WO2014109339A1 - Ship - Google Patents

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Publication number
WO2014109339A1
WO2014109339A1 PCT/JP2014/050170 JP2014050170W WO2014109339A1 WO 2014109339 A1 WO2014109339 A1 WO 2014109339A1 JP 2014050170 W JP2014050170 W JP 2014050170W WO 2014109339 A1 WO2014109339 A1 WO 2014109339A1
Authority
WO
WIPO (PCT)
Prior art keywords
exhaust gas
egr
path
cleaning device
exhaust
Prior art date
Application number
PCT/JP2014/050170
Other languages
French (fr)
Japanese (ja)
Inventor
哲司 上田
平岡 直大
村田 聡
渡辺 昌彦
祐輔 渡辺
昭範 羽染
前田 毅
Original Assignee
三菱重工業株式会社
三菱化工機株式会社
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 三菱重工業株式会社, 三菱化工機株式会社 filed Critical 三菱重工業株式会社
Priority to KR1020197016152A priority Critical patent/KR102156504B1/en
Priority to KR1020167025388A priority patent/KR20160111545A/en
Priority to CN201480002504.5A priority patent/CN104736830B/en
Priority to KR1020157007910A priority patent/KR20150056560A/en
Publication of WO2014109339A1 publication Critical patent/WO2014109339A1/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
    • 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02BINTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
    • F02B37/00Engines characterised by provision of pumps driven at least for part of the time by exhaust
    • 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
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/02Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
    • F01N3/04Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust using liquids
    • 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
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
    • F01N3/24Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by constructional aspects of converting apparatus
    • 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
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M35/00Combustion-air cleaners, air intakes, intake silencers, or induction systems specially adapted for, or arranged on, internal-combustion engines
    • F02M35/10Air intakes; Induction systems
    • 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
    • F01N2590/00Exhaust or silencing apparatus adapted to particular use, e.g. for military applications, airplanes, submarines
    • F01N2590/02Exhaust or silencing apparatus adapted to particular use, e.g. for military applications, airplanes, submarines for marine vessels or naval applications
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02BINTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
    • F02B29/00Engines characterised by provision for charging or scavenging not provided for in groups F02B25/00, F02B27/00 or F02B33/00 - F02B39/00; Details thereof
    • F02B29/04Cooling of air intake supply
    • 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
    • F02M26/02EGR systems specially adapted for supercharged engines
    • F02M26/04EGR systems specially adapted for supercharged engines with a single turbocharger
    • F02M26/06Low pressure loops, i.e. wherein recirculated exhaust gas is taken out from the exhaust downstream of the turbocharger turbine and reintroduced into the intake system upstream of the compressor
    • 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
    • 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
    • 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

