送された凝縮水を排気ガスの排気熱を利用して蒸発させることから、凝縮水貯留タンク70に貯留されている凝縮水を水蒸気として大気に放出することができ、この結果、例えば、作動ガス循環型エンジン601の車両への搭載性を向上し、凝縮器60によって分離された凝縮水を適正に処理することができる。 According to the working gas circulation engine 601 according to the embodiment of the present invention described above, the working gas circulation engine 601 is configured so that the condensed water stored in the condensed water storage tank 70 is higher than the atmospheric pressure by the pumping unit 80. The condensate stored in the condensate storage tank 70 is steamed because the condensed water pumped by the heat exchanger 90 is evaporated using the exhaust heat of the exhaust gas. As a result, for example, the mounting property of the working gas circulation engine 601 on the vehicle can be improved, and the condensed water separated by the condenser 60 can be appropriately treated.
 さらに、以上で説明した本発明の実施形態に係る作動ガス循環型エンジン601によれば、熱交換器90により凝縮水を蒸発させることで発生する水蒸気のエネルギを運動エネルギとして回収する膨張機610を備える。したがって、作動ガス循環型エンジン601は、膨張機610が熱交換器90で発生した水蒸気のエネルギを運動エネルギとして回収し、回収した出力回転部材611の回転出力をクランクシャフト19や発電機(不図示)の回転軸に伝達することで、例えば、作動ガス循環型エンジン601全体に要求される出力を得るためのエンジン本体10によるエンジン出力を相対的に小さくすることができるので、燃料消費率を抑制し航続距離を伸ばすことができると共に、水蒸気の発生量、凝縮水の発生量を抑制することができ、凝縮器60、ラジエータ63、凝縮水貯留タンク70の容量を相対的に小さくすることができることから、作動ガス循環型エンジン601の車両への搭載性を向上することができる。 Furthermore, according to the working gas circulation engine 601 according to the embodiment of the present invention described above, the expander 610 that recovers the energy of water vapor generated by evaporating condensed water by the heat exchanger 90 as kinetic energy. Prepare. Therefore, the working gas circulation engine 601 collects the energy of water vapor generated by the expander 610 in the heat exchanger 90 as kinetic energy, and uses the collected rotational output of the output rotating member 611 as a crankshaft 19 or a generator (not shown). ) To the rotating shaft, for example, the engine output by the engine body 10 for obtaining the output required for the working gas circulation engine 601 as a whole can be made relatively small, so the fuel consumption rate is suppressed. The cruising distance can be increased, the amount of water vapor and condensed water generated can be suppressed, and the capacities of the condenser 60, radiator 63, and condensed water storage tank 70 can be made relatively small. Therefore, the mounting property of the working gas circulation engine 601 on the vehicle can be improved.
(実施形態7)
 図16は、本発明の実施形態7に係る作動ガス循環型エンジンの模式的な概略構成図、図17は、本発明の実施形態7に係る作動ガス循環型エンジンの凝縮水温度制御を説明するフローチャートである。実施形態7に係る作動ガス循環型エンジンは、実施形態6に係る作動ガス循環型エンジンと略同様の構成であるが熱移動手段を備える点で実施形態6に係る作動ガス循環型エンジンとは異なる。その他、上述した実施形態と共通する構成、作用、効果については、重複した説明はできるだけ省略するとともに、同一の符号を付す。
(Embodiment 7)
FIG. 16 is a schematic schematic configuration diagram of a working gas circulation engine according to Embodiment 7 of the present invention, and FIG. 17 illustrates condensate temperature control of the working gas circulation engine according to Embodiment 7 of the present invention. It is a flowchart. The working gas circulation engine according to the seventh embodiment has substantially the same configuration as the working gas circulation engine according to the sixth embodiment, but is different from the working gas circulation engine according to the sixth embodiment in that it includes a heat transfer means. . In addition, about the structure, effect | action, and effect which are common in embodiment mentioned above, while overlapping description is abbreviate | omitted as much as possible, the same code | symbol is attached | subjected.
 本実施形態に係る作動ガス循環型エンジン701は、図16に示すように、熱移動手段としての熱移動部720を備える。 The working gas circulation engine 701 according to the present embodiment includes a heat transfer unit 720 as heat transfer means, as shown in FIG.
 熱移動部720は、所定の条件において、膨張機610を介した水蒸気の熱を凝縮水貯留タンク70に貯留されている凝縮水に移動させるものである。 The heat transfer unit 720 moves the heat of water vapor via the expander 610 to the condensed water stored in the condensed water storage tank 70 under a predetermined condition.
 本実施形態の熱移動部720は、分岐通路721と、熱交換器722と、流量調節弁723と、熱媒循環路724と、熱媒ポンプ725と、循環路放熱部726とを含んで構成される。 The heat transfer unit 720 according to the present embodiment includes a branch passage 721, a heat exchanger 722, a flow rate adjustment valve 723, a heat medium circulation path 724, a heat medium pump 725, and a circulation path heat dissipation section 726. Is done.
 分岐通路721は、凝縮水経路81をなす大気開放通路83から分岐する水蒸気の通路である。分岐通路721は、一端が大気開放通路83の膨張機610と大気側の開口との間に接続されると共に他端が大気に開口する。 The branch passage 721 is a water vapor passage that branches off from the atmosphere opening passage 83 forming the condensed water passage 81. One end of the branch passage 721 is connected between the expander 610 of the atmosphere release passage 83 and the opening on the atmosphere side, and the other end opens to the atmosphere.
 熱交換器722は、分岐通路721を流れる水蒸気と熱媒循環路724を流れる熱交換媒体(以下、熱媒という。)とを熱交換させるものである。熱交換器722は、分岐通路721に設けられる。熱交換器722は、熱媒循環路724が内部を通るようにして接続されている。 The heat exchanger 722 exchanges heat between water vapor flowing through the branch passage 721 and a heat exchange medium (hereinafter referred to as a heat medium) flowing through the heat medium circulation path 724. The heat exchanger 722 is provided in the branch passage 721. The heat exchanger 722 is connected so that the heat medium circulation path 724 passes through the inside.
 流量調節弁723は、分岐通路721を流れる水蒸気の流量を調節するものである。流量調節弁723は、分岐通路721の大気開放通路83と接続される一端と熱交換器722との間に設けられる。流量調節弁723は、電子制御装置50によりその駆動が制御され開度が制御されることで、分岐通路721を通って熱交換器722に導入される水蒸気の流量を調節することができる。 The flow rate adjusting valve 723 adjusts the flow rate of water vapor flowing through the branch passage 721. The flow rate adjustment valve 723 is provided between one end of the branch passage 721 connected to the atmosphere opening passage 83 and the heat exchanger 722. The flow rate adjustment valve 723 is controlled by the electronic control unit 50 so that the opening thereof is controlled, so that the flow rate of water vapor introduced into the heat exchanger 722 through the branch passage 721 can be adjusted.
 熱媒循環路724は、熱交換器722に熱媒を循環させるものであり、熱媒が流動可能である。この熱媒循環路724は、閉じられた環状の経路になっており、内部に熱媒が充填されている。熱媒循環路724は、熱交換器722の内部を通るようにして設けられる。 The heat medium circulation path 724 circulates the heat medium in the heat exchanger 722, and the heat medium can flow. The heat medium circulation path 724 is a closed annular path, and the inside is filled with the heat medium. The heat medium circulation path 724 is provided so as to pass through the inside of the heat exchanger 722.
 熱媒ポンプ725は、熱媒循環路724の経路上に設けられており、熱媒循環路724の熱媒は、この熱媒ポンプ725が駆動することで熱媒循環路724を所定の循環方向で循環することができる。熱媒ポンプ725は、電子制御装置50によりその駆動が制御されることで、熱媒循環路724を循環し熱交換器722に導入される熱媒の循環量を調節することができる。 The heat medium pump 725 is provided on the path of the heat medium circulation path 724, and the heat medium of the heat medium circulation path 724 is driven in the heat medium circulation path 724 in a predetermined circulation direction by driving the heat medium pump 725. Can be circulated in. The driving of the heat medium pump 725 is controlled by the electronic control device 50, and thus the circulation amount of the heat medium that is circulated through the heat medium circulation path 724 and introduced into the heat exchanger 722 can be adjusted.
