WO2013078775A1 - Dual-conduit entropy-cycle engine - Google Patents

Dual-conduit entropy-cycle engine Download PDF

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Publication number
WO2013078775A1
WO2013078775A1 PCT/CN2012/001620 CN2012001620W WO2013078775A1 WO 2013078775 A1 WO2013078775 A1 WO 2013078775A1 CN 2012001620 W CN2012001620 W CN 2012001620W WO 2013078775 A1 WO2013078775 A1 WO 2013078775A1
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WO
WIPO (PCT)
Prior art keywords
working fluid
gas
cycle engine
piston
entropy cycle
Prior art date
Application number
PCT/CN2012/001620
Other languages
French (fr)
Chinese (zh)
Inventor
靳北彪
Original Assignee
Jin Beibiao
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Filing date
Publication date
Application filed by Jin Beibiao filed Critical Jin Beibiao
Publication of WO2013078775A1 publication Critical patent/WO2013078775A1/en

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02BINTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
    • F02B47/00Methods of operating engines involving adding non-fuel substances or anti-knock agents to combustion air, fuel, or fuel-air mixtures of engines
    • F02B47/04Methods of operating engines involving adding non-fuel substances or anti-knock agents to combustion air, fuel, or fuel-air mixtures of engines the substances being other than water or steam only
    • F02B47/08Methods of operating engines involving adding non-fuel substances or anti-knock agents to combustion air, fuel, or fuel-air mixtures of engines the substances being other than water or steam only the substances including exhaust gas
    • F02B47/10Circulation of exhaust gas in closed or semi-closed circuits, e.g. with simultaneous addition of oxygen
    • 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 invention relates to the field of thermal energy and power, and in particular to a hot air machine.
  • the invention provides a dual-channel entropy cycle engine with high power and high power density, which solves the problem that the temperature and pressure of the conventional heat engine are difficult to be heated to the proper height and affect the power and power density.
  • a dual-channel entropy cycle engine includes a piston gas compression mechanism, a piston gas work mechanism, and two communication passages, and a working fluid outlet of the piston gas compression mechanism passes through the communication passage and the piston a working gas inlet of the gas working mechanism is connected, and a working medium outlet of the piston gas working mechanism is connected to a working medium inlet of the piston gas compression mechanism via another communication passage; the piston gas compression mechanism is The two communication passages are connected to the piston gas working mechanism to form a working fluid closed circuit; an internal combustion combustion chamber is disposed in the working fluid closed circuit, and a working fluid outlet is disposed on the working fluid closed circuit.
  • the internal combustion combustion chamber is disposed at an outlet of the working fluid outlet of the piston type gas compression mechanism and a working outlet of the piston gas working mechanism.
  • the downstream working fluid is closed in the circuit.
  • the internal combustion combustion chamber is further set as a side internal combustion combustion chamber.
  • the dual-channel entropy cycle engine further includes a cooler, and the cooler is disposed on the working fluid closed circuit.
  • the dual-channel entropy cycle engine further includes a direct connection channel, and the direct connection channel communicates with the working fluid outlet of the piston gas working mechanism and the piston type a working fluid inlet of the compression mechanism, the cooler being disposed on the direct connection passage or the communication between the working fluid outlet of the piston gas working mechanism and the working fluid inlet of the piston gas compression mechanism
  • a control width is provided on the direct passage and on the communication passage between the working fluid outlet of the piston gas working mechanism and the working fluid inlet of the piston gas compression mechanism.
  • the two-channel entropy cycle engine further includes an oxidant source
  • the cooler is disposed at a working fluid outlet of the piston gas working mechanism and the piston gas Compression mechanism Said communication channel between said mass inlets, said oxidant source being in communication with said communication passage between said oxidant inlet and said cooler and said working inlet of said piston-type gas compression mechanism, said cooler
  • the communication passage between the oxidant inlet and the oxidant inlet is provided with a cooling liquid discharge port, and a liquid carbon dioxide outlet is provided on the communication passage between the oxidant inlet and the piston type gas compression mechanism.
  • the cooler is disposed upstream of the working fluid outlet of the piston gas working mechanism and downstream of the working fluid inlet of the internal combustion combustion chamber.
  • the working fluid is closed on the circuit.
  • the cooler is configured as a radiator, a gas-liquid direct mixing cooler, an adsorption refrigerator or a non-direct mixer cooler.
  • the dual-channel entropy cycle engine further includes an oxidant source, the oxidant source passing through the heated fluid passage of the non-direct-mixing cooler and the internal combustion chamber Connected.