Definitions

  • the present invention relates to a ship including an exhaust gas cleaning device for cleaning exhaust gas and an internal combustion engine for performing EGR.
  • EGR Exhaust Gas Recirculation
  • EGR disclosed in Patent Document 2 is a system that recirculates exhaust gas after passing through a turbocharger turbine and being decompressed, and is called low-pressure EGR.
  • an exhaust gas cleaning device is provided for removing SOx (nitrogen oxide) and PM (particulate matter) in the exhaust gas. Regulations on SOx in exhaust gas are expected to be further strengthened in the future, and as described in the same document, it is considered to install an exhaust gas cleaning device such as a scrubber.
  • a wet two-stage flue gas desulfurization apparatus including a venturi scrubber and a desulfurization absorption tower is known as an exhaust gas cleaning apparatus that removes not only SOx but also PM.
  • various types of wet collecting devices for cleaning exhaust gas are known.
  • Patent Document 2 exhaust gas after passing through an economizer and an exhaust gas cleaning device is recirculated from the turbocharger turbine, not the exhaust gas immediately after the outlet of the turbocharger turbine.
  • the economizer and the exhaust gas cleaning device pass through the economizer regardless of whether or not EGR is performed. Therefore, exhaust heat recovery by the economizer is performed without waste, and it is not necessary to control the exhaust gas cleaning device according to the EGR rate. It is excellent in that point.
  • since SOx and PM are sufficiently removed by the exhaust gas cleaning device there is no problem in the properties of the exhaust gas for performing EGR, and further when the exhaust gas is recirculated. It was thought that there was no need to install a cleaning device.
  • the venturi scrubber mainly removes soot, which is the main component of PM
  • the desulfurization absorption tower mainly removes SOx.
  • the wet two-stage flue gas desulfurization device has a large pressure loss because it is necessary to increase the gas flow velocity at the throat portion of the venturi, and when it is installed in a low pressure line downstream of the turbocharger turbine outlet of the internal combustion engine, A blower for discharging is essential after the device.
  • Non-Patent Document 1 Various types of wet collection devices (exhaust gas cleaning devices) are known as shown in Non-Patent Document 1, but a device that can remove both SOx and PM theoretically and practically. The existence was not known. In particular, when sufficient removal of SOx is required, for example, the SOx removal rate [percentage of SOx amount in exhaust gas at the outlet with respect to the SOx amount in exhaust gas at the inlet of the exhaust gas cleaning device] is 95% or more. It is thought that it is necessary to secure a time for SOx to be dissolved in the liquid by increasing the contact time between the absorption liquid (for example, water, seawater, etc. and their aqueous solution) flowing through the exhaust gas cleaning device and the exhaust gas containing SOx.
  • the absorption liquid for example, water, seawater, etc. and their aqueous solution
  • the present invention has been made in view of such circumstances, and provides a ship equipped with an internal combustion engine that can perform EGR with exhaust gas from which not only SOx but also impurities such as PM are reliably removed.
  • the purpose is to do.
  • it aims at providing the ship provided with the internal combustion engine which can reduce the blower capacity
  • a ship according to the present invention is a supercharger having an internal combustion engine body for propulsion of a ship, a turbine driven by exhaust gas from the internal combustion engine body, and a compressor connected to the turbine and compressing intake air.
  • the venturi scrubber has the ability to remove SOx as well as impurities such as PM. Therefore, a venturi scrubber was adopted as an EGR exhaust gas cleaning device provided in the EGR path. Thereby, not only impurities such as PM but also SOx can be removed through the EGR path during EGR operation. Since a venturi scrubber is provided in the EGR path, it is sufficient to provide an EGR blower with a capacity corresponding to the amount of exhaust gas flowing through the EGR path, even if the pressure loss caused by the venturi scrubber is compensated. The blower capacity can be reduced as compared with the case where a blower is provided for the total amount of exhaust gas.
  • venturi scrubber is smaller in size than a general scrubber such as a desulfurization absorption tower, so that the installation space can be reduced as much as possible.
  • venturi scrubber can be installed on the internal combustion engine main body as an accessory of the internal combustion engine main body, and can be made more compact, and the design of the installation location of the internal combustion engine main body as a ship need not be changed. There is a merit.
  • the EGR path may be branched from the upstream side of the turbocharger turbine (high pressure EGR), or may be branched from the downstream side of the turbocharger turbine (low pressure EGR).
  • exhaust gas cleaning for removing sulfur oxides in exhaust gas between the turbine and the branch point and between the branch point and the EGR exhaust gas cleaning device.
  • the apparatus may not be provided.
  • An exhaust gas cleaning device such as a desulfurization absorption tower for removing sulfur oxide is provided between the turbine and the branch point, and between the branch point and the EGR exhaust gas cleaning device, that is, upstream of the EGR exhaust gas cleaning device. Since it is not provided, installation space can be reduced. Moreover, it is good also as not providing an exhaust-gas cleaning apparatus not only in the upstream of an EGR exhaust-gas cleaning apparatus but in the exhaust-gas path
  • the exhaust gas path is provided with an exhaust heat recovery device that recovers heat from the exhaust gas, and the EGR path is branched from the upstream side of the exhaust heat recovery device.
  • the pressure loss of the piping can be reduced compared to the case of branching from the downstream side of the exhaust heat recovery device arranged near the chimney of the ship.
  • the exhaust gas can be guided to the EGR exhaust gas cleaning device which is a venturi scrubber while keeping the pressure of the exhaust gas high.
  • the load of an EGR blower can be reduced and a venturi scrubber can be operated efficiently.
  • route can be shortened significantly and it can be made still more compact.
  • an exhaust heat recovery device that is provided in the exhaust gas path and recovers heat from the exhaust gas, and is provided in the exhaust gas path and downstream of the exhaust heat recovery device, the exhaust gas
  • An exhaust gas cleaning device for removing sulfur oxide therein, and the EGR path is branched from the downstream side of the exhaust heat recovery device and the exhaust gas cleaning device.
  • an EGR exhaust gas cleaning device is further provided in the EGR path.
  • impurities such as PM mainly composed of soot and dust that have not been sufficiently removed by the exhaust gas cleaning device and SOx can be reliably removed by the EGR exhaust gas cleaning device.
  • the EGR exhaust gas cleaning device is mainly intended to remove impurities such as PM in the exhaust gas after most of the SOx is removed, so it can be further downsized and installed on the internal combustion engine body.
  • An exhaust gas cleaning device typically includes a desulfurization absorption tower.
  • the exhaust gas cleaning device is a scrubber that sprays water, and includes a common waste water treatment device that processes waste water from the exhaust gas cleaning device and the EGR exhaust gas cleaning device. .
  • the wastewater from the exhaust gas treatment device designated as a scrubber and the EGR exhaust gas treatment device designated as a venturi scrubber was treated by a common wastewater treatment device. Thereby, the installation space of a waste water treatment apparatus can be omitted and waste water treatment can be performed efficiently.
  • the EGR path may be led to the upstream side of the compressor.
  • the EGR path may be led downstream of the compressor and upstream of the air cooler.
  • the EGR path may be led to the downstream side of the air cooler.
  • venturi scrubber is adopted as the EGR exhaust gas cleaning device provided in the EGR path, not only impurities such as PM but also SOx can be sufficiently removed in the EGR path during EGR operation. As a result, the compressor of the supercharger and the internal combustion engine main body are not adversely affected.
  • FIG. 1 shows a schematic configuration around a diesel engine (internal combustion engine) 1 provided in a ship.
  • the diesel engine 1 includes a diesel engine main body (hereinafter simply referred to as an “engine main body”) 3 that is a main engine for marine propulsion, a supercharger 5 that is driven by exhaust gas from the engine main body 3, and a supercharger. 5 is provided with an EGR system 7 which performs a low pressure EGR by recirculating a part of the exhaust gas led from 5 to the engine body 3.
  • the engine body 3 is a marine two-cycle diesel engine, and for example, a uniflow type that is scavenged in one direction so as to supply air from below and exhaust upward is adopted.
  • the output from the engine body 3 is directly connected to the screw propeller via a propeller shaft (not shown).
  • An exhaust port of a cylinder portion 9 (only four cylinders are shown as an example in FIG. 1) of each cylinder of the engine body 3 is connected to an exhaust static pressure tube 11 as an exhaust gas collecting tube.
  • the exhaust static pressure pipe 11 is connected to the inlet side of the turbine 5a of the supercharger 5 via the first exhaust path L1.
  • each cylinder section 9 is connected to the scavenging trunk 13, and the scavenging trunk 13 is connected to the compressor 5b of the supercharger 5 through the scavenging path K1.
  • An air cooler 15 as an intercooler is installed in the scavenging path K1.
  • the supercharger 5 includes a turbine 5a and a compressor 5b.
  • the turbine 5a and the compressor 5b are coaxially connected by a rotating shaft 5c.
  • the turbine 5a is driven by exhaust gas from the engine body 3, and the turbine work obtained by the turbine 5a is transmitted to the compressor 5b through the rotating shaft 5c.
  • the compressor 5b sucks outside air (air) or a mixture of outside air and recirculation gas and raises the pressure to a predetermined scavenging pressure.
  • An economizer (exhaust heat recovery device) 21 is connected to the second exhaust path L2.
  • the economizer 21 generates steam by the exhaust gas from the engine body 3.
  • the generated steam is used in various places on the ship.
  • a branch point 17 is provided on the upstream side of the economizer 21, and the EGR route L3 branches from the branch point 17.
  • the EGR path L3 is provided with an EGR valve 19 for performing EGR.
  • the opening degree of the EGR valve 19 is adjusted by a control unit (not shown).
  • the EGR valve 19 is fully opened when the engine body 3 is operated to perform EGR, and is fully closed when EGR is not performed.
  • the present invention is not limited to this embodiment, and the valve opening degree of the EGR valve 19 may be appropriately adjusted according to the operating state.
  • a venturi scrubber (EGR exhaust gas cleaning device) 25 is connected to the downstream side of the EGR valve 19 provided in the EGR path L3.
  • the venturi scrubber 25 removes not only impurities such as PM contained in the exhaust gas but also SOx by spraying a liquid such as water on the exhaust gas flowing through the EGR path L3.
  • the venturi scrubber 25 is installed in the vicinity of the engine body 3 or on the engine body 3.
  • the venturi scrubber 25 is smaller in size than a general scrubber such as a desulfurization absorption tower (for example, the venturi scrubber has a diameter of about 1/5 to 1/2 that of a general scrubber, This is possible because the height is about one-third to one-half and is configured to be mounted on the engine body 3).
  • the venturi scrubber 25 includes a venturi scrubber main body 25a and a gas-liquid separator 25b connected to the venturi scrubber main body 25a.
  • the venturi scrubber main body 25a includes an upper large-diameter portion 25c provided vertically above, a reduced taper portion 25d provided below the upper large-diameter portion 25c, and having a flow path cross-sectional area gradually decreasing in the flow direction, and a reduced taper portion 25d.
  • a throat portion 25e provided below, an enlarged taper portion 25f provided below the throat portion 25e and having a channel cross-sectional area gradually increasing in the flow direction, and a lower large diameter portion provided below the enlarged taper portion 25f. 25g.
  • the upper large-diameter portion 25c is provided with a spray nozzle 25h, and an absorbing liquid such as water or an aqueous solution is sprayed from the spray nozzle 25h toward the connection position between the reduced taper portion 25d and the throat portion 25e.
  • the absorbing liquid sprayed from the spray nozzle 25h is effectively diffused and mixed by increasing the flow rate of the exhaust gas at the throat portion 25e of the venturi scrubber body 25a to remove not only impurities such as PM but also SOx. To do.
  • gas-liquid separator 25b moisture contained in the exhaust gas led from the venturi scrubber main body 25a is removed.
  • a mist separator 25i for removing mist remaining in the exhaust gas is provided at the outlet of the gas-liquid separator 25b, and the separated mist is collected in the gas-liquid separator 25b.
  • the gas-liquid separator 25b may be a cyclone method in which the gas and liquid are separated by turning the exhaust gas instead of the method using a mist separator.
  • An EGR blower 27 is provided on the downstream side of the gas-liquid separator 25b.
  • the EGR blower 27 is rotationally driven by an electric motor 29 whose frequency is variable by an inverter.
  • the EGR blower 27 is used to compensate for the pressure loss of the exhaust gas that is generated when the EGR valve 19 and the venturi scrubber 25 pass through the piping constituting the EGR path L3.
  • a mixer 39 is provided on the downstream side of the EGR blower 27.
  • the mixer 39 the recirculated exhaust gas and air are mixed.
  • the mixed gas (only air when EGR is not performed) mixed in the mixer 39 is guided to the suction port of the compressor 5b through the air supply path K2.
  • an EGR cooler (not shown) may be provided on the EGR path. In this case, for example, the EGR cooler is installed downstream of the EGR blower.
  • the exhaust gas flowing through the EGR system 7 flows as a recirculation gas through the EGR valve 19 and through the venturi scrubber 25.
  • the exhaust gas from which not only impurities such as PM but also SOx is removed by the venturi scrubber 25 is guided to the EGR blower 27, and the exhaust gas pressurized to a predetermined pressure by the EGR blower 27 is guided to the mixer 39.
  • the mixer 39 the air and the exhaust gas are mixed and guided to the intake port of the compressor 5b through the intake path K2.
  • the mixture of air and exhaust gas pressurized by the compressor 5b is guided to the air cooler 15 through the scavenging path K1, cooled by the air cooler 15, and then guided to the scavenging trunk 13.
  • the venturi scrubber used in the test has a maximum gas flow rate of 50 to 80 m / s at the throat and a liquid gas ratio (absorbed liquid spray amount [kg] / standard state converted gas flow rate [Nm3]) of 0.5 to 2.0 kg / Nm3.
  • the specification was used.
  • the venturi scrubber nozzle used a one-fluid nozzle, and the spray angle was 80-100 °.
  • the exhaust gas used for the test was the actual exhaust gas of a marine two-cycle diesel engine.
  • the fuel used was A heavy oil, and the sulfur content in the A heavy oil was 0.71 wt%.
  • the engine speed was 105 rpm, which is the rated speed.
  • Gas properties are analyzed using a gas analyzer PG-250 manufactured by HORIBA, Ltd. NOx is analyzed by atmospheric pressure chemiluminescence, SOx and CO2 are analyzed by non-dispersive infrared absorption method, and O2 is analyzed by zirconia oxygen. Measurement was
  • venturi scrubber can significantly remove SOx.
  • NOx, CO2, and O2 cannot be removed significantly but only SOx can be removed is a new finding that has not been conventionally known.
  • the venturi scrubber 25 is adopted as the EGR exhaust gas cleaning device provided in the EGR path, not only impurities such as PM but also SOx can be removed in the EGR path L3 during the EGR operation. Thereby, the compressor 5b and the engine main body 3 are not adversely affected. Since the venturi scrubber 25 is provided in the EGR path L3, it is sufficient to provide the EGR blower 27 having a capacity corresponding to the amount of exhaust gas flowing through the EGR path L3 even when the pressure loss caused by the venturi scrubber 25 is compensated. The blower capacity can be reduced as compared with the case where the blower is provided for the entire amount of exhaust gas discharged from the engine body 3.
  • venturi scrubber 25 is smaller in size than a general scrubber such as a desulfurization absorption tower, the installation space can be reduced.
  • the venturi scrubber 25 can be installed on the engine body 3 as an accessory of the engine body 3 and can be made more compact, and the design of the installation location of the engine body 3 as a ship can be changed. There are good benefits.
  • an exhaust gas cleaning device for removing sulfur oxides is not provided in the second exhaust path L2, which is an exhaust gas path, installation space can be reduced. Further, even if no exhaust gas cleaning device is provided in the second exhaust path L2, SOx can be removed by the venturi scrubber 25 provided in the EGR path L3, so that the intake path of the engine body 3 is recirculated by the exhaust gas. In this case, so-called sulfuric acid dew point corrosion is not caused by condensation as sulfuric acid at a low temperature part.
  • the pressure loss of the piping can be reduced as compared with the case of branching from the downstream side of the economizer 21 arranged in the vicinity of the chimney of the ship.
  • the exhaust gas can be guided to the venturi scrubber 25 while keeping the pressure high.
  • the load of the EGR blower 27 can be reduced, and the venturi scrubber 25 can be operated efficiently.
  • route L3 can be shortened significantly, and it can be made still more compact.
  • An economizer (exhaust heat recovery device) 21 and a desulfurization absorption tower (exhaust gas cleaning device) 23 are sequentially connected to the second exhaust path L2.
  • the desulfurization absorption tower 23 is a packed tower type scrubber, for example, and removes SOx contained in the exhaust gas by spraying an absorption liquid such as water or an aqueous solution to the exhaust gas.
  • an absorption liquid such as water or an aqueous solution to the exhaust gas.
  • SOx is sufficiently removed, and the venturi scrubber 25 mainly remains with impurities such as PM. SOx removal is performed.
  • the desulfurization absorption tower 23 is applied when a fuel containing a sulfur content equal to or greater than the regulation value in the SOx regulation sea area (for example, 1.0% or more) is used as the fuel for the engine body 3.
  • a branch point 17 ′ is provided on the downstream side of the desulfurization absorption tower 23, and the EGR path L 3 branches from this branch point 17 ′.
  • the point that the EGR valve 19, the venturi scrubber 25, and the EGR blower 27 are provided in the EGR path L3 is the same as in the first embodiment.
  • Waste water from the venturi scrubber 25 is treated by the same waste water treatment device (not shown) as the desulfurization absorption tower 23 described above. That is, waste water from the desulfurization absorption tower 23 and the venturi scrubber 25 is processed by a common waste water treatment device.
  • the exhaust gas flowing through the EGR system 7 flows as a recirculation gas through the EGR valve 19 and through the venturi scrubber 25.
  • the venturi scrubber 25 removes impurities such as PM and SOx that has not been removed by the desulfurization absorption tower 23.
  • the exhaust gas that has passed through the venturi scrubber 25 is guided to the EGR blower 27, and the exhaust gas pressurized to a predetermined pressure by the EGR blower 27 is guided to the mixer 39.
  • the mixer 39 the air and the exhaust gas are mixed and guided to the intake port of the compressor 5b through the intake path K2.
  • the mixture of air and exhaust gas pressurized by the compressor 5b is guided to the air cooler 15 through the scavenging path K1, cooled by the air cooler 15, and then guided to the scavenging trunk 13.
  • a venturi scrubber 25 is further provided in the EGR path L3.
  • impurities such as PM that have not been sufficiently removed by the desulfurization absorption tower 23 and the remaining SOx can be reliably removed by the venturi scrubber 25.
  • the compressor 5b and the engine main body 3 are not adversely affected.
  • the venturi scrubber 25 mainly aims to remove impurities such as PM and remaining SOx in the exhaust gas after passing through the desulfurization absorption tower 23, so that it is further downsized compared to the venturi scrubber of the first embodiment. In addition, it is possible to reduce the utility associated with the apparatus.
  • the wastewater from the desulfurization absorption tower 23 and the venturi scrubber 25 was treated with a common wastewater treatment device. Thereby, the installation space of a waste water treatment apparatus can be omitted and waste water treatment can be performed efficiently.
  • the EGR is performed by branching from the branch point 17 ′ on the downstream side of the economizer 21 and the exhaust gas of the entire amount passes through the economizer 21 regardless of whether the EGR is performed or not, the exhaust heat recovery by the economizer 21 is performed. Is effectively done without waste. Further, since the EGR is performed by branching from the branch point 17 ′ on the downstream side of the desulfurization absorption tower 23, the desulfurization absorption tower 23 is passed regardless of whether or not the EGR is performed. Therefore, the desulfurization is performed according to the EGR rate. There is no need to control the absorption tower 23. Further, since the entire amount of exhaust gas passes through the desulfurization absorption tower 23, it is not necessary to use expensive low S component fuel (for example, sulfur content is 1.0% or less) even when a ship navigates the SOx restricted sea area.
  • expensive low S component fuel for example, sulfur content is 1.0% or less
  • the exhaust gas is not recirculated by branching immediately after the turbine 5a of the supercharger 5, but the exhaust gas is recirculated from the branch point 17 ′ on the downstream side of the desulfurization absorption tower 23, and the EGR path It was decided to make it longer.
  • the mist and steam accompanying the desulfurization absorption tower 23 can be removed while the exhaust gas flows through the EGR path L3, the blades of the EGR blower 27 and the blades of the compressor 5b can be protected, and the maintenance cycle is further increased. Can be long.
  • the low-pressure EGR that branches the EGR path L3 from the downstream side of the turbine 5a has been described.
  • the present invention is not limited to this, for example, the upstream side of the turbine 5a. It may be a high pressure EGR branched from the first exhaust path L1.
  • the downstream side of the EGR path L3 is the upstream side of the compressor 5b.
  • the present invention is not limited to this.
  • the downstream side of the compressor 5b and the air The downstream side of the EGR path L3 may be connected to the upstream side of the cooler 15, or the downstream side of the EGR path L3 may be connected to the downstream side of the air cooler 15.
  • the branch point 17 ′ is positioned downstream of the desulfurization absorption tower 23, but may be upstream of the economizer 21, and the economizer 21 and the desulfurization absorption tower 23 It may be between.