 循環路放熱部726は、熱媒循環路724の経路上に設けられる。循環路放熱部726は、凝縮水貯留タンク70に貯留される凝縮水と接触するように構成される。循環路放熱部726は、凝縮水貯留タンク70内で熱媒循環路724の一部分を蛇行させるようにして形成される。これにより、循環路放熱部726は、凝縮水貯留タンク70に貯留される凝縮水との接触面積、すなわち、放熱面積を十分に確保することができ、凝縮水に効率よく熱を放熱することができる。 The circulation path heat radiation part 726 is provided on the route of the heat medium circulation path 724. The circulation path heat radiating unit 726 is configured to come into contact with the condensed water stored in the condensed water storage tank 70. The circulation path heat radiation part 726 is formed so as to meander a part of the heat medium circulation path 724 in the condensed water storage tank 70. Thereby, the circulation path heat radiation part 726 can secure a sufficient contact area with the condensed water stored in the condensed water storage tank 70, that is, a heat radiation area, and can efficiently radiate heat to the condensed water. it can.
 したがって、熱移動部720は、流量調節弁723が分岐通路721を流れる水蒸気の流量を調節し水蒸気が熱交換器722に導入されると共に、熱媒ポンプ725が駆動し熱媒循環路724の熱媒が熱交換器722と循環路放熱部726との間を循環することで、熱媒循環路724を循環する熱媒を介して膨張機610を介した水蒸気の熱を凝縮水貯留タンク70に貯留されている凝縮水に移動させることができる。すなわち、熱移動部720は、熱媒循環路724を循環する熱媒が熱交換器722にて膨張機610を介した水蒸気と熱交換し水蒸気から熱を吸収することで、この熱媒の温度が上昇する。そして、熱移動部720は、水蒸気の熱を吸収し温度が上昇した熱媒が熱媒循環路724を循環し循環路放熱部726にて凝縮水貯留タンク70に貯留されている凝縮水と熱交換し凝縮水に熱を放熱することで、言い換えれば、凝縮水が熱媒の熱を吸収することで、この凝縮水の温度が上昇する。つまり、熱移動部720は、膨張機610を介した水蒸気から熱を廃熱回収し、この回収した熱により凝縮水貯留タンク70に貯留されている凝縮水の温度を上昇させる。なお、熱交換器722にて熱媒循環路724を循環する熱媒と熱交換した水蒸気は、分岐通路721の他端の開口から大気に放出される。 Therefore, in the heat transfer unit 720, the flow rate adjustment valve 723 adjusts the flow rate of water vapor flowing through the branch passage 721 so that the water vapor is introduced into the heat exchanger 722, and the heat medium pump 725 is driven to heat the heat medium circulation path 724. As the medium circulates between the heat exchanger 722 and the circulation path heat radiating unit 726, the heat of the steam via the expander 610 is transferred to the condensed water storage tank 70 via the heating medium circulating in the heating medium circulation path 724. It can be moved to the stored condensed water. That is, the heat transfer unit 720 exchanges heat with the water vapor via the expander 610 in the heat exchanger 722 by the heat medium circulating in the heat medium circulation path 724 and absorbs heat from the water vapor, so that the temperature of the heat medium Rises. The heat transfer unit 720 absorbs the heat of the water vapor and the heat medium whose temperature has risen circulates in the heat medium circulation path 724, and the condensed water and heat stored in the condensed water storage tank 70 in the circulation path heat radiation part 726. By exchanging heat and radiating heat to the condensed water, in other words, the condensed water absorbs the heat of the heat medium, so that the temperature of the condensed water rises. That is, the heat transfer unit 720 recovers the heat from the water vapor via the expander 610 and raises the temperature of the condensed water stored in the condensed water storage tank 70 by the recovered heat. Note that the water vapor exchanged with the heat medium circulating in the heat medium circulation path 724 by the heat exchanger 722 is released to the atmosphere from the opening at the other end of the branch path 721.
 ここで、本実施形態の作動ガス循環型エンジン701は、温度検出手段としての温度センサ57を備えると共に、機能概念的に、電子制御装置(ECU)50に熱移動部制御部752が設けられている。 Here, the working gas circulation engine 701 of the present embodiment includes a temperature sensor 57 as temperature detecting means, and a functionally conceptual electronic control unit (ECU) 50 is provided with a heat transfer unit control unit 752. Yes.
 温度センサ57は、凝縮水貯留タンク70の内部に設けられており、凝縮水貯留タンク70に貯留されている凝縮水の温度を検出する。温度センサ57は、検出信号を電子制御装置50に送信する。 The temperature sensor 57 is provided inside the condensed water storage tank 70 and detects the temperature of the condensed water stored in the condensed water storage tank 70. The temperature sensor 57 transmits a detection signal to the electronic control device 50.
 熱移動部制御部752は、熱移動部720の駆動を制御するものであり、ここでは、熱移動部720の流量調節弁723、熱媒ポンプ725の駆動を制御するものである。そして、本実施形態の熱移動部制御部752は、所定の条件において、熱移動部720の流量調節弁723、熱媒ポンプ725を駆動することで、膨張機610を介した水蒸気の熱を凝縮水貯留タンク70に貯留されている凝縮水に移動させる。 The heat transfer unit controller 752 controls the drive of the heat transfer unit 720, and here controls the drive of the flow rate adjustment valve 723 and the heat medium pump 725 of the heat transfer unit 720. And the heat transfer part control part 752 of this embodiment condenses the heat | fever of the water vapor | steam via the expander 610 by driving the flow control valve 723 and the heat medium pump 725 of the heat transfer part 720 on predetermined conditions. The condensed water stored in the water storage tank 70 is moved.
 具体的には、熱移動部制御部752は、温度センサ57が検出した凝縮水貯留タンク70に貯留されている凝縮水の温度が予め設定される所定温度以下である場合に、熱移動部720の流量調節弁723、熱媒ポンプ725を駆動し、膨張機610を介した水蒸気の熱を凝縮水貯留タンク70に貯留されている凝縮水に移動させる。これにより、凝縮水貯留タンク70に貯留されている凝縮水は、予め設定される所定温度以下の低温である場合に、熱移動部720により膨張機610を介した水蒸気から回収された熱によりその温度が上昇し予熱される。 Specifically, when the temperature of the condensed water stored in the condensed water storage tank 70 detected by the temperature sensor 57 is equal to or lower than a predetermined temperature set in advance, the heat transfer unit control unit 752 performs heat transfer unit 720. The flow rate adjustment valve 723 and the heat medium pump 725 are driven to move the heat of the water vapor via the expander 610 to the condensed water stored in the condensed water storage tank 70. As a result, the condensed water stored in the condensed water storage tank 70 is heated by heat recovered from the water vapor via the expander 610 by the heat transfer unit 720 when the temperature is lower than a predetermined temperature set in advance. The temperature rises and is preheated.
 この結果、作動ガス循環型エンジン701は、凝縮水貯留タンク70に貯留されている凝縮水が予め設定される所定温度以下の低温である場合に、凝縮水が熱交換器90に到達する前に予熱されることで、熱交換器90において、この予熱された凝縮水を効率的に蒸発させることができる。そしてさらに、この作動ガス循環型エンジン701は、膨張機610に導入される水蒸気の温度が相対的に上昇することから、膨張機610における廃熱回収の効率を向上することができ、すなわち、膨張機610の出力を増加することができる。したがって、作動ガス循環型エンジン701は、例えば、作動ガス循環型エンジン701全体に要求される出力を得るためのエンジン本体10によるエンジン出力をさらに相対的に小さくすることができるので、燃料消費率をさらに抑制し航続距離をさらに伸ばすことができると共に、水蒸気の発生量、凝縮水の発生量をさらに抑制することができ、凝縮器60、ラジエータ63、凝縮水貯留タンク70の容量をさらに相対的に小さくすることができることから、作動ガス循環型エンジン701の車両への搭載性をさらに向上することができる。 As a result, when the condensed water stored in the condensed water storage tank 70 is at a low temperature that is equal to or lower than a preset predetermined temperature, the working gas circulation engine 701 is not allowed to reach the heat exchanger 90 before the condensed water reaches the heat exchanger 90. By preheating, the preheated condensed water can be efficiently evaporated in the heat exchanger 90. Further, since the temperature of the water vapor introduced into the expander 610 relatively increases, the working gas circulation engine 701 can improve the efficiency of waste heat recovery in the expander 610, that is, the expansion The output of the machine 610 can be increased. Accordingly, the working gas circulation engine 701 can further reduce the engine output by the engine body 10 for obtaining the output required for the working gas circulation engine 701 as a whole, for example. Further, the cruising distance can be further increased and the generation amount of water vapor and the generation amount of condensed water can be further suppressed, and the capacities of the condenser 60, the radiator 63, and the condensed water storage tank 70 can be further increased. Since it can be made small, the mountability of the working gas circulation engine 701 on the vehicle can be further improved.