  • a cryogenic liquid discharge port is provided on the non-direct mixer cooler.
  • the dual-channel entropy cycle engine further includes a cooling liquid discharge port, and the cooling liquid discharge port is disposed at The communication passage between the cooler and the working fluid outlet.
  • the dual-channel entropy cycle engine further includes an oxidant source, and the oxidant source is in communication with the working fluid closed loop.
  • the oxidant source is in communication with the internal combustion chamber.
  • the entropy cycle engine further includes a direct mixing condensing cooler, wherein the cooled fluid inlet of the direct mixing condensing cooler is in communication with the working fluid outlet.
  • the oxidant source is in communication with the heated fluid inlet of the direct mixing condensing cooler and is in communication with the working fluid closed circuit via the heated fluid outlet of the direct mixing condensing cooler.
  • the oxidant source is in communication with the internal combustion combustion chamber via a heated fluid outlet of the direct mixing condensing cooler.
  • the pressure of the oxidant source is greater than 2 MPa.
  • the working fluid outlet is disposed upstream of the working fluid outlet of the piston gas working mechanism (10) and the working fluid of the internal combustion combustion chamber The inlet is closed on the downstream working fluid.
  • the dual-channel entropy cycle engine further includes a non-direct-mixing condensing cooler, the cooled working fluid inlet of the non-direct-mixing condensing cooler and the working fluid The outlet is connected.
  • the direct mixing condensing cooler is provided with a cryogenic liquid discharge port.
  • the non-direct mixing condensing cooler is provided with a cryogenic liquid discharge port.
  • the dual channel entropy cycle engine also includes a cryogenic liquid working fluid storage tank in communication with the cryogenic liquid discharge port.
  • Scheme 22 Based on the scheme 14, further optionally, the direct mixing condensing cooler is provided with a non-condensing gas outlet.
  • Scheme 23 On the basis of the scheme 18, further optionally, the non-direct mixing condensing cooler is provided with a non-condensing gas outlet.
  • Scheme 24 On the basis of Option 22 or Scheme 23, further optionally, the non-condensable gas outlet is in communication with the closed circuit of the working fluid.
  • the entropy cycle engine further includes an oxidant source, the oxidant source being in communication with the internal combustion combustion chamber via a heated fluid passage of the non-direct mixing condensing cooler .
  • control valve is set to be pressure controlled, and the pressure control valve controls the pressure of the working fluid outlet in the closed loop of the working fluid to exceed a set value.
  • the working fluid is exported when the limit is reached.
  • the pressure control valve is controlled by a control mechanism that causes a minimum pressure in the working fluid closed circuit to be greater than 0.2 MPa.
  • control valve is controlled by an opening degree control mechanism, and the opening degree control mechanism controls the control valve according to a pressure setting range in the working fluid closed circuit.
  • the degree of opening allows the working fluid outlet to be in a normally open state at a certain degree of opening.
  • the dual-channel entropy cycle engine further includes an auxiliary gas working mechanism, and the working fluid outlet is connected to the working fluid inlet of the auxiliary gas working mechanism.
  • the two-channel entropy cycle engine further includes a gas storage tank, and the gas storage tank is in communication with the working fluid outlet.
  • Solution 32 On the basis of the solution 1, further optionally, a check valve is arranged on the communication passage.
  • the solution 33 is further selected, wherein the working fluid outlet of the piston gas working mechanism is upstream and the working fluid inlet of the piston gas compression mechanism is downstream.
  • Another piston gas working mechanism is arranged on the closed circuit.
  • the piston gas working mechanism further outputs power to the piston gas compression mechanism.
  • the solution 36 is further optional.
  • the dual-channel entropy cycle engine further includes a non-condensable storage tank, and the non-condensable storage tank is connected to the working fluid closed circuit via a control device.
  • the dual-channel entropy cycle engine further includes a non-condensable gas returning compressor, the air inlet of the non-condensing gas returning compressor and the working fluid
  • the closed loop is in communication
  • the gas outlet of the non-condensable gas returning compressor is in communication with the non-condensable gas storage tank.
  • a three-way catalyst is disposed in the closed loop of the working fluid.
  • the angle between the cylinder center line of the piston gas compression mechanism and the cylinder center line of the piston gas working mechanism is less than 180 degrees, the piston Gas compression
  • the piston of the book mechanism and the piston of the piston gas working mechanism are respectively connected to the same connecting rod journal of the same crankshaft via a connecting rod.