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Abstract

Provided is a ship which comprises an internal combustion engine which performs EGR using appropriately cleaned exhaust gas. A ship is provided with: an engine body (3) which propels the ship; a supercharger (5) which is driven by exhaust gas from the engine body (3) and which has a turbine (5a) and a compressor (5b); a second exhaust gas passage (L2) to which the exhaust gas from the turbine (5a) is conducted; an EGR passage (L3) which is branched from the branch point (17) of the second exhaust gas passage (L2), the branch point (17) being located upstream of an economizer (21), and which conducts part of the exhaust gas to upstream of the compressor (5b); and a venturi scrubber (25) which is provided in the EGR passage (L3).

Description

船舶Ship
 本発明は、排気ガスを洗浄する排気ガス洗浄装置を備えるとともにEGRを行う内燃機関を備えた船舶に関するものである。 The present invention relates to a ship including an exhaust gas cleaning device for cleaning exhaust gas and an internal combustion engine for performing EGR.
 近年では、環境への配慮から、船舶の推進用として搭載されたエンジン(内燃機関)から排出される排気ガスに対する規制が強化されつつある。
 排気ガス中に含まれる窒素酸化物(NOx)を低減するために、排気ガスの一部をエンジン本体の給気側に戻すEGR(排気再循環;Exhaust Gas Recirculation)が行われている(下記特許文献1参照)。同文献に開示されたEGRは、過給機のタービンに流入する前の高圧とされた排気ガスを再循環する方式のもので、高圧EGRと称されている。
In recent years, regulations for exhaust gas discharged from an engine (internal combustion engine) mounted for ship propulsion are being strengthened for environmental consideration.
In order to reduce nitrogen oxide (NOx) contained in the exhaust gas, EGR (Exhaust Gas Recirculation) is performed to return a part of the exhaust gas to the supply side of the engine body (the following patent) Reference 1). The EGR disclosed in this document is a type of recirculating exhaust gas that has been made high pressure before flowing into the turbocharger turbine, and is called high pressure EGR.
 これに対して、特許文献2に開示されたEGRは、過給機タービンを通過して減圧された後の排気ガスを再循環する方式のもので、低圧EGRと称されている。同文献では、排気ガス中のSOx(窒素酸化物)やPM(粒子状物質)を除去するために排気ガス洗浄装置が設けられている。排気ガス中のSOxに対する規制についても今後は更に強化されることが予想され、同文献に記載されているように、スクラバ等の排気ガス洗浄装置を設置することが検討されている。
 また、特許文献3に記載されているように、SOxだけでなくPMをも除去する排気ガス洗浄装置として、ベンチュリスクラバおよび脱硫吸収塔を備えた湿式二段排煙脱硫装置が知られている。
 また、非特許文献1に記載されているように、排気ガスを洗浄する湿式捕集装置として種々の形式ものが知られている。
On the other hand, EGR disclosed in Patent Document 2 is a system that recirculates exhaust gas after passing through a turbocharger turbine and being decompressed, and is called low-pressure EGR. In this document, an exhaust gas cleaning device is provided for removing SOx (nitrogen oxide) and PM (particulate matter) in the exhaust gas. Regulations on SOx in exhaust gas are expected to be further strengthened in the future, and as described in the same document, it is considered to install an exhaust gas cleaning device such as a scrubber.
Further, as described in Patent Document 3, a wet two-stage flue gas desulfurization apparatus including a venturi scrubber and a desulfurization absorption tower is known as an exhaust gas cleaning apparatus that removes not only SOx but also PM.
Further, as described in Non-Patent Document 1, various types of wet collecting devices for cleaning exhaust gas are known.
特開2012-172647号公報JP 2012-172647 A 特開2012-047056号公報JP 2012-047056 A 特開2009-240908号公報JP 2009-240908 A
 特許文献2では、過給機タービンの出口直後の排気ガスではなく、過給機タービンからさらにエコノマイザおよび排気ガス洗浄装置を通過した後の排気ガスを再循環させている。これにより、EGRを行うか否かに関わらずエコノマイザおよび排気ガス洗浄装置を通過するので、エコノマイザによる排熱回収が無駄なく行われ、かつEGR率に応じて排気ガス洗浄装置を制御する必要がないという点で優れている。
 そして、特許文献2に記載の構成は、排気ガス洗浄装置によりSOxやPMが十分に除去されているので、EGRを行う排気ガスの性状としては問題がなく、排気ガスを再循環する際に更に洗浄装置を設置する必要は無いと考えられていた。
In Patent Document 2, exhaust gas after passing through an economizer and an exhaust gas cleaning device is recirculated from the turbocharger turbine, not the exhaust gas immediately after the outlet of the turbocharger turbine. As a result, the economizer and the exhaust gas cleaning device pass through the economizer regardless of whether or not EGR is performed. Therefore, exhaust heat recovery by the economizer is performed without waste, and it is not necessary to control the exhaust gas cleaning device according to the EGR rate. It is excellent in that point.
In the configuration described in Patent Document 2, since SOx and PM are sufficiently removed by the exhaust gas cleaning device, there is no problem in the properties of the exhaust gas for performing EGR, and further when the exhaust gas is recirculated. It was thought that there was no need to install a cleaning device.
 また、特許文献3の湿式二段排煙脱硫装置では、ベンチュリスクラバが主にPMの主成分である煤塵の除去を行い、脱硫吸収塔が主にSOxの除去を行う。しかし、湿式二段排煙脱硫装置は、ベンチュリのスロート部でガス流速を大きくする必要があるため圧力損失が大きく、内燃機関の過給機タービン出口の下流のような低圧ラインに設ける場合は脱硫装置後に排出用のブロアが必須となってしまう。したがって、仮に、特許文献3の湿式二段排煙脱硫装置を特許文献2に適用した場合、内燃機関から排出される全ての排気ガス(湿式二段排煙脱硫装置を通過した後にEGR経路に流入する排気ガスを含む)がベンチュリスクラバを通るため、全排気ガスを流すための大容量のブロアが必要となってしまうという問題が生じる。
 また、脱硫吸収塔に加えてベンチュリスクラバを設けるため、装置サイズも大きく、船舶の煙突サイズが大きくなるという問題も生じ、さらに船舶としての設計を変更せざるを得ないという問題も生じる。
Further, in the wet two-stage flue gas desulfurization apparatus of Patent Document 3, the venturi scrubber mainly removes soot, which is the main component of PM, and the desulfurization absorption tower mainly removes SOx. However, the wet two-stage flue gas desulfurization device has a large pressure loss because it is necessary to increase the gas flow velocity at the throat portion of the venturi, and when it is installed in a low pressure line downstream of the turbocharger turbine outlet of the internal combustion engine, A blower for discharging is essential after the device. Therefore, if the wet two-stage flue gas desulfurization device of Patent Document 3 is applied to Patent Document 2, all exhaust gases discharged from the internal combustion engine (flow into the EGR path after passing through the wet two-stage flue gas desulfurization device) A large capacity blower is required to flow all exhaust gases.
Further, since the venturi scrubber is provided in addition to the desulfurization absorption tower, there is a problem that the apparatus size is large, the chimney size of the ship is increased, and there is a problem that the design of the ship must be changed.
 また、非特許文献1に示されているように各種の湿式捕集装置(排気ガス洗浄装置)が種々知られているが、理論的にも現実的にもSOxとPMをともに除去できる装置の存在は知られていなかった。
 特に、例えばSOx除去率[排気ガス洗浄装置の入口における排気ガス中のSOx量に対する出口における排気ガス中のSOx量の百分率]が95%以上といったようにSOxの十分な除去が求められる場合には、排気ガス洗浄装置を流れる吸収液(例えば、水、海水等やこれらの水溶液)とSOxを含む排気ガスの接触時間を長くすることでSOxが液体に溶け込む時間を確保する必要があると考えられていたため、充填塔式スクラバ(特許文献3の脱硫吸収塔)が必要であると一般的に考えられていた。
 一方、ベンチュリスクラバは、ベンチュリによって排気ガスの流速を増させる方式のため、液体とSOxの接触時間を十分に確保できず、SOxを効率的に除去することができないと考えられていた。
Various types of wet collection devices (exhaust gas cleaning devices) are known as shown in Non-Patent Document 1, but a device that can remove both SOx and PM theoretically and practically. The existence was not known.
In particular, when sufficient removal of SOx is required, for example, the SOx removal rate [percentage of SOx amount in exhaust gas at the outlet with respect to the SOx amount in exhaust gas at the inlet of the exhaust gas cleaning device] is 95% or more. It is thought that it is necessary to secure a time for SOx to be dissolved in the liquid by increasing the contact time between the absorption liquid (for example, water, seawater, etc. and their aqueous solution) flowing through the exhaust gas cleaning device and the exhaust gas containing SOx. Therefore, it was generally considered that a packed tower type scrubber (desulfurization absorption tower of Patent Document 3) was necessary.
On the other hand, since the venturi scrubber increases the flow rate of the exhaust gas by venturi, it was considered that the contact time between the liquid and SOx could not be sufficiently secured and SOx could not be removed efficiently.
 本発明は、このような事情に鑑みてなされたものであって、SOxだけでなくPM等の不純物をも確実に除去された排気ガスによってEGRを行うことができる内燃機関を備えた船舶を提供することを目的とする。
 また、排気ガス洗浄装置の設置スペースを可及的に削減できる内燃機関を備えた船舶を提供することを目的とする。
 また、排気ガスを強制送風するためのブロア容量を可及的に低減できる内燃機関を備えた船舶を提供することを目的とする。
The present invention has been made in view of such circumstances, and provides a ship equipped with an internal combustion engine that can perform EGR with exhaust gas from which not only SOx but also impurities such as PM are reliably removed. The purpose is to do.
It is another object of the present invention to provide a ship equipped with an internal combustion engine that can reduce the installation space of the exhaust gas cleaning device as much as possible.
Moreover, it aims at providing the ship provided with the internal combustion engine which can reduce the blower capacity | capacitance for forcedly ventilating exhaust gas as much as possible.
 上記課題を解決するために、本発明の船舶は以下の手段を採用する。
 すなわち、本発明にかかる船舶は、船舶推進用の内燃機関本体と、該内燃機関本体からの排気ガスによって駆動されるタービン、及び、該タービンに連結されるとともに吸気を圧縮するコンプレッサを有する過給機と、前記内燃機関本体からの排気ガスが導かれる排気ガス経路と、前記排気ガス経路の分岐点から分岐され、排気ガスの一部を前記内燃機関本体の吸気経路に導くEGR経路と、該EGR経路に設けられ、ベンチュリスクラバとされたEGR排気ガス洗浄装置とを備えている。
In order to solve the above problems, the ship of the present invention employs the following means.
That is, a ship according to the present invention is a supercharger having an internal combustion engine body for propulsion of a ship, a turbine driven by exhaust gas from the internal combustion engine body, and a compressor connected to the turbine and compressing intake air. An exhaust gas path through which exhaust gas from the internal combustion engine body is guided, an EGR path branched from a branch point of the exhaust gas path, and leading a part of the exhaust gas to the intake path of the internal combustion engine body, And an EGR exhaust gas cleaning device provided in the EGR path and serving as a venturi scrubber.
 発明者等が鋭意検討した結果、ベンチュリスクラバはPM等の不純物だけでなくSOxを除去する性能を有していることを見出した。そこで、EGR経路に設けられるEGR排気ガス洗浄装置としてベンチュリスクラバを採用することとした。これにより、EGR運転時にEGR経路にてPM等の不純物だけでなくSOxをも除去できる。
 EGR経路にベンチュリスクラバを設けることとしたので、ベンチュリスクラバによって生じる圧力損失を補う場合であってもEGR経路を流れる排気ガス量に応じた容量のEGRブロアを設ければ足り、内燃機関本体から排出される排気ガスの全量に対してブロアを設ける場合に比べてブロア容量を低減することができる。
 また、ベンチュリスクラバは、脱硫吸収塔といった一般のスクラバに比べてサイズが小さいので、設置スペースを可及的に削減することができる。また、ベンチュリスクラバを内燃機関本体の付属設備として内燃機関本体上に設置することができ、より一層コンパクトにすることができるとともに、船舶としての内燃機関本体の設置場所の設計を変更しなくて良いというメリットがある。
 なお、EGR経路は、過給機のタービンの上流側から分岐してよく(高圧EGR)、過給機のタービンの下流側から分岐してもよい(低圧EGR)。
As a result of intensive studies by the inventors, it has been found that the venturi scrubber has the ability to remove SOx as well as impurities such as PM. Therefore, a venturi scrubber was adopted as an EGR exhaust gas cleaning device provided in the EGR path. Thereby, not only impurities such as PM but also SOx can be removed through the EGR path during EGR operation.
Since a venturi scrubber is provided in the EGR path, it is sufficient to provide an EGR blower with a capacity corresponding to the amount of exhaust gas flowing through the EGR path, even if the pressure loss caused by the venturi scrubber is compensated. The blower capacity can be reduced as compared with the case where a blower is provided for the total amount of exhaust gas.
Further, the venturi scrubber is smaller in size than a general scrubber such as a desulfurization absorption tower, so that the installation space can be reduced as much as possible. Further, the venturi scrubber can be installed on the internal combustion engine main body as an accessory of the internal combustion engine main body, and can be made more compact, and the design of the installation location of the internal combustion engine main body as a ship need not be changed. There is a merit.
The EGR path may be branched from the upstream side of the turbocharger turbine (high pressure EGR), or may be branched from the downstream side of the turbocharger turbine (low pressure EGR).