 また、作動ガス循環型エンジン701は、熱移動部制御部752が熱移動部720の流量調節弁723、熱媒ポンプ725の駆動を制御し、凝縮水貯留タンク70に貯留されている凝縮水の温度を調節し、ひいては、膨張機610に導入される水蒸気の温度を調節することで、この熱移動部720が膨張機610の出力を調節する調節装置、さらには、作動ガス循環型エンジン701全体での出力を調節する調節装置としても機能することができる。 In the working gas circulation engine 701, the heat transfer unit controller 752 controls driving of the flow rate adjusting valve 723 and the heat medium pump 725 of the heat transfer unit 720, and the condensed water stored in the condensed water storage tank 70 is controlled. The heat transfer unit 720 adjusts the output of the expander 610 by adjusting the temperature and, in turn, the temperature of the water vapor introduced into the expander 610, and the working gas circulation engine 701 as a whole. It can also function as an adjusting device that adjusts the output of the.
 次に、図17のフローチャートを参照して本実施形態に係る作動ガス循環型エンジン701の凝縮水温度制御を説明する。なお、この制御ルーチンは、数msないし数十ms毎の制御周期で繰り返し実行される。 Next, the condensate temperature control of the working gas circulation engine 701 according to this embodiment will be described with reference to the flowchart of FIG. This control routine is repeatedly executed at a control cycle of several ms to several tens of ms.
 まず、電子制御装置50の熱移動部制御部752は、温度センサ57が検出した凝縮水貯留タンク70に貯留されている凝縮水の温度を取得する(S400)。 First, the heat transfer unit controller 752 of the electronic control unit 50 acquires the temperature of the condensed water stored in the condensed water storage tank 70 detected by the temperature sensor 57 (S400).
 次に、熱移動部制御部752は、S400で取得した凝縮水の温度が予め設定された所定温度よりも高いか否かを判定する(S401)。 Next, the heat transfer unit control unit 752 determines whether or not the temperature of the condensed water acquired in S400 is higher than a predetermined temperature set in advance (S401).
 熱移動部制御部752は、S400で取得した凝縮水の温度が予め設定された所定温度よりも高いと判定した場合(S401:Yes)、現在の制御周期を終了し、次の制御周期に移行する。 When it is determined that the temperature of the condensed water acquired in S400 is higher than the predetermined temperature set in advance (S401: Yes), the heat transfer unit control unit 752 ends the current control cycle and proceeds to the next control cycle. To do.
 熱移動部制御部752は、S400で取得した凝縮水の温度が予め設定された所定温度以下であると判定した場合(S401:No)、熱媒ポンプ725を駆動しONに制御すると共に流量調節弁723を駆動し凝縮水の温度に応じた所定の開度まで開弁し(S402)、現在の制御周期を終了し、次の制御周期に移行する。 When it is determined that the temperature of the condensed water acquired in S400 is equal to or lower than a predetermined temperature set in advance (S401: No), the heat transfer unit control unit 752 drives the heat medium pump 725 to control it to ON and adjust the flow rate. The valve 723 is driven and opened to a predetermined opening degree corresponding to the temperature of the condensed water (S402), the current control cycle is terminated, and the next control cycle is started.
 以上で説明した本発明の実施形態に係る作動ガス循環型エンジン701によれば、作動ガス循環型エンジン701は、凝縮水貯留タンク70に貯留される凝縮水を圧送部80により大気圧よりも高い圧力で熱交換器90に圧送し、熱交換器90によりこの圧送された凝縮水を排気ガスの排気熱を利用して蒸発させることから、凝縮水貯留タンク70に貯留されている凝縮水を水蒸気として大気に放出することができ、この結果、例えば、作動ガス循環型エンジン701の車両への搭載性を向上し、凝縮器60によって分離された凝縮水を適正に処理することができる。 According to the working gas circulation engine 701 according to the embodiment of the present invention described above, the working gas circulation engine 701 has the condensed water stored in the condensed water storage tank 70 higher than the atmospheric pressure by the pumping unit 80. The condensate stored in the condensate storage tank 70 is steamed because the condensed water pumped by the heat exchanger 90 is evaporated using the exhaust heat of the exhaust gas. As a result, for example, the mounting property of the working gas circulation engine 701 on the vehicle can be improved, and the condensed water separated by the condenser 60 can be appropriately treated.
 さらに、以上で説明した本発明の実施形態に係る作動ガス循環型エンジン701によれば、作動ガス循環型エンジン701は、膨張機610が熱交換器90で発生した水蒸気のエネルギを運動エネルギとして回収し、回収した出力回転部材611の回転出力をクランクシャフト19や発電機(不図示)の回転軸に伝達することで、例えば、作動ガス循環型エンジン701全体に要求される出力を得るためのエンジン本体10によるエンジン出力を相対的に小さくすることができるので、燃料消費率を抑制し航続距離を伸ばすことができると共に、水蒸気の発生量、凝縮水の発生量を抑制することができ、凝縮器60、ラジエータ63、凝縮水貯留タンク70の容量を相対的に小さくすることができることから、作動ガス循環型エンジン701の車両への搭載性を向上することができる。 Furthermore, according to the working gas circulation engine 701 according to the embodiment of the present invention described above, the working gas circulation engine 701 collects energy of water vapor generated by the expander 610 in the heat exchanger 90 as kinetic energy. Then, the rotation output of the collected output rotation member 611 is transmitted to the rotation shaft of the crankshaft 19 or a generator (not shown), for example, an engine for obtaining the output required for the entire working gas circulation engine 701 Since the engine output by the main body 10 can be made relatively small, the fuel consumption rate can be suppressed and the cruising distance can be increased, and the amount of water vapor and condensed water can be suppressed. 60, the capacity of the radiator 63, and the condensed water storage tank 70 can be relatively reduced. It is possible to improve the mountability to the vehicle.
 さらに、以上で説明した本発明の実施形態に係る作動ガス循環型エンジン701によれば、凝縮水貯留タンク70に貯留されている凝縮水の温度を検出する温度センサ57と、温度センサ57が検出した温度が予め設定された所定温度以下である場合に、膨張機610を介した水蒸気の熱を凝縮水貯留タンク70に貯留されている凝縮水に移動させる熱移動部720とを備える。したがって、作動ガス循環型エンジン701は、凝縮水貯留タンク70に貯留されている凝縮水が予め設定される所定温度以下の低温である場合に、凝縮水貯留タンク70に貯留されている凝縮水が熱移動部720により膨張機610を介した水蒸気から回収された熱によりその温度が上昇し予熱されることから、膨張機610に導入される水蒸気の温度を相対的に上昇させ膨張機610の出力を増加することができる。この結果、作動ガス循環型エンジン701は、燃料消費率をさらに抑制し航続距離をさらに伸ばすことができると共に、水蒸気の発生量、凝縮水の発生量をさらに抑制することができ、凝縮器60、ラジエータ63、凝縮水貯留タンク70の容量をさらに相対的に小さくすることができることから、作動ガス循環型エンジン701の車両への搭載性をさらに向上することができる。また、作動ガス循環型エンジン701は、熱移動部720により凝縮水貯留タンク70に貯留されている凝縮水に移動させる水蒸気の熱量を調節することで、膨張機610の出力や作動ガス循環型エンジン701全体での出力を調節することができる。 Furthermore, according to the working gas circulation engine 701 according to the embodiment of the present invention described above, the temperature sensor 57 that detects the temperature of the condensed water stored in the condensed water storage tank 70, and the temperature sensor 57 detects the temperature. And a heat transfer unit 720 that moves the heat of water vapor via the expander 610 to the condensed water stored in the condensed water storage tank 70 when the temperature is equal to or lower than a predetermined temperature set in advance. Therefore, when the condensed water stored in the condensed water storage tank 70 is at a low temperature that is equal to or lower than a predetermined temperature set in advance, the working gas circulation engine 701 uses the condensed water stored in the condensed water storage tank 70. Since the temperature is increased and preheated by the heat recovered from the water vapor via the expander 610 by the heat transfer unit 720, the temperature of the water vapor introduced into the expander 610 is relatively increased to increase the output of the expander 610. Can be increased. As a result, the working gas circulation engine 701 can further suppress the fuel consumption rate and further extend the cruising distance, and can further suppress the generation amount of water vapor and the generation amount of condensed water. Since the capacity | capacitance of the radiator 63 and the condensed water storage tank 70 can be made further relatively small, the mounting property to the vehicle of the working gas circulation type engine 701 can further be improved. In addition, the working gas circulation engine 701 adjusts the heat amount of water vapor transferred to the condensed water stored in the condensed water storage tank 70 by the heat transfer unit 720, so that the output of the expander 610 and the working gas circulation engine are adjusted. The output of the entire 701 can be adjusted.