  • Solution 40 Based on the solution 39, further optionally, an angle between a cylinder center line of the piston type gas compression mechanism and a cylinder center line of the piston gas working mechanism is 90 degrees.
  • the piston of the piston type gas compression mechanism and the piston of the piston type gas working mechanism are respectively connected to the different connecting rod journals on the same crankshaft via a connecting rod.
  • the phase difference between the two connecting rod journals is greater than 0 degrees and less than 180 degrees.
  • the dual-channel entropy cycle engine further includes a low-temperature cold source for providing a low-temperature substance, and the low-temperature substance is used for cooling the piston type.
  • the dual-channel entropy cycle engine further includes a turbine power mechanism and an impeller compressor, and the working fluid outlet is connected to the working fluid inlet of the turbine power mechanism.
  • the working fluid outlet of the turbine power mechanism is connected to the working fluid inlet of the impeller compressor via an auxiliary cooler, and the working fluid outlet of the impeller compressor is in communication with the working fluid closed circuit;
  • An auxiliary working fluid outlet is disposed on the passage between the mass outlet and the working fluid inlet of the impeller compressor.
  • the dual-channel entropy cycle engine further includes a four-type door cylinder piston mechanism, and the air supply port of the four-type door cylinder piston mechanism and the working fluid closed circuit In communication, the refill port of the four-type door cylinder piston mechanism is in communication with the working fluid outlet.
  • the dual channel entropy cycle engine further includes an oxidant source, and the oxidant source is configured as the four types of door cylinder piston mechanism.
  • the side internal combustion combustion chamber is set as a four-type door cylinder piston mechanism, and the air supply port of the four types of door cylinder piston mechanism and the piston gas work
  • the cylinders of the mechanism are in communication, and the refilling port of the four types of door cylinder piston mechanisms is in communication with the working fluid outlet.
  • the dual-channel entropy cycle engine further includes an oxidant sensor and an oxidant control device, the oxidant sensor being disposed in the working fluid closed circuit, the oxidant sensor A signal is provided to the oxidant control device, the oxidant source being in communication with the working fluid closed circuit via an oxidant control valve, the oxidant control device controlling the oxidant control valve.
  • the piston gas compression mechanism is further configured as a piston liquid mechanism, and the piston liquid mechanism comprises a gas liquid cylinder and a gas-liquid isolation structure, wherein the gas-liquid isolation structure is Inside the gas-liquid cylinder.
  • the piston gas working mechanism is set as a piston liquid mechanism
  • the piston liquid mechanism comprises a gas liquid cylinder and a gas-liquid isolation structure, wherein the gas-liquid isolation structure is Inside the gas-liquid cylinder.
  • the gas working fluid of the gas-liquid cylinder has a pressure greater than the liquid in the gas-liquid cylinder and the gas-liquid liquid. Isolation of the isolation structure when doing reciprocating motion explain the sum of the power of the book.
  • the mass flow rate of the substance discharged from the internal combustion combustion chamber is greater than the mass flow rate of the substance introduced into the internal combustion combustion chamber from outside the closed circuit of the working medium.
  • the pressure-bearing capacity of the closed loop of the working fluid is greater than 2 MPa.
  • a regenerator is disposed on the communication passage, a working fluid outlet of the piston gas working mechanism and a working fluid inlet of the piston gas compression mechanism
  • the communication passage between the two is set as the cooled fluid passage of the regenerator, and the communication passage between the working fluid outlet of the piston type gas compression mechanism and the working fluid inlet of the piston gas working mechanism is It is the heated fluid passage of the regenerator.
  • the internal combustion combustion chamber is disposed in the communication passage in the form of a separate cavity.
  • the principle of the present invention is: replacing the conventional hot air machine with the internal combustion combustion chamber (that is, introducing an oxidant, a fuel into a working fluid of a hot air machine that needs to be heated, and causing a combustion chemical reaction to increase the temperature of the working medium)
  • the working fluid of all types of hot air compressors such as Stirling engine heats the heat exchanger, so that the temperature and pressure of the working fluid can reach a higher level, achieving the essential improvement of the efficiency and power density of the hot air machine, and can be greatly improved. Reduce the size, weight and manufacturing costs of the mechanism.