 さらに、本発明の船舶では、前記タービンと前記分岐点の間、及び、前記分岐点と前記EGR排気ガス洗浄装置との間には、排気ガス中の硫黄酸化物を除去するための排気ガス洗浄装置が設けられていないこととしてもよい。 Further, in the ship of the present invention, exhaust gas cleaning for removing sulfur oxides in exhaust gas between the turbine and the branch point and between the branch point and the EGR exhaust gas cleaning device. The apparatus may not be provided.
 前記タービンと分岐点の間、及び、分岐点とEGR排気ガス洗浄装置との間、すなわちEGR排気ガス洗浄装置の上流側に、硫黄酸化物を除去するための脱硫吸収塔といった排気ガス洗浄装置が設けられていないので、設置スペースを削減することができる。
 また、EGR排気ガス洗浄装置の上流側に限らず、分岐点よりも下流側の排気ガス経路にも排気ガス洗浄装置を設けないこととしても良い。分岐点よりも下流側の排気ガス経路に排気ガス洗浄装置が設けられていなくても、EGR経路に設けたベンチュリスクラバにてSOxを除去できるので、再循環される排気ガスによって内燃機関本体の吸気経路において、低温部で硫酸となって凝縮することによる、いわゆる硫酸露点腐食を生じることがない。
An exhaust gas cleaning device such as a desulfurization absorption tower for removing sulfur oxide is provided between the turbine and the branch point, and between the branch point and the EGR exhaust gas cleaning device, that is, upstream of the EGR exhaust gas cleaning device. Since it is not provided, installation space can be reduced.
Moreover, it is good also as not providing an exhaust-gas cleaning apparatus not only in the upstream of an EGR exhaust-gas cleaning apparatus but in the exhaust-gas path | route downstream from a branch point. Even if the exhaust gas cleaning device is not provided in the exhaust gas path downstream of the branch point, the SOx can be removed by the venturi scrubber provided in the EGR path. In the path, so-called sulfuric acid dew point corrosion due to condensation as sulfuric acid in the low temperature portion does not occur.
 さらに、本発明の船舶では、前記排気ガス経路には、排気ガスから熱を回収する排熱回収装置が設けられ、前記EGR経路は、該排熱回収装置の上流側から分岐されている。 Further, in the ship of the present invention, the exhaust gas path is provided with an exhaust heat recovery device that recovers heat from the exhaust gas, and the EGR path is branched from the upstream side of the exhaust heat recovery device.
 排熱回収装置の上流側からEGR経路を分岐することとしたので、船舶の煙突近傍に配置している排熱回収装置の下流側から分岐する場合に比べて、配管の圧損を低減できるため、排気ガスの圧力を高く保ったままベンチュリスクラバとされたEGR排気ガス洗浄装置に排気ガスを導くことができる。これにより、EGRブロアの負荷を低減させることができ、ベンチュリスクラバを効率的に作動させることができる。また、内燃機関本体付近から分岐することができるため、EGR経路の配管長さを大幅に短くでき、より一層コンパクトにすることができる。 Since the EGR path is branched from the upstream side of the exhaust heat recovery device, the pressure loss of the piping can be reduced compared to the case of branching from the downstream side of the exhaust heat recovery device arranged near the chimney of the ship. The exhaust gas can be guided to the EGR exhaust gas cleaning device which is a venturi scrubber while keeping the pressure of the exhaust gas high. Thereby, the load of an EGR blower can be reduced and a venturi scrubber can be operated efficiently. Moreover, since it can branch from the internal combustion engine main body vicinity, the piping length of an EGR path | route can be shortened significantly and it can be made still more compact.
 さらに、本発明の船舶では、前記排気ガス経路に設けられ、排気ガスから熱を回収する排熱回収装置と、前記排気ガス経路であり、かつ前記排熱回収装置の下流に設けられ、排気ガス中の硫黄酸化物を除去するための排気ガス洗浄装置とを備え、前記EGR経路は、前記排熱回収装置および前記排気ガス洗浄装置の下流側から分岐される。 Further, in the ship of the present invention, an exhaust heat recovery device that is provided in the exhaust gas path and recovers heat from the exhaust gas, and is provided in the exhaust gas path and downstream of the exhaust heat recovery device, the exhaust gas An exhaust gas cleaning device for removing sulfur oxide therein, and the EGR path is branched from the downstream side of the exhaust heat recovery device and the exhaust gas cleaning device.
 排気ガス経路に設けられた排気ガス洗浄装置に加えて、さらにEGR経路にEGR排気ガス洗浄装置を設けることとした。これにより、排気ガス洗浄装置にて十分に除去されていない煤塵を主成分としたPM等の不純物およびSOxをEGR排気ガス洗浄装置にて確実に除去することができる。本構成においては排気ガス洗浄装置でSOxが除去されたのちにEGR排気ガス洗浄装置を通過するため、SOx除去効果をさらに高めることができる。
 また、EGR排気ガス洗浄装置は、大部分のSOxが除去された後の排気ガス中のPM等の不純物を除去することを主目的としているので、さらに小型化が可能となり内燃機関本体上に設置することができ、また装置に付随するユーティリティの低減が可能となる。
 なお、排気ガス洗浄装置としては、典型的には、脱硫吸収塔が挙げられる。
In addition to the exhaust gas cleaning device provided in the exhaust gas path, an EGR exhaust gas cleaning device is further provided in the EGR path. Thereby, impurities such as PM mainly composed of soot and dust that have not been sufficiently removed by the exhaust gas cleaning device and SOx can be reliably removed by the EGR exhaust gas cleaning device. In this configuration, since SOx is removed by the exhaust gas cleaning device and then passes through the EGR exhaust gas cleaning device, the SOx removal effect can be further enhanced.
The EGR exhaust gas cleaning device is mainly intended to remove impurities such as PM in the exhaust gas after most of the SOx is removed, so it can be further downsized and installed on the internal combustion engine body. In addition, the utility associated with the apparatus can be reduced.
An exhaust gas cleaning device typically includes a desulfurization absorption tower.
 さらに、本発明の船舶では、前記排気ガス洗浄装置は、水を散布するスクラバとされ、前記排気ガス洗浄装置および前記EGR排気ガス洗浄装置からの排水を処理する共通の排水処理装置を備えている。 Furthermore, in the ship according to the present invention, the exhaust gas cleaning device is a scrubber that sprays water, and includes a common waste water treatment device that processes waste water from the exhaust gas cleaning device and the EGR exhaust gas cleaning device. .
 スクラバとされた排気ガス処理装置およびベンチュリスクラバとされたEGR排気ガス処理装置からの排水を共通の排水処理装置で処理することとした。これにより、排水処理装置の設置スペースを省略でき効率的に排水処理を行うことができる。 The wastewater from the exhaust gas treatment device designated as a scrubber and the EGR exhaust gas treatment device designated as a venturi scrubber was treated by a common wastewater treatment device. Thereby, the installation space of a waste water treatment apparatus can be omitted and waste water treatment can be performed efficiently.
 さらに、本発明の船舶では、前記EGR経路は、前記コンプレッサの上流側に導かれることとしてもよい。または、前記EGR経路は、前記コンプレッサの下流側でかつ前記空気冷却器の上流側に導かれることとしてもよい。または、前記EGR経路は、前記空気冷却器の下流側に導かれることとしてもよい。 Furthermore, in the ship of the present invention, the EGR path may be led to the upstream side of the compressor. Alternatively, the EGR path may be led downstream of the compressor and upstream of the air cooler. Alternatively, the EGR path may be led to the downstream side of the air cooler.
 EGR経路に設けられるEGR排気ガス洗浄装置としてベンチュリスクラバを採用することとしたので、EGR運転時にEGR経路にてPM等の不純物だけでなくSOxをも十分に除去できる。これにより、過給機のコンプレッサや内燃機関本体に悪影響を及ぼすことがない。 Since the venturi scrubber is adopted as the EGR exhaust gas cleaning device provided in the EGR path, not only impurities such as PM but also SOx can be sufficiently removed in the EGR path during EGR operation. As a result, the compressor of the supercharger and the internal combustion engine main body are not adversely affected.
本発明の船舶の第1実施形態を示した概略構成図である。BRIEF DESCRIPTION OF THE DRAWINGS It is the schematic block diagram which showed 1st Embodiment of the ship of this invention. 本発明の船舶の第2実施形態を示した概略構成図である。It is the schematic block diagram which showed 2nd Embodiment of the ship of this invention.
[第1実施形態]
 以下に、本発明にかかる第1実施形態について、図1を参照して説明する。
 図1には、船舶に設けられたディーゼルエンジン(内燃機関)1まわりの概略構成が示されている。
 ディーゼルエンジン1は、船舶推進用の主機とされたディーゼルエンジン本体(以下、単に「エンジン本体」という。)3と、エンジン本体3からの排気ガスによって駆動される過給機5と、過給機5から導かれた排気ガスの一部がエンジン本体3へ再循環されて低圧EGRを行うEGRシステム7とを備えている。
[First Embodiment]
A first embodiment according to the present invention will be described below with reference to FIG.
FIG. 1 shows a schematic configuration around a diesel engine (internal combustion engine) 1 provided in a ship.
The diesel engine 1 includes a diesel engine main body (hereinafter simply referred to as an “engine main body”) 3 that is a main engine for marine propulsion, a supercharger 5 that is driven by exhaust gas from the engine main body 3, and a supercharger. 5 is provided with an EGR system 7 which performs a low pressure EGR by recirculating a part of the exhaust gas led from 5 to the engine body 3.
 エンジン本体3は、舶用2サイクルディーゼルエンジンとされており、例えば下方から給気して上方へ排気するように1方向に掃気されるユニフロー型が採用されている。エンジン本体3からの出力は、図示しないプロペラ軸を介してスクリュープロペラに直接的に接続されている。
 エンジン本体3の各気筒のシリンダ部9(図1では例示として4気筒のみを示している。)の排気ポートは排気ガス集合管としての排気静圧管11に接続されている。排気静圧管11は、第1排気経路L1を介して、過給機5のタービン5aの入口側と接続されている。
The engine body 3 is a marine two-cycle diesel engine, and for example, a uniflow type that is scavenged in one direction so as to supply air from below and exhaust upward is adopted. The output from the engine body 3 is directly connected to the screw propeller via a propeller shaft (not shown).
An exhaust port of a cylinder portion 9 (only four cylinders are shown as an example in FIG. 1) of each cylinder of the engine body 3 is connected to an exhaust static pressure tube 11 as an exhaust gas collecting tube. The exhaust static pressure pipe 11 is connected to the inlet side of the turbine 5a of the supercharger 5 via the first exhaust path L1.
 一方、各シリンダ部9の掃気ポートは掃気トランク13に接続されており、掃気トランク13は、掃気経路K1を介して、過給機5のコンプレッサ5bと接続されている。また、掃気経路K1にはインタークーラーとしての空気冷却器15が設置されている。 On the other hand, the scavenging port of each cylinder section 9 is connected to the scavenging trunk 13, and the scavenging trunk 13 is connected to the compressor 5b of the supercharger 5 through the scavenging path K1. An air cooler 15 as an intercooler is installed in the scavenging path K1.
 過給機5は、タービン5aと、コンプレッサ5bとを備えている。タービン5a及びコンプレッサ5bは、回転軸5cによって同軸にて連結されている。タービン5aは、エンジン本体3からの排気ガスによって駆動され、タービン5aにて得られたタービン仕事は回転軸5cを介してコンプレッサ5bに伝達される。コンプレッサ5bは、外気(空気)や外気と再循環ガスとの混合気を吸い込み所定の掃気圧まで昇圧する。 The supercharger 5 includes a turbine 5a and a compressor 5b. The turbine 5a and the compressor 5b are coaxially connected by a rotating shaft 5c. The turbine 5a is driven by exhaust gas from the engine body 3, and the turbine work obtained by the turbine 5a is transmitted to the compressor 5b through the rotating shaft 5c. The compressor 5b sucks outside air (air) or a mixture of outside air and recirculation gas and raises the pressure to a predetermined scavenging pressure.
 タービン5aにてタービン仕事を与えた後の排気ガスは、第2排気経路L2へと流出する。第2排気経路L2には、エコノマイザ(排熱回収装置)21が接続されている。エコノマイザ21は、エンジン本体3からの排気ガスによって蒸気を生成する。生成された蒸気は、船内の各所にて利用される。
 エコノマイザ21の上流側には分岐点17が設けられており、この分岐点17からEGR経路L3が分岐する。EGR経路L3には、EGRを行うためのEGR弁19が設けられている。EGR弁19は、図示しない制御部によって開度が調整されるようになっており、エンジン本体3がEGRを行う運転のときには全開となり、EGRを行わないときは全閉となる。但し、本実施形態に限らず、運転状態に応じてEGR弁19の弁開度を適宜調整する構成とすることもできる。
The exhaust gas after the turbine work is given by the turbine 5a flows out to the second exhaust path L2. An economizer (exhaust heat recovery device) 21 is connected to the second exhaust path L2. The economizer 21 generates steam by the exhaust gas from the engine body 3. The generated steam is used in various places on the ship.
A branch point 17 is provided on the upstream side of the economizer 21, and the EGR route L3 branches from the branch point 17. The EGR path L3 is provided with an EGR valve 19 for performing EGR. The opening degree of the EGR valve 19 is adjusted by a control unit (not shown). The EGR valve 19 is fully opened when the engine body 3 is operated to perform EGR, and is fully closed when EGR is not performed. However, the present invention is not limited to this embodiment, and the valve opening degree of the EGR valve 19 may be appropriately adjusted according to the operating state.
 EGR経路L3に設けられたEGR弁19の下流側には、ベンチュリスクラバ(EGR排気ガス洗浄装置)25が接続されている。
 ベンチュリスクラバ25は、EGR経路L3を流れる排気ガスに対して水等の液体を噴霧することによって排気ガス中に含まれているPM等の不純物だけでなくSOxをも除去する。ベンチュリスクラバ25は、エンジン本体3の近傍もしくはエンジン本体3上に設置されている。このような配置は、脱硫吸収塔といった一般のスクラバに比べてベンチュリスクラバ25はサイズが小さい(例えば、ベンチュリスクラバは一般的なスクラバと比較して直径がおよそ5分の1~2分の1、高さがおよそ3分の1~2分の1とされ、エンジン本体3に載置可能なサイズで構成される)ので可能となっている。
A venturi scrubber (EGR exhaust gas cleaning device) 25 is connected to the downstream side of the EGR valve 19 provided in the EGR path L3.