(実施形態8)
 図18は、本発明の実施形態8に係る作動ガス循環型エンジンの模式的な概略構成図、図19は、本発明の実施形態8に係る作動ガス循環型エンジンの凝縮水温度・水位制御を説明するフローチャートである。実施形態8に係る作動ガス循環型エンジンは、実施形態7に係る作動ガス循環型エンジンと略同様の構成であるが熱移動手段の構成が実施形態7に係る作動ガス循環型エンジンとは異なる。その他、上述した実施形態と共通する構成、作用、効果については、重複した説明はできるだけ省略するとともに、同一の符号を付す。
(Embodiment 8)
FIG. 18 is a schematic schematic configuration diagram of a working gas circulation engine according to an eighth embodiment of the present invention, and FIG. 19 illustrates condensate temperature and water level control of the working gas circulation engine according to the eighth embodiment of the present invention. It is a flowchart to explain. The working gas circulation engine according to the eighth embodiment has substantially the same configuration as the working gas circulation engine according to the seventh embodiment, but the structure of the heat transfer means is different from that of the working gas circulation engine according to the seventh embodiment. In addition, about the structure, effect | action, and effect which are common in embodiment mentioned above, while overlapping description is abbreviate | omitted as much as possible, the same code | symbol is attached | subjected.
 本実施形態に係る作動ガス循環型エンジン801は、図18に示すように、熱移動手段としての熱移動部820を備える。 The working gas circulation engine 801 according to the present embodiment includes a heat transfer unit 820 as heat transfer means, as shown in FIG.
 熱移動部820は、所定の条件において、膨張機610を介した水蒸気の熱を凝縮水貯留タンク870に貯留されている凝縮水に移動させるものである。本実施形態の熱移動部820は、膨張機610を介した水蒸気を凝縮水貯留タンク870内に直接導入することで、膨張機610を介した水蒸気そのものと共に水蒸気の熱を凝縮水貯留タンク870に貯留されている凝縮水に移動させる。 The heat transfer unit 820 moves the heat of water vapor via the expander 610 to the condensed water stored in the condensed water storage tank 870 under predetermined conditions. The heat transfer unit 820 of the present embodiment directly introduces the water vapor via the expander 610 into the condensed water storage tank 870, so that the heat of the water vapor together with the water vapor via the expander 610 is transferred to the condensed water storage tank 870. Move to stored condensate.
 本実施形態の熱移動部820は、分岐通路821と、流量調節弁822とを含んで構成される。 The heat transfer unit 820 of this embodiment includes a branch passage 821 and a flow rate adjustment valve 822.
 分岐通路821は、凝縮水経路81をなす大気開放通路83から分岐する水蒸気の通路である。分岐通路821は、一端が大気開放通路83の膨張機610と大気側の開口との間に接続されると共に他端が凝縮水貯留手段としての凝縮水貯留タンク870の内部で開口する。 The branch passage 821 is a water vapor passage that branches off from the open air passage 83 forming the condensed water passage 81. One end of the branch passage 821 is connected between the expander 610 of the atmosphere opening passage 83 and the opening on the atmosphere side, and the other end opens inside a condensed water storage tank 870 as condensed water storage means.
 流量調節弁822は、分岐通路821を流れる水蒸気の流量を調節するものである。流量調節弁822は、電子制御装置50によりその駆動が制御され開度が制御されることで、分岐通路821を通って凝縮水貯留タンク870の内部に導入される水蒸気の流量を調節することができる。 The flow rate adjustment valve 822 adjusts the flow rate of water vapor flowing through the branch passage 821. The flow rate adjustment valve 822 is controlled by the electronic control unit 50 so that the opening thereof is controlled, and thereby the flow rate of the water vapor introduced into the condensed water storage tank 870 through the branch passage 821 can be adjusted. it can.
 したがって、熱移動部820は、流量調節弁822が分岐通路821を流れる水蒸気の流量を調節し水蒸気を凝縮水貯留タンク870の内部に導入することで、膨張機610を介した水蒸気が凝縮水貯留タンク870内に直接導入され、水蒸気そのものと共に水蒸気の熱を凝縮水貯留タンク870に貯留されている凝縮水に移動させることができる。すなわち、熱移動部820は、分岐通路821を介して膨張機610を通過した水蒸気が凝縮水貯留タンク870内に直接導入することで、凝縮水貯留タンク870に貯留されている凝縮水と水蒸気とが熱交換し凝縮水が水蒸気の熱を吸収することで、この凝縮水の温度が上昇する。つまり、熱移動部820は、膨張機610を介した水蒸気を凝縮水貯留タンク870内に直接導入することで、凝縮水貯留タンク870内の凝縮水により、膨張機610を介した水蒸気から熱を廃熱回収し、この回収した熱により凝縮水の温度を上昇させる。また、熱移動部820は、分岐通路821を介して膨張機610を通過した水蒸気が凝縮水貯留タンク870内に直接導入され、凝縮水貯留タンク870に貯留されている凝縮水と水蒸気とが熱交換し水蒸気が凝縮水に熱を吸収されることで、この水蒸気の温度が下降し一部が液化、凝縮する。これにより、凝縮水貯留タンク870に貯留されている凝縮水の水位は、水蒸気の一部が液化、凝縮することで上昇する。 Accordingly, the heat transfer unit 820 adjusts the flow rate of the water vapor flowing through the branch passage 821 by the flow rate adjustment valve 822 and introduces the water vapor into the condensed water storage tank 870 so that the water vapor via the expander 610 is stored in the condensed water. It is directly introduced into the tank 870, and the heat of the water vapor can be transferred to the condensed water stored in the condensed water storage tank 870 together with the water vapor itself. That is, the heat transfer unit 820 directly introduces the water vapor that has passed through the expander 610 through the branch passage 821 into the condensate water storage tank 870, so that the condensate water and water vapor stored in the condensate water storage tank 870 Heat exchange and the condensed water absorbs the heat of the water vapor, so that the temperature of the condensed water rises. That is, the heat transfer unit 820 directly introduces the water vapor via the expander 610 into the condensed water storage tank 870, so that the heat from the water vapor via the expander 610 is obtained by the condensed water in the condensed water storage tank 870. Waste heat is recovered, and the temperature of the condensed water is increased by the recovered heat. Further, the heat transfer unit 820 directly introduces the water vapor that has passed through the expander 610 via the branch passage 821 into the condensed water storage tank 870, and the condensed water and the water vapor stored in the condensed water storage tank 870 are heated. When the water vapor is exchanged and heat is absorbed by the condensed water, the temperature of the water vapor is lowered, and a part of the water vapor is liquefied and condensed. Thereby, the water level of the condensed water stored in the condensed water storage tank 870 rises as a part of the water vapor is liquefied and condensed.