  • the internal combustion combustion chamber to perform internal combustion heating on the working fluid in the closed circuit of the working fluid, and pushing the piston of the piston gas working mechanism to perform external work, and realizing the work by guiding part of the working fluid from the closed loop of the working fluid In the closed loop, the working medium is balanced, and part of the heat can be derived while the working fluid in the closed circuit of the working fluid is derived;
  • the function of the cooler and the regenerator in the present invention is compared with the traditional Stirling engine
  • the function of the chiller and the regenerator is the same;
  • the function of the condensing cooler in the present invention is to condense and liquefy part of the working fluid in the closed circuit, and to export it from the closed loop of the working fluid in the form of liquid, so that
  • the working medium balance in the closed circuit of the working fluid can be realized, and the function of not discharging the gas to the environment can be realized, and the overall zero emission of the engine is formed.
  • the so-called accessory gas work mechanism refers to any mechanism that can generate power by gas working fluid expansion and/or flow, such as a piston gas work mechanism, an impeller gas work mechanism, a Roots gas work mechanism, etc.
  • the function is to perform work by using the gas working medium in the high energy state in the two-channel entropy cycle engine.
  • the so-called communication passage means a passage through which the working fluid of the piston type gas compression mechanism and the piston type gas working mechanism communicate.
  • the working fluid in the closed circuit of the working fluid may be a flue gas formed by the combustion of the oxidant and the fuel, or a mixture of the flue gas and other gases previously stored, such as a mixture of flue gas and helium, and smoke. a mixture of gas and argon, and the like.
  • the working fluid closed circuit refers to a space in which the working fluid can circulate in the communication passage of the piston type gas compression mechanism and the piston type gas work mechanism and the communication.
  • the internal combustion combustion chamber means that the high temperature product formed by the combustion chemical reaction between the oxidant and the fuel is directly used as a circulating working medium or mixed with other gases existing in the closed circuit of the working fluid as a circulating working medium. The combustion chamber.
  • the "internal combustion combustion chamber in the working fluid closed circuit” includes directly arranging the internal combustion combustion chamber in the working fluid closed circuit, and also includes the high temperature combustion product of the internal combustion combustion chamber.
  • the structure in which the working fluid is closed in a loop that is, the structure of the side-by-side internal combustion combustor.
  • the side-by-side internal combustion combustion chamber means that the internal combustion combustion chamber is an independent combustion space in which a passage is connected to the working fluid closed circuit.
  • the internal combustion combustion chamber may be an internal combustion continuous combustion chamber, an internal combustion intermittent combustion chamber or an internal combustion timing combustion chamber;
  • the internal combustion continuous combustion chamber refers to an internal combustion combustion chamber in which an exothermic chemical reaction may continuously occur;
  • the internal combustion intermittent combustion chamber refers to an internal combustion combustion chamber that does not continuously generate an exothermic chemical reaction, and the internal combustion intermittent combustion chamber may be a timing intermittent combustion chamber, and only occurs in the combustion chamber in each working cycle of the two-channel entropy circulation engine.
  • exothermic chemical reaction occurs only in one stroke; or may be a positive-time intermittent combustion chamber in which an exothermic chemical reaction occurs in a plurality of working cycles: or may be long
  • the two-channel entropy cycle engine continuously generates an exothermic chemical reaction in the combustion chamber in a plurality of working cycles.
  • the term "oxidant source” means a device, mechanism or storage tank which can supply an oxidant, and the oxidant in the oxidant source should have a higher pressure than the pressure in the internal combustion combustion chamber when entering the internal combustion combustion chamber.
  • the oxidizing agent refers to a substance which can react with a fuel in a liquid or high-pressure gas state, such as liquid oxygen, high-pressure oxygen, high-pressure compressed air, liquefied air, hydrogen peroxide, aqueous hydrogen peroxide, and the like.
  • a fuel in a liquid or high-pressure gas state
  • liquid oxygen high-pressure oxygen
  • high-pressure compressed air high-pressure compressed air
  • liquefied air hydrogen peroxide
  • hydrogen peroxide hydrogen peroxide
  • aqueous hydrogen peroxide aqueous hydrogen peroxide
  • the fuel source refers to a device, a mechanism or a storage tank that can provide fuel, and when the fuel in the fuel source enters the internal combustion combustion chamber, the pressure thereof should be higher than the pressure in the internal combustion combustion chamber, and the fuel is a substance capable of undergoing a combustion chemical reaction with an oxidant, such as a hydrocarbon, a carbon oxyhydroxide or a solid carbon; wherein the hydrocarbon includes gasoline, diesel, heavy oil, kerosene, aviation kerosene, and the like;
  • the hydroxide includes methanol, ethanol, methyl ether, diethyl ether, etc.;
  • the solid carbon has the advantages of high concentration of carbon dioxide in the product after combustion and combustion, and is easy to liquefy; the solid carbon can be pre-assembled, powdered and injected into the solid. Or powdered, and then injected into the hot air machine
  • the so-called working fluid outlet refers to the outlet of a part of the working fluid from the two-channel entropy circulating engine working fluid system, the purpose of which is to balance the excess of the introduced oxidant and reducing agent.