The venturi scrubber 25 removes not only impurities such as PM contained in the exhaust gas but also SOx by spraying a liquid such as water on the exhaust gas flowing through the EGR path L3. The venturi scrubber 25 is installed in the vicinity of the engine body 3 or on the engine body 3. In such an arrangement, the venturi scrubber 25 is smaller in size than a general scrubber such as a desulfurization absorption tower (for example, the venturi scrubber has a diameter of about 1/5 to 1/2 that of a general scrubber, This is possible because the height is about one-third to one-half and is configured to be mounted on the engine body 3).
 ベンチュリスクラバ25は、ベンチュリスクラバ本体25aと、ベンチュリスクラバ本体25aに接続された気液分離器25bとを備えている。
 ベンチュリスクラバ本体25aは、鉛直上方に設けられた上部大径部25cと、上部大径部25cの下方に設けられ流れ方向に流路断面積が漸次減少する縮小テーパ部25dと、縮小テーパ部25dの下方に設けられたスロート部25eと、スロート部25eの下方に設けられ流れ方向に流路断面積が漸次増大する拡大テーパ部25fと、拡大テーパ部25fの下方に設けられた下部大径部25gとを備えている。
 上部大径部25cには、スプレーノズル25hが設けられており、スプレーノズル25hから水や水溶液等の吸収液が縮小テーパ部25dとスロート部25eとの接続位置に向かって噴霧される。スプレーノズル25hから噴霧された吸収液は、ベンチュリスクラバ本体25aのスロート部25eにて排気ガスの流速が増大されることによって効果的に拡散および混合され、PM等の不純物だけでなくSOxをも除去する。
The venturi scrubber 25 includes a venturi scrubber main body 25a and a gas-liquid separator 25b connected to the venturi scrubber main body 25a.
The venturi scrubber main body 25a includes an upper large-diameter portion 25c provided vertically above, a reduced taper portion 25d provided below the upper large-diameter portion 25c, and having a flow path cross-sectional area gradually decreasing in the flow direction, and a reduced taper portion 25d. A throat portion 25e provided below, an enlarged taper portion 25f provided below the throat portion 25e and having a channel cross-sectional area gradually increasing in the flow direction, and a lower large diameter portion provided below the enlarged taper portion 25f. 25g.
The upper large-diameter portion 25c is provided with a spray nozzle 25h, and an absorbing liquid such as water or an aqueous solution is sprayed from the spray nozzle 25h toward the connection position between the reduced taper portion 25d and the throat portion 25e. The absorbing liquid sprayed from the spray nozzle 25h is effectively diffused and mixed by increasing the flow rate of the exhaust gas at the throat portion 25e of the venturi scrubber body 25a to remove not only impurities such as PM but also SOx. To do.
 気液分離器25bでは、ベンチュリスクラバ本体25aから導かれた排気ガス中に含まれる水分が除去される。気液分離器25bの出口には、排気ガス中に残存するミストを除去するミストセパレータ25iが設けられ、分離されたミストは気液分離器25b内に集められる。
 なお気液分離器25bとしては、ミストセパレータを用いた方式に代えて、排気ガスを旋回させて気液を分離させるサイクロン方式としてもよい。
In the gas-liquid separator 25b, moisture contained in the exhaust gas led from the venturi scrubber main body 25a is removed. A mist separator 25i for removing mist remaining in the exhaust gas is provided at the outlet of the gas-liquid separator 25b, and the separated mist is collected in the gas-liquid separator 25b.
The gas-liquid separator 25b may be a cyclone method in which the gas and liquid are separated by turning the exhaust gas instead of the method using a mist separator.
 気液分離器25bの下流側には、EGRブロア27が設けられている。EGRブロア27は、インバータにより周波数可変とされた電動モータ29によって回転駆動される。EGRブロア27は、EGRバルブ19及びベンチュリスクラバ25を通りEGR経路L3を構成する配管を流れる際に生じる排気ガスの圧力損失を補うように用いられる。 An EGR blower 27 is provided on the downstream side of the gas-liquid separator 25b. The EGR blower 27 is rotationally driven by an electric motor 29 whose frequency is variable by an inverter. The EGR blower 27 is used to compensate for the pressure loss of the exhaust gas that is generated when the EGR valve 19 and the venturi scrubber 25 pass through the piping constituting the EGR path L3.
 EGRブロア27の下流側には、ミキサ39が設けられている。ミキサ39にて、再循環する排気ガスと空気とが混合される。ミキサ39にて混合された混合ガス(EGRが行われない場合は空気のみ)は、給気経路K2を通りコンプレッサ5bの吸込口へと導かれる。さらに、図示しないEGR冷却器をEGR経路上に設けても良い。この場合、例えばEGR冷却器はEGRブロアの下流側に設置される。 A mixer 39 is provided on the downstream side of the EGR blower 27. In the mixer 39, the recirculated exhaust gas and air are mixed. The mixed gas (only air when EGR is not performed) mixed in the mixer 39 is guided to the suction port of the compressor 5b through the air supply path K2. Further, an EGR cooler (not shown) may be provided on the EGR path. In this case, for example, the EGR cooler is installed downstream of the EGR blower.
 次に、上記構成のディーゼルエンジン1を備えた船舶の動作について説明する。
 船舶が排気ガスのNOx規制が厳格とされている海域(排気ガス規制海域(Emission
Control Area;ECA))を航行する際のようにEGRを使用する場合には、EGR弁19を開とする。これにより、エンジン本体3から第1排気経路L1を通りタービン5aへと導かれた排気ガスがエコノマイザ21を通過する前に、分岐点17で分岐されてEGRシステム7側に流れる。残部の排気ガスは、第2排気経路L2を流れ、エコノマイザ21を通過した後に図示しない煙突から大気へと放出される。
Next, operation | movement of the ship provided with the diesel engine 1 of the said structure is demonstrated.
Marine areas where exhaust gas NOx regulations are considered strict (emission regulations)
When using EGR as in navigating the Control Area (ECA)), the EGR valve 19 is opened. As a result, the exhaust gas guided from the engine body 3 to the turbine 5a through the first exhaust path L1 is branched at the branch point 17 and flows toward the EGR system 7 before passing through the economizer 21. The remaining exhaust gas flows through the second exhaust path L2, passes through the economizer 21, and is discharged from a chimney (not shown) to the atmosphere.
 EGRシステム7を流れる排気ガスは再循環ガスとして、EGR弁19を通りベンチュリスクラバ25を流れる。ベンチュリスクラバ25にてPM等の不純物だけでなくSOxが除去された排気ガスがEGRブロア27へと導かれ、EGRブロア27にて所定圧まで加圧された排気ガスがミキサ39へと導かれる。ミキサ39では、空気と排気ガスが混合され、吸気経路K2を通りコンプレッサ5bの吸込口へと導かれる。コンプレッサ5bで加圧された空気と排気ガスの混合気は、掃気経路K1を通り空気冷却器15へと導かれ、空気冷却器15にて冷却された後に掃気トランク13へと導かれる。 The exhaust gas flowing through the EGR system 7 flows as a recirculation gas through the EGR valve 19 and through the venturi scrubber 25. The exhaust gas from which not only impurities such as PM but also SOx is removed by the venturi scrubber 25 is guided to the EGR blower 27, and the exhaust gas pressurized to a predetermined pressure by the EGR blower 27 is guided to the mixer 39. In the mixer 39, the air and the exhaust gas are mixed and guided to the intake port of the compressor 5b through the intake path K2. The mixture of air and exhaust gas pressurized by the compressor 5b is guided to the air cooler 15 through the scavenging path K1, cooled by the air cooler 15, and then guided to the scavenging trunk 13.
 以下に、ベンチュリスクラバによってSOxが除去されることを確認した試験結果について説明する。上述したように、ベンチュリスクラバは、一般に、流速を増大させて吸収液の拡散を高めることによってPM等の不純物を効果的に除去するものとして知られているが、SOxの除去についても効果があることを新たに見出した。
 下記の表1には、ベンチュリスクラバ入口における排気ガスの組成が示されており、表2には、ベンチュリスクラバ出口における排気ガスの組成が示されている。各表において、No.1からNo.8は、各サンプリングの試験番号を示し、全数で8回のサンプリングを行った。
 試験に用いたベンチュリスクラバは、スロート部における最大ガス流速50~80m/s、液ガス比(吸収液の噴霧量[kg]/標準状態換算のガス流量[Nm3])0.5~2.0kg/Nm3の仕様のものを用いた。ベンチュリスクラバのノズルは一流体ノズルを用い、噴霧角度は80~100°とした。
 試験に用いた排気ガスは、舶用2サイクルディーゼルエンジンの実際の排気ガスを用いた。燃料はA重油を用い、A重油中の硫黄分は0.71wt%であった。エンジン回転数は定格回転数である105rpmとした。ガスの性状分析は、(株)堀場製作所のガス分析計PG-250を用い、NOxは常圧化学発光法にて、SOxとCO2は非分散型赤外線吸収法にて、またO2はジルコニア酸素分析計にて計測を行った。
Below, the test result which confirmed that SOx was removed by a venturi scrubber is demonstrated. As described above, the venturi scrubber is generally known to effectively remove impurities such as PM by increasing the flow rate and enhancing the diffusion of the absorption liquid, but it is also effective for removing SOx. I found a new thing.
Table 1 below shows the composition of the exhaust gas at the venturi scrubber inlet, and Table 2 shows the composition of the exhaust gas at the venturi scrubber outlet. In each table, No. 1 to No. 8 indicate the test number of each sampling, and sampling was performed 8 times in total.
The venturi scrubber used in the test has a maximum gas flow rate of 50 to 80 m / s at the throat and a liquid gas ratio (absorbed liquid spray amount [kg] / standard state converted gas flow rate [Nm3]) of 0.5 to 2.0 kg / Nm3. The specification was used. The venturi scrubber nozzle used a one-fluid nozzle, and the spray angle was 80-100 °.
The exhaust gas used for the test was the actual exhaust gas of a marine two-cycle diesel engine. The fuel used was A heavy oil, and the sulfur content in the A heavy oil was 0.71 wt%. The engine speed was 105 rpm, which is the rated speed. Gas properties are analyzed using a gas analyzer PG-250 manufactured by HORIBA, Ltd. NOx is analyzed by atmospheric pressure chemiluminescence, SOx and CO2 are analyzed by non-dispersive infrared absorption method, and O2 is analyzed by zirconia oxygen. Measurement was performed with a meter.
Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000002
Figure JPOXMLDOC01-appb-T000002
 上記の試験結果から、ベンチュリスクラバは、SOxを大幅に除去することができることが分かる。特に、NOx、CO2及びO2については有意な除去ができないにも関わらず、SOxのみについて除去できるという点は、従来では知られていない新たな知見である。 From the above test results, it can be seen that the venturi scrubber can significantly remove SOx. In particular, the fact that NOx, CO2, and O2 cannot be removed significantly but only SOx can be removed is a new finding that has not been conventionally known.
 以上の通り、本実施形態のディーゼルエンジン1を備えた船舶によれば、以下の作用効果を奏する。
 EGR経路に設けられるEGR排気ガス洗浄装置としてベンチュリスクラバ25を採用することとしたので、EGR運転時にEGR経路L3にてPM等の不純物だけでなくSOxをも除去できる。これにより、コンプレッサ5bやエンジン本体3に悪影響を及ぼすことがない。
 EGR経路L3にベンチュリスクラバ25を設けることとしたので、ベンチュリスクラバ25によって生じる圧力損失を補う場合であってもEGR経路L3を流れる排気ガス量に応じた容量のEGRブロア27を設ければ足り、エンジン本体3から排出される排気ガスの全量に対してブロアを設ける場合に比べてブロア容量を低減することができる。
 また、ベンチュリスクラバ25は、脱硫吸収塔といった一般のスクラバに比べてサイズが小さいので、設置スペースを削減することができる。また、ベンチュリスクラバ25をエンジン本体3の付属設備としてエンジン本体3上に設置することができ、より一層コンパクトにすることができるとともに、船舶としてのエンジン本体3の設置場所の設計を変更しなくて良いメリットがある。
As mentioned above, according to the ship provided with the diesel engine 1 of this embodiment, there exist the following effects.
Since the venturi scrubber 25 is adopted as the EGR exhaust gas cleaning device provided in the EGR path, not only impurities such as PM but also SOx can be removed in the EGR path L3 during the EGR operation. Thereby, the compressor 5b and the engine main body 3 are not adversely affected.
Since the venturi scrubber 25 is provided in the EGR path L3, it is sufficient to provide the EGR blower 27 having a capacity corresponding to the amount of exhaust gas flowing through the EGR path L3 even when the pressure loss caused by the venturi scrubber 25 is compensated. The blower capacity can be reduced as compared with the case where the blower is provided for the entire amount of exhaust gas discharged from the engine body 3.
Moreover, since the venturi scrubber 25 is smaller in size than a general scrubber such as a desulfurization absorption tower, the installation space can be reduced. In addition, the venturi scrubber 25 can be installed on the engine body 3 as an accessory of the engine body 3 and can be made more compact, and the design of the installation location of the engine body 3 as a ship can be changed. There are good benefits.
 排気ガス経路である第2排気経路L2に、硫黄酸化物を除去するための排気ガス洗浄装置が設けられていないので、設置スペースを削減することができる。
 また、第2排気経路L2に排気ガス洗浄装置が設けられていなくても、EGR経路L3に設けたベンチュリスクラバ25にてSOxを除去できるので、再循環される排気ガスによってエンジン本体3の吸気経路において、低温部で硫酸となって凝縮することによる、いわゆる硫酸露点腐食を生じることがない。
Since an exhaust gas cleaning device for removing sulfur oxides is not provided in the second exhaust path L2, which is an exhaust gas path, installation space can be reduced.
Further, even if no exhaust gas cleaning device is provided in the second exhaust path L2, SOx can be removed by the venturi scrubber 25 provided in the EGR path L3, so that the intake path of the engine body 3 is recirculated by the exhaust gas. In this case, so-called sulfuric acid dew point corrosion is not caused by condensation as sulfuric acid at a low temperature part.
 エコノマイザ21の上流側からEGR経路L3を分岐することとしたので、船舶の煙突近傍に配置しているエコノマイザ21の下流側から分岐する場合に比べて、配管の圧損を低減できるため、排気ガスの圧力を高く保ったままベンチュリスクラバ25に排気ガスを導くことができる。これにより、EGRブロア27の負荷を低減させることができ、ベンチュリスクラバ25を効率的に作動させることができる。また、エンジン本体3付近から分岐することができるため、EGR経路L3の配管長さを大幅に短くでき、より一層コンパクトにすることができる。 Since the EGR path L3 is branched from the upstream side of the economizer 21, the pressure loss of the piping can be reduced as compared with the case of branching from the downstream side of the economizer 21 arranged in the vicinity of the chimney of the ship. The exhaust gas can be guided to the venturi scrubber 25 while keeping the pressure high. Thereby, the load of the EGR blower 27 can be reduced, and the venturi scrubber 25 can be operated efficiently. Moreover, since it can branch from the engine main body 3 vicinity, the piping length of the EGR path | route L3 can be shortened significantly, and it can be made still more compact.