 なお、本実施形態の凝縮水貯留タンク870は、分岐通路821を介して導入された水蒸気を大気に放出する放出口871を有している。分岐通路821を介して凝縮水貯留タンク870の内部に導入されこの凝縮水貯留タンク870にて液化しなかった水蒸気は、放出口871を介して大気に放出される。 In addition, the condensed water storage tank 870 of this embodiment has the discharge port 871 which discharge | releases the water vapor | steam introduced via the branch passage 821 to air | atmosphere. The water vapor introduced into the condensed water storage tank 870 through the branch passage 821 and not liquefied in the condensed water storage tank 870 is discharged to the atmosphere through the discharge port 871.
 ここで、本実施形態の作動ガス循環型エンジン801は、水位検出手段としての水位センサ55と、温度検出手段としての温度センサ57とを備えると共に、機能概念的に、電子制御装置(ECU)50に熱移動部制御部852が設けられている。 Here, the working gas circulation engine 801 of the present embodiment includes a water level sensor 55 as a water level detection unit and a temperature sensor 57 as a temperature detection unit, and is functionally conceptually an electronic control unit (ECU) 50. The heat transfer unit control unit 852 is provided.
 熱移動部制御部852は、熱移動部820の駆動を制御するものであり、ここでは、熱移動部820の流量調節弁822の駆動を制御するものである。そして、本実施形態の熱移動部制御部852は、所定の条件において、熱移動部820の流量調節弁822を駆動することで、膨張機610を介した水蒸気を凝縮水貯留タンク870に貯留されている凝縮水に移動させる。 The heat transfer unit controller 852 controls the drive of the heat transfer unit 820, and here controls the drive of the flow rate adjustment valve 822 of the heat transfer unit 820. Then, the heat transfer unit control unit 852 of this embodiment drives the flow rate adjustment valve 822 of the heat transfer unit 820 under a predetermined condition, so that the water vapor via the expander 610 is stored in the condensed water storage tank 870. Move to condensed water.
 具体的には、熱移動部制御部852は、温度センサ57が検出した凝縮水貯留タンク870に貯留されている凝縮水の温度が予め設定される所定温度以下である場合に、熱移動部820の流量調節弁822を駆動し、膨張機610を介した水蒸気を分岐通路821を介して凝縮水貯留タンク870内に直接導入する。これにより、凝縮水貯留タンク870に貯留されている凝縮水は、予め設定される所定温度以下の低温である場合に、熱移動部820により膨張機610を介した水蒸気が直接導入されることで水蒸気の熱によりその温度が上昇し予熱される。 Specifically, the heat transfer unit control unit 852, when the temperature of the condensed water stored in the condensed water storage tank 870 detected by the temperature sensor 57 is equal to or lower than a predetermined temperature set in advance, The flow rate regulating valve 822 is driven, and the water vapor that has passed through the expander 610 is directly introduced into the condensed water storage tank 870 via the branch passage 821. As a result, when the condensed water stored in the condensed water storage tank 870 is at a low temperature equal to or lower than a predetermined temperature set in advance, the heat transfer unit 820 directly introduces water vapor via the expander 610. The temperature rises and is preheated by the heat of water vapor.
 この結果、作動ガス循環型エンジン801は、凝縮水貯留タンク870に貯留されている凝縮水が予め設定される所定温度以下の低温である場合に、凝縮水が熱交換器90に到達する前に予熱されることで、熱交換器90において、この予熱された凝縮水を効率的に蒸発させることができる。そしてさらに、この作動ガス循環型エンジン801は、膨張機610に導入される水蒸気の温度が相対的に上昇することから、膨張機610における廃熱回収の効率を向上することができ、すなわち、膨張機610の出力を増加することができる。したがって、作動ガス循環型エンジン801は、例えば、作動ガス循環型エンジン801全体に要求される出力を得るためのエンジン本体10によるエンジン出力をさらに相対的に小さくすることができるので、燃料消費率をさらに抑制し航続距離をさらに伸ばすことができると共に、水蒸気の発生量、凝縮水の発生量をさらに抑制することができ、凝縮器60、ラジエータ63、凝縮水貯留タンク870の容量をさらに相対的に小さくすることができることから、作動ガス循環型エンジン801の車両への搭載性をさらに向上することができる。 As a result, when the condensed water stored in the condensed water storage tank 870 is at a low temperature that is equal to or lower than a predetermined temperature set in advance, the working gas circulation engine 801 does not reach the heat exchanger 90 before the condensed water reaches the heat exchanger 90. By preheating, the preheated condensed water can be efficiently evaporated in the heat exchanger 90. Further, the working gas circulation engine 801 can improve the efficiency of waste heat recovery in the expander 610 since the temperature of the water vapor introduced into the expander 610 is relatively increased. The output of the machine 610 can be increased. Accordingly, the working gas circulation engine 801 can further reduce the engine output by the engine main body 10 for obtaining the output required for the working gas circulation engine 801 as a whole, for example, so that the fuel consumption rate can be reduced. Further, the cruising distance can be further increased and the generation amount of water vapor and the generation amount of condensed water can be further suppressed, and the capacities of the condenser 60, the radiator 63, and the condensed water storage tank 870 can be further relatively increased. Since it can be made small, the mountability of the working gas circulation engine 801 on the vehicle can be further improved.
 また、作動ガス循環型エンジン801は、熱移動部制御部852が熱移動部820の流量調節弁822の駆動を制御し、凝縮水貯留タンク870に貯留されている凝縮水の温度を調節し、ひいては、膨張機610に導入される水蒸気の温度を調節することで、この熱移動部820が膨張機610の出力を調節する調節装置、さらには、作動ガス循環型エンジン801全体での出力を調節する調節装置としても機能することができる。 Further, in the working gas circulation engine 801, the heat transfer unit control unit 852 controls the driving of the flow rate adjustment valve 822 of the heat transfer unit 820 to adjust the temperature of the condensed water stored in the condensed water storage tank 870, As a result, the heat transfer unit 820 adjusts the output of the expander 610 by adjusting the temperature of water vapor introduced into the expander 610, and further adjusts the output of the working gas circulation engine 801 as a whole. It can also function as an adjusting device.
 そしてさらに、本実施形態の熱移動部制御部852は、水位センサ55が検出した凝縮水貯留タンク870に貯留されている凝縮水の水位が予め設定される所定水位以下である場合に、熱移動部820の流量調節弁822を駆動し、膨張機610を介した水蒸気を分岐通路821を介して凝縮水貯留タンク870内に直接導入する。これにより、凝縮水貯留タンク870に貯留されている凝縮水は、予め設定される所定水位以下の低水位である場合に、熱移動部820により膨張機610を介した水蒸気が直接導入されることで水蒸気の一部が液化、凝縮しその水位が上昇する。 Further, the heat transfer unit controller 852 of the present embodiment performs heat transfer when the water level of the condensed water stored in the condensed water storage tank 870 detected by the water level sensor 55 is equal to or lower than a predetermined water level set in advance. The flow control valve 822 of the unit 820 is driven, and the water vapor that has passed through the expander 610 is directly introduced into the condensed water storage tank 870 via the branch passage 821. Thereby, when the condensed water stored in the condensed water storage tank 870 is at a low water level not higher than a predetermined water level set in advance, water vapor is directly introduced by the heat transfer unit 820 via the expander 610. As a result, part of the water vapor liquefies and condenses and the water level rises.
 この結果、作動ガス循環型エンジン801は、凝縮水貯留タンク870に貯留されている凝縮水が予め設定される所定水位以下の低水位である場合に、熱移動部820により膨張機610を介した水蒸気が直接導入され水蒸気の一部が液化、凝縮しその水位が上昇することで、例えば凝縮水貯留タンク870の凝縮水の枯渇を防止することができ、凝縮水ポンプ82が気体を吸い込んでしまうことを防止することができる。 As a result, when the condensed water stored in the condensed water storage tank 870 has a low water level that is equal to or lower than a predetermined water level set in advance, the working gas circulation engine 801 passes the expander 610 through the expander 610. Steam is directly introduced and a part of the steam is liquefied and condensed, and its water level rises. For example, it is possible to prevent depletion of condensed water in the condensed water storage tank 870, and the condensed water pump 82 sucks gas. This can be prevented.
 次に、図19のフローチャートを参照して本実施形態に係る作動ガス循環型エンジン801の凝縮水温度・水位制御を説明する。なお、この制御ルーチンは、数msないし数十ms毎の制御周期で繰り返し実行される。 Next, the condensate temperature / water level control of the working gas circulation engine 801 according to this embodiment will be described with reference to the flowchart of FIG. This control routine is repeatedly executed at a control cycle of several ms to several tens of ms.
 まず、電子制御装置50の熱移動部制御部852は、温度センサ57が検出した凝縮水貯留タンク870に貯留されている凝縮水の温度及び水位センサ55が検出した凝縮水貯留タンク870に貯留されている凝縮水の水位を取得する(S500)。 First, the heat transfer unit controller 852 of the electronic control unit 50 is stored in the condensed water storage tank 870 detected by the temperature sensor 55 and the temperature of the condensed water stored in the condensed water storage tank 870 detected by the temperature sensor 57. The level of the condensed water is acquired (S500).
 次に、熱移動部制御部852は、S500で取得した凝縮水の温度が予め設定された所定温度よりも高いか否かを判定する(S501)。 Next, the heat transfer unit control unit 852 determines whether or not the temperature of the condensed water acquired in S500 is higher than a predetermined temperature set in advance (S501).
 熱移動部制御部852は、S500で取得した凝縮水の温度が予め設定された所定温度よりも高いと判定した場合(S501:Yes)、S500で取得した凝縮水の水位が予め設定された所定水位よりも高いか否かを判定する(S502)。 When it is determined that the temperature of the condensed water acquired in S500 is higher than the predetermined temperature set in advance (S501: Yes), the heat transfer unit control unit 852 sets the predetermined water level of the condensed water acquired in S500. It is determined whether it is higher than the water level (S502).
 熱移動部制御部852は、S500で取得した凝縮水の水位が予め設定された所定水位よりも高いと判定した場合(S502:Yes)、現在の制御周期を終了し、次の制御周期に移行する。 When it is determined that the water level of the condensed water acquired in S500 is higher than the predetermined water level set in advance (S502: Yes), the heat transfer unit control unit 852 ends the current control cycle and proceeds to the next control cycle. To do.
 熱移動部制御部852は、S500で取得した凝縮水の温度が予め設定された所定温度以下であると判定した場合(S501:No)、流量調節弁822を駆動し凝縮水の温度に応じた所定の開度まで開弁し(S503)、現在の制御周期を終了し、次の制御周期に移行する。 When it is determined that the temperature of the condensed water acquired in S500 is equal to or lower than the predetermined temperature set in advance (S501: No), the heat transfer unit control unit 852 drives the flow rate adjustment valve 822 to respond to the temperature of the condensed water. The valve is opened to a predetermined opening degree (S503), the current control cycle is terminated, and the next control cycle is started.
 熱移動部制御部852は、S500で取得した凝縮水の水位が予め設定された所定水位以下であると判定した場合(S502:No)、流量調節弁822を駆動し凝縮水の水位に応じた所定の開度まで開弁し(S503)、現在の制御周期を終了し、次の制御周期に移行する。 When it is determined that the water level of the condensed water acquired in S500 is equal to or lower than the predetermined water level set in advance (S502: No), the heat transfer unit control unit 852 drives the flow control valve 822 to respond to the water level of the condensed water. The valve is opened to a predetermined opening degree (S503), the current control cycle is terminated, and the next control cycle is started.
 以上で説明した本発明の実施形態に係る作動ガス循環型エンジン801によれば、作動ガス循環型エンジン801は、凝縮水貯留タンク870に貯留される凝縮水を圧送部80により大気圧よりも高い圧力で熱交換器90に圧送し、熱交換器90によりこの圧送された凝縮水を排気ガスの排気熱を利用して蒸発させることから、凝縮水貯留タンク870に貯留されている凝縮水を水蒸気として大気に放出することができ、この結果、例えば、作動ガス循環型エンジン801の車両への搭載性を向上し、凝縮器60によって分離された凝縮水を適正に処理することができる。 According to the working gas circulation engine 801 according to the embodiment of the present invention described above, the working gas circulation engine 801 has the condensed water stored in the condensed water storage tank 870 higher than the atmospheric pressure by the pumping unit 80. The condensate stored in the condensate storage tank 870 is steamed because the condensed water pumped by the heat exchanger 90 is evaporated using the exhaust heat of the exhaust gas. As a result, for example, the mounting property of the working gas circulation engine 801 on the vehicle can be improved, and the condensed water separated by the condenser 60 can be appropriately treated.
 さらに、以上で説明した本発明の実施形態に係る作動ガス循環型エンジン801によれば、作動ガス循環型エンジン801は、膨張機610が熱交換器90で発生した水蒸気のエネルギを運動エネルギとして回収し、回収した出力回転部材611の回転出力をクランクシャフト19や発電機(不図示)の回転軸に伝達することで、例えば、作動ガス循環型エンジン801全体に要求される出力を得るためのエンジン本体10によるエンジン出力を相対的に小さくすることができるので、燃料消費率を抑制し航続距離を伸ばすことができると共に、水蒸気の発生量、凝縮水の発生量を抑制することができ、凝縮器60、ラジエータ63、凝縮水貯留タンク870の容量を相対的に小さくすることができることから、作動ガス循環型エンジン801の車両への搭載性を向上することができる。 Furthermore, according to the working gas circulation engine 801 according to the embodiment of the present invention described above, the working gas circulation engine 801 collects the energy of water vapor generated by the expander 610 in the heat exchanger 90 as kinetic energy. Then, by transmitting the rotation output of the collected output rotation member 611 to the rotation shaft of the crankshaft 19 or a generator (not shown), for example, an engine for obtaining an output required for the entire working gas circulation engine 801 Since the engine output by the main body 10 can be made relatively small, the fuel consumption rate can be suppressed and the cruising distance can be increased, and the amount of water vapor and condensed water can be suppressed. 60, the capacity of the radiator 63, and the condensed water storage tank 870 can be relatively reduced, so that the working gas circulation engine 8 It is possible to improve the mountability to the first vehicle.
 さらに、以上で説明した本発明の実施形態に係る作動ガス循環型エンジン801によれば、凝縮水貯留タンク870に貯留されている凝縮水の温度を検出する温度センサ57と、温度センサ57が検出した温度が予め設定された所定温度以下である場合に、膨張機610を介した水蒸気の熱を凝縮水貯留タンク870に貯留されている凝縮水に移動させる熱移動部820とを備える。したがって、作動ガス循環型エンジン801は、凝縮水貯留タンク870に貯留されている凝縮水が予め設定される所定温度以下の低温である場合に、凝縮水貯留タンク870に貯留されている凝縮水が熱移動部820により膨張機610を介した水蒸気から回収された熱によりその温度が上昇し予熱されることから、膨張機610に導入される水蒸気の温度を相対的に上昇させ膨張機610の出力を増加することができる。この結果、作動ガス循環型エンジン801は、燃料消費率をさらに抑制し航続距離をさらに伸ばすことができると共に、水蒸気の発生量、凝縮水の発生量をさらに抑制することができ、凝縮器60、ラジエータ63、凝縮水貯留タンク870の容量をさらに相対的に小さくすることができることから、作動ガス循環型エンジン801の車両への搭載性をさらに向上することができる。また、作動ガス循環型エンジン801は、熱移動部820により凝縮水貯留タンク870に貯留されている凝縮水に移動させる水蒸気の熱量を調節することで、膨張機610の出力や作動ガス循環型エンジン801全体での出力を調節することができる。 Furthermore, according to the working gas circulation engine 801 according to the embodiment of the present invention described above, the temperature sensor 57 that detects the temperature of the condensed water stored in the condensed water storage tank 870, and the temperature sensor 57 detects the temperature. And a heat transfer unit 820 that moves the heat of the water vapor via the expander 610 to the condensed water stored in the condensed water storage tank 870 when the temperature is equal to or lower than a predetermined temperature set in advance. Therefore, when the condensed water stored in the condensed water storage tank 870 has a low temperature equal to or lower than a predetermined temperature set in advance, the working gas circulation engine 801 uses the condensed water stored in the condensed water storage tank 870 to Since the temperature rises and is preheated by the heat recovered from the water vapor via the expander 610 by the heat transfer unit 820, the temperature of the water vapor introduced into the expander 610 is relatively increased to increase the output of the expander 610. Can be increased. As a result, the working gas circulation engine 801 can further suppress the fuel consumption rate and further extend the cruising distance, and can further suppress the generation amount of water vapor and the generation amount of condensed water. Since the capacity | capacitance of the radiator 63 and the condensed water storage tank 870 can further be made relatively small, the mounting property to the vehicle of the working gas circulation type engine 801 can further be improved. In addition, the working gas circulation engine 801 adjusts the amount of water vapor transferred to the condensed water stored in the condensed water storage tank 870 by the heat transfer unit 820, so that the output of the expander 610 and the working gas circulation engine can be adjusted. The output of the whole 801 can be adjusted.