[第2実施形態]
 次に、本発明の船舶に係る第2実施形態について説明する。本実施形態は、第1実施形態に対して、第2排気経路L2に脱硫吸収塔23を備えている点で相違する。その他の共通する構成については、同一符号を用いてその説明を省略する。
[Second Embodiment]
Next, a second embodiment according to the ship of the present invention will be described. This embodiment is different from the first embodiment in that a desulfurization absorption tower 23 is provided in the second exhaust path L2. Other common configurations are denoted by the same reference numerals and description thereof is omitted.
 第2排気経路L2には、エコノマイザ(排熱回収装置)21と脱硫吸収塔(排気ガス洗浄装置)23が順に接続されている。
 脱硫吸収塔23は、例えば充填塔式スクラバとされ、排気ガスに対して水や水溶液等の吸収液を噴霧することによって排気ガス中に含まれているSOxを除去する。なお、後述するが、EGR経路L3に導かれる排気ガスは、脱硫吸収塔23を通過した後に導かれるので、SOxについては十分に除去されており、ベンチュリスクラバ25では主としてPM等の不純物と残存するSOxの除去が行われる。
 なお、脱硫吸収塔23は、エンジン本体3の燃料としてSOx規制海域における規制値以上のS分(例えば1.0%以上)の硫黄分を含む燃料が用いられるときに適用される。
An economizer (exhaust heat recovery device) 21 and a desulfurization absorption tower (exhaust gas cleaning device) 23 are sequentially connected to the second exhaust path L2.
The desulfurization absorption tower 23 is a packed tower type scrubber, for example, and removes SOx contained in the exhaust gas by spraying an absorption liquid such as water or an aqueous solution to the exhaust gas. As will be described later, since the exhaust gas guided to the EGR path L3 is guided after passing through the desulfurization absorption tower 23, SOx is sufficiently removed, and the venturi scrubber 25 mainly remains with impurities such as PM. SOx removal is performed.
The desulfurization absorption tower 23 is applied when a fuel containing a sulfur content equal to or greater than the regulation value in the SOx regulation sea area (for example, 1.0% or more) is used as the fuel for the engine body 3.
 脱硫吸収塔23の下流側には分岐点17’が設けられており、この分岐点17’からEGR経路L3が分岐する。EGR経路L3に、EGR弁19、ベンチュリスクラバ25、EGRブロア27が設けられている点は第1実施形態と同様である。
 ベンチュリスクラバ25からの排水は、上述の脱硫吸収塔23と同じ排水処理装置(図示せず)で処理されるようになっている。すなわち、脱硫吸収塔23およびベンチュリスクラバ25からの排水を共通の排水処理装置で処理する。
A branch point 17 ′ is provided on the downstream side of the desulfurization absorption tower 23, and the EGR path L 3 branches from this branch point 17 ′. The point that the EGR valve 19, the venturi scrubber 25, and the EGR blower 27 are provided in the EGR path L3 is the same as in the first embodiment.
Waste water from the venturi scrubber 25 is treated by the same waste water treatment device (not shown) as the desulfurization absorption tower 23 described above. That is, waste water from the desulfurization absorption tower 23 and the venturi scrubber 25 is processed by a common waste water treatment device.
 次に、上記構成のディーゼルエンジン1を備えた船舶の動作について説明する。
 船舶が排気ガスのNOx規制が厳格とされている海域(排気ガス規制海域(Emission
Control Area;ECA))を航行する際のようにEGRを使用する場合には、EGR弁19を開とする。これにより、エンジン本体3から第1排気経路L1を通りタービン5aへと導かれた排気ガスがエコノマイザ21及び脱硫吸収塔23を通過した後に、分岐点17’で分岐されてEGRシステム7側に流れる。残部の排気ガスは、第2排気経路L2を流れ、図示しない煙突から大気へと放出される。
Next, operation | movement of the ship provided with the diesel engine 1 of the said structure is demonstrated.
Marine areas where exhaust gas NOx regulations are considered strict (emission regulations)
When using EGR as in navigating the Control Area (ECA)), the EGR valve 19 is opened. Thus, after the exhaust gas guided from the engine body 3 to the turbine 5a through the first exhaust path L1 passes through the economizer 21 and the desulfurization absorption tower 23, it is branched at the branch point 17 ′ and flows to the EGR system 7 side. . The remaining exhaust gas flows through the second exhaust path L2, and is discharged from a chimney (not shown) to the atmosphere.
 EGRシステム7を流れる排気ガスは再循環ガスとして、EGR弁19を通りベンチュリスクラバ25を流れる。ベンチュリスクラバ25にて、PM等の不純物と、脱硫吸収塔23にて除去されなかったSOxが除去される。ベンチュリスクラバ25を通過した排気ガスがEGRブロア27へと導かれ、EGRブロア27にて所定圧まで加圧された排気ガスがミキサ39へと導かれる。ミキサ39では、空気と排気ガスが混合され、吸気経路K2を通りコンプレッサ5bの吸込口へと導かれる。コンプレッサ5bで加圧された空気と排気ガスの混合気は、掃気経路K1を通り空気冷却器15へと導かれ、空気冷却器15にて冷却された後に掃気トランク13へと導かれる。 The exhaust gas flowing through the EGR system 7 flows as a recirculation gas through the EGR valve 19 and through the venturi scrubber 25. The venturi scrubber 25 removes impurities such as PM and SOx that has not been removed by the desulfurization absorption tower 23. The exhaust gas that has passed through the venturi scrubber 25 is guided to the EGR blower 27, and the exhaust gas pressurized to a predetermined pressure by the EGR blower 27 is guided to the mixer 39. In the mixer 39, the air and the exhaust gas are mixed and guided to the intake port of the compressor 5b through the intake path K2. The mixture of air and exhaust gas pressurized by the compressor 5b is guided to the air cooler 15 through the scavenging path K1, cooled by the air cooler 15, and then guided to the scavenging trunk 13.
 以上の通り、本実施形態のディーゼルエンジン1を備えた船舶によれば、以下の作用効果を奏する。
 第2排気経路L2に設けられた脱硫吸収塔23に加えて、さらにEGR経路L3にベンチュリスクラバ25を設けることとした。これにより、脱硫吸収塔23にて十分に除去されていないPM等の不純物および残存するSOxをベンチュリスクラバ25にて確実に除去することができる。これにより、コンプレッサ5bやエンジン本体3に悪影響を及ぼすことがない。
 また、ベンチュリスクラバ25は、脱硫吸収塔23を通過した後の排気ガス中のPM等の不純物と残存するSOxの除去を主目的としているので、第1実施形態のベンチュリスクラバに比べてさらに小型化が可能となり、また装置に付随するユーティリティの低減が可能となる。
As mentioned above, according to the ship provided with the diesel engine 1 of this embodiment, there exist the following effects.
In addition to the desulfurization absorption tower 23 provided in the second exhaust path L2, a venturi scrubber 25 is further provided in the EGR path L3. Thereby, impurities such as PM that have not been sufficiently removed by the desulfurization absorption tower 23 and the remaining SOx can be reliably removed by the venturi scrubber 25. Thereby, the compressor 5b and the engine main body 3 are not adversely affected.
Further, the venturi scrubber 25 mainly aims to remove impurities such as PM and remaining SOx in the exhaust gas after passing through the desulfurization absorption tower 23, so that it is further downsized compared to the venturi scrubber of the first embodiment. In addition, it is possible to reduce the utility associated with the apparatus.
 脱硫吸収塔23およびベンチュリスクラバ25からの排水を共通の排水処理装置で処理することとした。これにより、排水処理装置の設置スペースを省略でき効率的に排水処理を行うことができる。 The wastewater from the desulfurization absorption tower 23 and the venturi scrubber 25 was treated with a common wastewater treatment device. Thereby, the installation space of a waste water treatment apparatus can be omitted and waste water treatment can be performed efficiently.
 エコノマイザ21の下流側の分岐点17’から分岐してEGRを行うこととし、EGRを行うか否かに関わらずエコノマイザ21を全量の排気ガスが通過することとしたので、エコノマイザ21による排熱回収が無駄なく有効に行われる。
 また、脱硫吸収塔23の下流側の分岐点17’から分岐してEGRを行うこととしたので、EGRを行うか否かに関わらず脱硫吸収塔23を通過するので、EGR率に応じて脱硫吸収塔23を制御する必要がない。
 また、全量の排気ガスが脱硫吸収塔23を通過するので、SOx規制海域を船舶が航行する場合でも割高な低S分燃料(例えば硫黄分が1.0%以下)を使用する必要がない。
Since the EGR is performed by branching from the branch point 17 ′ on the downstream side of the economizer 21 and the exhaust gas of the entire amount passes through the economizer 21 regardless of whether the EGR is performed or not, the exhaust heat recovery by the economizer 21 is performed. Is effectively done without waste.
Further, since the EGR is performed by branching from the branch point 17 ′ on the downstream side of the desulfurization absorption tower 23, the desulfurization absorption tower 23 is passed regardless of whether or not the EGR is performed. Therefore, the desulfurization is performed according to the EGR rate. There is no need to control the absorption tower 23.
Further, since the entire amount of exhaust gas passes through the desulfurization absorption tower 23, it is not necessary to use expensive low S component fuel (for example, sulfur content is 1.0% or less) even when a ship navigates the SOx restricted sea area.
 脱硫吸収塔23を通過して冷却された後の排気ガスをEGR弁19およびベンチュリスクラバ25へと導くこととしたので、EGR弁19およびベンチュリスクラバ25の構成部品として耐高温部材を使わなくても良い。さらには、排気ガス温度が低いので排気ガス中に含まれる水蒸気を少なくできるとともに、ミスト径を大きくすることができ、ミストセパレータ25iでのミスト回収率を増大させることができる。これにより、EGRブロア27の翼やコンプレッサ5bの翼の保護ができ、メンテナンス周期を長くできる。 Since the exhaust gas after passing through the desulfurization absorption tower 23 and being cooled is guided to the EGR valve 19 and the venturi scrubber 25, high temperature resistant members are not used as components of the EGR valve 19 and the venturi scrubber 25. good. Furthermore, since the exhaust gas temperature is low, water vapor contained in the exhaust gas can be reduced, the mist diameter can be increased, and the mist recovery rate at the mist separator 25i can be increased. Thereby, the blades of the EGR blower 27 and the blades of the compressor 5b can be protected, and the maintenance cycle can be lengthened.
 また、過給機5のタービン5aの直後から分岐して排気ガスを再循環するのではなく、脱硫吸収塔23の下流側の分岐点17’から排気ガスの再循環を行うこととし、EGR経路を長くすることとした。これにより、EGR経路L3を排気ガスが流通する間に脱硫吸収塔23から随伴するミストや蒸気を除去することができ、EGRブロア27の翼やコンプレッサ5bの翼の保護ができ、メンテナンス周期をさらに長くできる。 Further, the exhaust gas is not recirculated by branching immediately after the turbine 5a of the supercharger 5, but the exhaust gas is recirculated from the branch point 17 ′ on the downstream side of the desulfurization absorption tower 23, and the EGR path It was decided to make it longer. As a result, the mist and steam accompanying the desulfurization absorption tower 23 can be removed while the exhaust gas flows through the EGR path L3, the blades of the EGR blower 27 and the blades of the compressor 5b can be protected, and the maintenance cycle is further increased. Can be long.
 なお、上述した各実施形態では、EGR経路L3をタービン5aの下流側から分岐する低圧EGRを前提として説明したが、本発明はこれに限定されるものではなく、例えば、タービン5aの上流側の第1排気経路L1から分岐する高圧EGRとしてもよい。
 また、上述した各実施形態では、EGR経路L3の下流側の接続先をコンプレッサ5bの上流側としたが、本発明はこれに限定されるものではなく、例えば、コンプレッサ5bの下流側でかつ空気冷却器15の上流側にEGR経路L3の下流側を接続してもよく、または、空気冷却器15の下流側にEGR経路L3の下流側を接続してもよい。
 また、図2に示した第2実施形態では、分岐点17’を脱硫吸収塔23の下流側の位置としたが、エコノマイザ21の上流側としてもよく、また、エコノマイザ21と脱硫吸収塔23との間としてもよい。
In the above-described embodiments, the low-pressure EGR that branches the EGR path L3 from the downstream side of the turbine 5a has been described. However, the present invention is not limited to this, for example, the upstream side of the turbine 5a. It may be a high pressure EGR branched from the first exhaust path L1.
Further, in each of the above-described embodiments, the downstream side of the EGR path L3 is the upstream side of the compressor 5b. However, the present invention is not limited to this. For example, the downstream side of the compressor 5b and the air The downstream side of the EGR path L3 may be connected to the upstream side of the cooler 15, or the downstream side of the EGR path L3 may be connected to the downstream side of the air cooler 15.
In the second embodiment shown in FIG. 2, the branch point 17 ′ is positioned downstream of the desulfurization absorption tower 23, but may be upstream of the economizer 21, and the economizer 21 and the desulfurization absorption tower 23 It may be between.
1 ディーゼルエンジン(内燃機関)
3 エンジン本体(内燃機関本体)
5 過給機
5a タービン
5b コンプレッサ
7 EGRシステム
11 排気静圧管
13 掃気トランク
15 空気冷却器
19 EGR弁
21 エコノマイザ(排熱回収装置)
23 脱硫吸収塔(排気ガス洗浄装置)
25 ベンチュリスクラバ(EGR排気ガス洗浄装置)
27 EGRブロア
L1 第1排気経路
L2 第2排気経路
L3 EGR経路
K1 掃気経路
1 Diesel engine (internal combustion engine)
3 Engine body (Internal combustion engine body)
5 Supercharger 5a Turbine 5b Compressor 7 EGR system 11 Exhaust static pressure pipe 13 Scavenging trunk 15 Air cooler 19 EGR valve 21 Economizer (exhaust heat recovery device)
23 Desulfurization absorption tower (exhaust gas cleaning device)
25 Venturi scrubber (EGR exhaust gas cleaning device)
27 EGR blower L1 First exhaust path L2 Second exhaust path L3 EGR path K1 Scavenging path

Claims (8)

  1.  船舶推進用の内燃機関本体と、
     該内燃機関本体からの排気ガスによって駆動されるタービン、及び、該タービンに連結されるとともに吸気を圧縮するコンプレッサを有する過給機と、
     前記内燃機関本体からの排気ガスが導かれる排気ガス経路と、
     前記排気ガス経路の分岐点から分岐され、排気ガスの一部を前記内燃機関本体の吸気経路に導くEGR経路と、
     該EGR経路に設けられ、ベンチュリスクラバとされたEGR排気ガス洗浄装置と、
    を備えている船舶。
    An internal combustion engine body for ship propulsion,
    A turbine driven by exhaust gas from the internal combustion engine body, and a supercharger having a compressor coupled to the turbine and compressing intake air;
    An exhaust gas path through which exhaust gas from the internal combustion engine body is guided;
    An EGR path branched from a branch point of the exhaust gas path and guiding a part of the exhaust gas to the intake path of the internal combustion engine body;
    An EGR exhaust gas cleaning device provided in the EGR path and serving as a venturi scrubber;
    Ship equipped with.
  2.  前記タービンと前記分岐点の間、及び、前記分岐点と前記EGR排気ガス洗浄装置との間には、排気ガス中の硫黄酸化物を除去するための排気ガス洗浄装置が設けられていない請求項1に記載の船舶。 An exhaust gas cleaning device for removing sulfur oxide in the exhaust gas is not provided between the turbine and the branch point and between the branch point and the EGR exhaust gas cleaning device. The ship according to 1.
  3.  前記排気ガス経路には、排気ガスから熱を回収する排熱回収装置が設けられ、
     前記EGR経路は、該排熱回収装置の上流側から分岐されている請求項1または2に記載の船舶。
    The exhaust gas path is provided with an exhaust heat recovery device that recovers heat from the exhaust gas,
    The ship according to claim 1 or 2, wherein the EGR path is branched from an upstream side of the exhaust heat recovery apparatus.
  4.  前記排気ガス経路に設けられ、排気ガスから熱を回収する排熱回収装置と、
     前記排気ガス経路に設けられ、排気ガス中の硫黄酸化物を除去するための排気ガス洗浄装置と、
    を備え、
     前記EGR経路は、前記排熱回収装置および前記排気ガス洗浄装置の下流側から分岐される請求項1に記載の船舶。
    An exhaust heat recovery device that is provided in the exhaust gas path and recovers heat from the exhaust gas;
    An exhaust gas cleaning device provided in the exhaust gas path for removing sulfur oxides in the exhaust gas;
    With
    The ship according to claim 1, wherein the EGR path is branched from a downstream side of the exhaust heat recovery device and the exhaust gas cleaning device.
  5.  前記排気ガス洗浄装置は、水を散布するスクラバとされ、
     前記排気ガス洗浄装置および前記EGR排気ガス洗浄装置からの排水を処理する共通の排水処理装置を備えている請求項4に記載の船舶。
    The exhaust gas cleaning device is a scrubber that sprays water,
    The marine vessel according to claim 4, comprising a common waste water treatment device for treating waste water from the exhaust gas cleaning device and the EGR exhaust gas cleaning device.
  6.  前記EGR経路は、前記コンプレッサの上流側に導かれる請求項1から5のいずれかに記載の船舶。 The ship according to any one of claims 1 to 5, wherein the EGR path is led to an upstream side of the compressor.
  7.  前記コンプレッサの下流には、該コンプレッサによって圧縮された圧縮空気を冷却する空気冷却器が設けられ、
     前記EGR経路は、前記コンプレッサの下流側でかつ前記空気冷却器の上流側に導かれる請求項1から5のいずれかに記載の船舶。
    An air cooler for cooling the compressed air compressed by the compressor is provided downstream of the compressor,
    The marine vessel according to any one of claims 1 to 5, wherein the EGR path is led downstream of the compressor and upstream of the air cooler.
  8.  前記コンプレッサの下流には、該コンプレッサによって圧縮された圧縮空気を冷却する空気冷却器が設けられ、
     前記EGR経路は、前記空気冷却器の下流側に導かれる請求項1から5のいずれかに記載の船舶。
    An air cooler for cooling the compressed air compressed by the compressor is provided downstream of the compressor,
    The ship according to any one of claims 1 to 5, wherein the EGR path is led to a downstream side of the air cooler.
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Cited By (2)