 さらに、以上で説明した本発明の実施形態に係る作動ガス循環型エンジン801によれば、凝縮水貯留タンク870に貯留されている凝縮水の水位を検出する水位センサ55を備え、熱移動部820は、水位センサ55が検出した水位が予め設定された所定水位以下である場合に、膨張機610を介した水蒸気を凝縮水貯留タンク870に貯留されている凝縮水に導入する。したがって、作動ガス循環型エンジン801は、凝縮水貯留タンク870に貯留されている凝縮水の水位が予め設定される所定水位以下の低水位である場合に、熱移動部820により膨張機610を介した水蒸気を凝縮水貯留タンク870内に直接導入しこの水蒸気の一部が液化、凝縮することで、凝縮水貯留タンク870に貯留されている凝縮水の水位を上昇させることができる。この結果、作動ガス循環型エンジン801は、凝縮水貯留タンク870に貯留されている凝縮水の水位が上昇することで、例えば凝縮水貯留タンク870の凝縮水の枯渇を防止することができ、凝縮水ポンプ82が気体を吸い込んでしまうことを防止することができる。 Furthermore, the working gas circulation engine 801 according to the embodiment of the present invention described above includes the water level sensor 55 that detects the water level of the condensed water stored in the condensed water storage tank 870, and includes the heat transfer unit 820. When the water level detected by the water level sensor 55 is equal to or lower than a predetermined water level set in advance, the water vapor through the expander 610 is introduced into the condensed water stored in the condensed water storage tank 870. Therefore, the working gas circulation engine 801 passes the expander 610 by the heat transfer unit 820 when the water level of the condensed water stored in the condensed water storage tank 870 is a low water level equal to or lower than a predetermined water level set in advance. By directly introducing the water vapor into the condensed water storage tank 870 and liquefying and condensing a part of the water vapor, the water level of the condensed water stored in the condensed water storage tank 870 can be raised. As a result, the working gas circulation engine 801 can prevent depletion of the condensed water in the condensed water storage tank 870, for example, by increasing the water level of the condensed water stored in the condensed water storage tank 870. It is possible to prevent the water pump 82 from sucking gas.
 なお、上述した本発明の実施形態に係る作動ガス循環型エンジンは、上述した実施形態に限定されず、特許請求の範囲に記載された範囲で種々の変更が可能である。本発明の実施形態に係る作動ガス循環型エンジンは、以上で説明した実施形態を複数組み合わせることで構成してもよい。例えば、本発明の実施形態に係る作動ガス循環型エンジンは、実施形態5に係る作動ガス循環型エンジン501(図10参照)と、実施形態8に係る作動ガス循環型エンジン801(図18参照)とを組み合わせることで構成してもよい。すなわち、図20に示す本発明の変形例4に係る作動ガス循環型エンジン801Aは、例えば、熱移動手段としての熱移動部820を備えると共に、機能概念的に、電子制御装置(ECU)50に圧送量制御手段としての圧送量制御部551と、熱移動部制御部852とが設けられていてもよい。 The working gas circulation engine according to the above-described embodiment of the present invention is not limited to the above-described embodiment, and various modifications can be made within the scope described in the claims. The working gas circulation engine according to the embodiment of the present invention may be configured by combining a plurality of the embodiments described above. For example, the working gas circulation engine according to the embodiment of the present invention includes the working gas circulation engine 501 according to the fifth embodiment (see FIG. 10) and the working gas circulation engine 801 according to the eighth embodiment (see FIG. 18). You may comprise by combining. That is, the working gas circulation engine 801A according to the fourth modification of the present invention shown in FIG. A pumping amount control unit 551 as a pumping amount control unit and a heat transfer unit control unit 852 may be provided.
 以上の説明では、作動ガス循環型エンジンは、燃料が燃焼室CC内に直接噴射されるよう燃料噴射手段42を設けるものとして説明したが、燃料噴射手段42は、燃料を吸気ポート11bに噴射させるべくシリンダヘッド11に取り付けられてもよい。つまり、以上で説明した本発明の作動ガス循環型エンジンは、いわゆるポート噴射式の作動ガス循環型エンジンに適用してもよく、この場合であっても、凝縮水を適正に処理することができる。 In the above description, the working gas circulation engine has been described as providing the fuel injection means 42 so that the fuel is directly injected into the combustion chamber CC. However, the fuel injection means 42 injects the fuel into the intake port 11b. It may be attached to the cylinder head 11 as much as possible. That is, the working gas circulation engine of the present invention described above may be applied to a so-called port injection working gas circulation engine, and even in this case, the condensed water can be appropriately processed. .
 以上の説明では、作動ガス循環型エンジンは、燃料としての水素(H)を拡散燃焼させるものとして例示したが、燃料に対して図示しない点火プラグで点火して、いわゆる、火花点火燃焼させる形態のものであってもよく、その燃料に対して点火プラグで点火して着火の補助を行い拡散燃焼させる形態のものであってもよい。つまり、以上で説明した本発明の作動ガス循環型エンジンは、燃焼形態の異なる作動ガス循環型エンジンに適用してもよく、この場合であっても、凝縮水を適正に処理することができる。 In the above description, the working gas circulation engine has been exemplified as a fuel that diffuses and burns hydrogen (H 2 ) as a fuel. However, a so-called spark ignition combustion is performed by igniting a fuel with a spark plug (not shown). Alternatively, the fuel may be ignited with a spark plug to assist ignition and diffuse combustion may be used. That is, the working gas circulation engine of the present invention described above may be applied to working gas circulation engines having different combustion forms, and even in this case, the condensed water can be appropriately processed.
 以上のように、本発明に係る作動ガス循環型エンジンは、凝縮水を適正に処理することができるものであり、排気ガス中に含まれる作動ガスを燃焼室の排気側から吸気側に循環させ再び燃焼室に供給可能な種々の作動ガス循環型エンジンに適用して好適である。 As described above, the working gas circulation engine according to the present invention can appropriately process condensed water, and circulates the working gas contained in the exhaust gas from the exhaust side to the intake side of the combustion chamber. The present invention is suitable for various working gas circulation engines that can be supplied to the combustion chamber again.

Claims (15)

  1.  酸化剤と、当該酸化剤との燃焼により水蒸気を生成する燃料と、空気より比熱比の高い作動ガスとが供給され、前記燃料の燃焼に伴って前記作動ガスが膨張可能であると共に前記燃料の燃焼後の排気ガスとして前記水蒸気と前記作動ガスとを排気可能な燃焼室と、
     前記排気ガス中に含まれる前記作動ガスを前記燃焼室の排気側から吸気側に循環させ再び前記燃焼室に供給可能な循環経路と、
     前記循環経路に設けられ前記排気ガス中に含まれる前記水蒸気を凝縮して凝縮水とする凝縮手段と、
     前記凝縮水を貯留可能な凝縮水貯留手段と、
     前記凝縮水貯留手段に貯留される前記凝縮水を大気圧よりも高い圧力で圧送する圧送手段と、
     前記圧送手段により圧送された前記凝縮水を前記排気ガスの排気熱により蒸発させる蒸発手段とを備えることを特徴とする、
     作動ガス循環型エンジン。
    An oxidant, a fuel that generates water vapor by combustion with the oxidant, and a working gas having a specific heat ratio higher than that of air are supplied, and the working gas can expand as the fuel burns, and the fuel A combustion chamber capable of exhausting the water vapor and the working gas as exhaust gas after combustion;
    A circulation path through which the working gas contained in the exhaust gas can be circulated from the exhaust side to the intake side of the combustion chamber and supplied again to the combustion chamber;
    Condensation means provided in the circulation path to condense the water vapor contained in the exhaust gas into condensed water;
    Condensed water storage means capable of storing the condensed water;
    A pumping means for pumping the condensed water stored in the condensed water storage means at a pressure higher than atmospheric pressure;
    Evaporating means for evaporating the condensed water pumped by the pumping means by exhaust heat of the exhaust gas,
    Working gas circulation engine.