* Cited by examiner, † Cited by third party
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CN107427776A (en) * 2015-03-13 2017-12-01 三菱重工业株式会社 Supply tank, emission-control equipment, ship
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* Cited by examiner, † Cited by third party
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JP2016151196A (en) * 2015-02-16 2016-08-22 三菱重工業株式会社 Exhaust gas recirculation system and marine engine mounted with the same
JP6109983B1 (en) * 2016-03-04 2017-04-05 三菱重工業株式会社 EGR system
JP6633944B2 (en) * 2016-03-07 2020-01-22 川崎重工業株式会社 Engine system and control method
CN108252830A (en) * 2016-12-28 2018-07-06 沪东重机有限公司 A kind of boat diesel engine exhaust gas method for recycling and device based on desulfurizing tower
KR102297868B1 (en) * 2017-03-14 2021-09-03 대우조선해양 주식회사 Integrated exhaust gas scrubbing system
KR20190026978A (en) * 2017-03-28 2019-03-13 미츠비시 히타치 파워 시스템즈 가부시키가이샤 Ship desulfurization device and ship
JP7058565B2 (en) * 2018-06-26 2022-04-22 三菱化工機株式会社 Solid component separator controller, solid component separator, marine exhaust gas scrubber system, and marine diesel engine
CN109026381A (en) * 2018-07-29 2018-12-18 合肥市智信汽车科技有限公司 A kind of haulage vehicle particle cleaning system
KR20240061821A (en) 2022-11-01 2024-05-08 주식회사 에스와이이노테크 Providing system for Training mental health care for pregnant

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06147028A (en) * 1992-11-06 1994-05-27 Yanmar Diesel Engine Co Ltd Diesel engine with exhaust gas reflux device
JPH11148335A (en) * 1997-11-14 1999-06-02 Ryuuki Engineering:Kk Wet type exhaust gas purification device
JP2002332919A (en) * 2001-02-26 2002-11-22 Mitsubishi Heavy Ind Ltd Exhaust gas recirculation system
JP2012047056A (en) * 2010-08-24 2012-03-08 Mitsubishi Heavy Ind Ltd Engine exhaust-gas cleaning device
JP2012172647A (en) * 2011-02-24 2012-09-10 Mitsui Eng & Shipbuild Co Ltd Exhaust heat recovery system of engine including turbocharger

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4825398Y1 (en) * 1968-03-12 1973-07-24
JPH08254160A (en) * 1995-03-16 1996-10-01 Kawasaki Heavy Ind Ltd Exhaust gas recirculation control device for diesel engine
US7445761B1 (en) * 2003-05-02 2008-11-04 Alexander Wade J Method and system for providing compressed substantially oxygen-free exhaust gas for industrial purposes
JP2007263078A (en) * 2006-03-29 2007-10-11 Mitsubishi Heavy Ind Ltd Emission gas treatment apparatus and method for marine vessel
US7861511B2 (en) * 2007-10-30 2011-01-04 General Electric Company System for recirculating the exhaust of a turbomachine
JP5101353B2 (en) * 2008-03-12 2012-12-19 三菱重工業株式会社 Tachometer sensor mounting structure
JP2009240908A (en) * 2008-03-31 2009-10-22 Babcock Hitachi Kk Wet two step flue gas desulfurization apparatus and operation method of wet two step flue gas desulfurization apparatus
JP5357720B2 (en) * 2009-11-27 2013-12-04 三菱重工業株式会社 Ships equipped with exhaust gas treatment equipment
JP4997336B2 (en) * 2010-01-29 2012-08-08 エムエーエヌ・ディーゼル・アンド・ターボ・フィリアル・アフ・エムエーエヌ・ディーゼル・アンド・ターボ・エスイー・ティスクランド Large two-cycle diesel engine with exhaust gas recirculation system
JP2012082720A (en) * 2010-10-07 2012-04-26 Mitsubishi Heavy Ind Ltd Control device of internal combustion engine
JP6041418B2 (en) * 2010-12-16 2016-12-07 臼井国際産業株式会社 Exhaust gas purification system for large-displacement marine diesel engines using low quality fuels below heavy oil

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06147028A (en) * 1992-11-06 1994-05-27 Yanmar Diesel Engine Co Ltd Diesel engine with exhaust gas reflux device
JPH11148335A (en) * 1997-11-14 1999-06-02 Ryuuki Engineering:Kk Wet type exhaust gas purification device
JP2002332919A (en) * 2001-02-26 2002-11-22 Mitsubishi Heavy Ind Ltd Exhaust gas recirculation system
JP2012047056A (en) * 2010-08-24 2012-03-08 Mitsubishi Heavy Ind Ltd Engine exhaust-gas cleaning device
JP2012172647A (en) * 2011-02-24 2012-09-10 Mitsui Eng & Shipbuild Co Ltd Exhaust heat recovery system of engine including turbocharger

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107427776A (en) * 2015-03-13 2017-12-01 三菱重工业株式会社 Supply tank, emission-control equipment, ship
CN107427775A (en) * 2015-03-13 2017-12-01 三菱重工业株式会社 Washer, emission-control equipment, ship
CN107427776B (en) * 2015-03-13 2021-01-01 三菱重工业株式会社 Water supply tank, exhaust gas treatment device, and ship
CN107427775B (en) * 2015-03-13 2021-03-16 三菱重工业株式会社 Scrubber, exhaust gas treatment device, and ship

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