  2.  前記酸化剤は、酸素であり、前記燃料は、水素である、
     請求項1に記載の作動ガス循環型エンジン。
    The oxidant is oxygen and the fuel is hydrogen;
    The working gas circulation engine according to claim 1.
  3.  前記蒸発手段は、前記循環経路を循環する前記作動ガスの循環方向に対して前記凝縮手段より上流側の前記排気ガスの排気熱により前記凝縮水を蒸発させる、
     請求項1に記載の作動ガス循環型エンジン。
    The evaporating means evaporates the condensed water by exhaust heat of the exhaust gas upstream from the condensing means with respect to a circulation direction of the working gas circulating in the circulation path;
    The working gas circulation engine according to claim 1.
  4.  前記圧送手段は、前記凝縮水貯留手段と前記蒸発手段とを前記凝縮水が流動可能に接続する凝縮水経路と、前記凝縮水経路に設けられ当該凝縮水経路の前記凝縮水を加圧し前記凝縮水貯留手段側から前記蒸発手段側に圧送するポンプとを有する、
     請求項1に記載の作動ガス循環型エンジン。
    The pressure feeding means includes a condensed water path connecting the condensed water storage means and the evaporation means so that the condensed water can flow, and pressurizes the condensed water of the condensed water path provided in the condensed water path to condense the condensed water. A pump for pumping from the water storage means side to the evaporation means side,
    The working gas circulation engine according to claim 1.
  5.  前記圧送手段は、前記凝縮水貯留手段と前記蒸発手段とを前記凝縮水が流動可能に接続すると共に、前記凝縮水を貯留する空間部が密閉状態とされた前記凝縮水貯留手段を介して前記循環経路と連通する凝縮水経路を有し、大気圧よりも高い前記循環経路のガスの圧力により前記凝縮水経路の前記凝縮水を加圧し前記凝縮水貯留手段側から前記蒸発手段側に圧送する、
     請求項1に記載の作動ガス循環型エンジン。
    The pumping means connects the condensed water storage means and the evaporating means so that the condensed water can flow, and the space for storing the condensed water is sealed via the condensed water storage means. A condensed water path communicating with the circulating path, pressurizing the condensed water in the condensed water path by the pressure of the gas in the circulating path higher than atmospheric pressure, and pumping the condensed water from the condensed water storage means side to the evaporation means side ,
    The working gas circulation engine according to claim 1.
  6.  前記圧送手段は、前記循環経路から分岐して設けられ相対的に高圧の前記作動ガスを貯留する作動ガス貯留手段と、前記作動ガス貯留手段と前記循環経路との間の前記作動ガスの流出入を調節する調節手段とを有する、
     請求項5に記載の作動ガス循環型エンジン。
    The pressure feeding means is provided by branching from the circulation path and storing the relatively high pressure working gas, and the working gas inflow and outflow between the working gas storage means and the circulation path. Adjusting means for adjusting
    The working gas circulation engine according to claim 5.
  7.  前記凝縮水の発生量に基づいて前記圧送手段による前記凝縮水の圧送量を制御する圧送量制御手段を備える、
     請求項1に記載の作動ガス循環型エンジン。
    Comprising a pumping amount control means for controlling the pumping amount of the condensed water by the pumping means based on the generation amount of the condensed water;
    The working gas circulation engine according to claim 1.
  8.  前記圧送量制御手段は、前記圧送量が前記発生量と同等になるように圧送量を制御する、
     請求項7に記載の作動ガス循環型エンジン。
    The pumping amount control means controls the pumping amount so that the pumping amount becomes equal to the generated amount.
    The working gas circulation engine according to claim 7.
  9.  前記凝縮水貯留手段への前記凝縮水の流量を検出する流量検出手段を備え、
     前記圧送量制御手段は、前記流量検出手段が検出した前記凝縮水の流量に基づいて前記圧送量を制御する、
     請求項7に記載の作動ガス循環型エンジン。
    Comprising flow rate detection means for detecting the flow rate of the condensed water to the condensed water storage means,
    The pumping amount control unit controls the pumping amount based on the flow rate of the condensed water detected by the flow rate detection unit.
    The working gas circulation engine according to claim 7.
  10.  前記凝縮水貯留手段に貯留されている前記凝縮水の水位を検出する水位検出手段を備え、
     前記圧送量制御手段は、前記水位検出手段が検出した前記凝縮水の水位に基づいて前記圧送量を制御する、
     請求項7に記載の作動ガス循環型エンジン。
    Comprising water level detection means for detecting the level of the condensed water stored in the condensed water storage means,
    The pumping amount control unit controls the pumping amount based on the water level of the condensed water detected by the water level detection unit.
    The working gas circulation engine according to claim 7.
  11.  前記圧送量制御手段は、前記燃焼室に供給される前記酸化剤又は前記燃料の供給量に基づいて前記圧送量を制御する、
     請求項7に記載の作動ガス循環型エンジン。
    The pumping amount control means controls the pumping amount based on a supply amount of the oxidant or the fuel supplied to the combustion chamber.
    The working gas circulation engine according to claim 7.
  12.  前記圧送量制御手段は、エンジン負荷及びエンジン回転数に基づいて前記凝縮水の圧送量を制御する、
     請求項7に記載の作動ガス循環型エンジン。
    The pumping amount control means controls the pumping amount of the condensed water based on the engine load and the engine speed.
    The working gas circulation engine according to claim 7.
  13.  前記蒸発手段により前記凝縮水を蒸発させることで発生する水蒸気のエネルギを運動エネルギとして回収する廃熱回収手段を備える、
     請求項1に記載の作動ガス循環型エンジン。
    A waste heat recovery means for recovering the energy of water vapor generated by evaporating the condensed water by the evaporation means as kinetic energy;
    The working gas circulation engine according to claim 1.
  14.  前記凝縮水貯留手段に貯留されている前記凝縮水の温度を検出する温度検出手段と、
     前記温度検出手段が検出した温度が予め設定された所定温度以下である場合に、前記廃熱回収手段を介した水蒸気の熱を前記凝縮水貯留手段に貯留されている前記凝縮水に移動させる熱移動手段とを備える、
     請求項13に記載の作動ガス循環型エンジン。
    Temperature detecting means for detecting the temperature of the condensed water stored in the condensed water storing means;
    Heat that moves the heat of water vapor through the waste heat recovery means to the condensed water stored in the condensed water storage means when the temperature detected by the temperature detection means is equal to or lower than a predetermined temperature set in advance. A moving means,
    The working gas circulation engine according to claim 13.
  15.  前記凝縮水貯留手段に貯留されている前記凝縮水の水位を検出する水位検出手段を備え、
     前記熱移動手段は、前記水位検出手段が検出した水位が予め設定された所定水位以下である場合に、前記廃熱回収手段を介した水蒸気を前記凝縮水貯留手段に貯留されている前記凝縮水に導入する、
     請求項14に記載の作動ガス循環型エンジン。
    Comprising water level detection means for detecting the level of the condensed water stored in the condensed water storage means,
    When the water level detected by the water level detection unit is equal to or lower than a predetermined water level set in advance, the heat transfer unit is configured to store the condensed water stored in the condensed water storage unit through the waste heat recovery unit. To introduce,
    The working gas circulation engine according to claim 14.
PCT/JP2009/052431 2009-02-13 2009-02-13 Operating gas circulation type engine WO2010092684A1 (en)

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