  • the working fluid to maintain the balance of the dual channel entropy cycle engine working fluid system.
  • the working fluid outlet may be a continuous derivation working medium, and may be an intermittent derivation working medium (that is, the working medium is derivatized according to the working medium accumulated in the closed circuit of the working medium), or may be The working fluid is exported according to the timing relationship.
  • the derived working medium may be in each working cycle of the two-channel entropy cycle engine, the working fluid outlet When the pressure at the specification is low, the working medium is exported; or the working medium is derived at the timing, and the working is performed intermittently after the working pressure is low at the working outlet of the two-channel entropy cycle engine after multiple working cycles
  • a pressure limiting device such as a pressure limiting valve to derive the working medium when the pressure in the working fluid closed circuit exceeds a certain limit.
  • a control valve is provided on the working fluid outlet: the control valve is controlled by a peak pressure control mechanism, and the peak pressure control mechanism causes the pressure in the closed circuit of the working fluid to exceed a set value
  • the control is wide open, and the control valve is closed when the pressure in the closed circuit drops back to the set value; or the control valve is controlled by the valley pressure control mechanism, and the working fluid is closed
  • the control valve is opened when the pressure inside is in the valley pressure state, and the control is closed when the pressure in the working fluid closed circuit is to 0.2 MPa; or the control valve is controlled by the opening degree control mechanism,
  • the opening degree control mechanism controls the opening degree of the control valve according to the pressure setting range in the working fluid closed circuit, so that the working fluid outlet is in a normally open state under a certain opening degree.
  • the working fluid in the closed loop of the working fluid may be derived in the form of a gas or may be derived in the form of a liquid.
  • the gas storage tank that communicates with the working fluid outlet can be used as a compressed gas source.
  • the cooler refers to any device capable of cooling the working fluid, such as a direct mixing type, a heat exchanger type, and a radiator type cooler.
  • the direct-mixing cooler refers to a device that directly mixes a heated fluid with a cooled working fluid, and directly performs heat exchange to achieve working fluid cooling;
  • the heat exchanger refers to a receiving medium that uses other fluids as heat.
  • the heat sink is a device that uses an ambient gas as a heat receiving medium to diffuse the heat of the working medium into the environment to reach a cooling working medium.
  • the heat exchanger and the heat sink are both non-direct mixed coolers, that is, the heated fluid is not mixed with the cooled working medium.
  • the condensing cooler comprises a direct mixing condensing cooler and a non-direct mixing condensing cooler, wherein the straight mixed condensing cooler means that the heated fluid and the cooled fluid are mixed therein to cause a portion of the cooled fluid to be generated or a device that condenses all of the temperature to heat the heated fluid;
  • the non-direct mixed condensing cooler means having a heated fluid passage and a cooled fluid passage, the heated fluid in the heated fluid passage and the cooled fluid passage Means in which the cooled fluid is subjected to heat exchange but not mixed, such as a heat exchanger type and a radiator type condensing cooler; the non-direct mixed condensing cooler and the direct mixing condensing cooler may have when necessary The function of the gas-liquid separator.
  • the circulating gas in the working fluid closed circuit may be selected from the group consisting of argon gas, helium gas, oxygen gas and the like.
  • non-condensable gas means a gas which is not liquefied after being cooled in the two-channel entropy cycle engine by an inert gas, nitrogen gas or the like, and preferably the non-condensable gas is argon gas.
  • the function of providing the non-condensable gas returning compressor is to extract non-condensable gas from the working fluid closed circuit and store it in the non-condensable gas storage tank when the system is not operating.
  • the low-temperature cold source refers to a device, a mechanism or a storage tank capable of providing a low-temperature substance having a temperature below 0 ° C, for example, a storage tank stored with a low-temperature substance obtained by a commercially available method, the low-temperature substance may be It is liquid nitrogen, liquid oxygen, liquid helium or liquefied air.
  • the oxidizing agent in the present invention is liquid oxygen, liquid oxygen can be directly used as the low temperature substance.
  • the low-temperature cold source is directly connected to the working fluid closed circuit to mix the low-temperature substance with the working medium in the working fluid closed circuit, or to make the low-temperature substance through a heat exchange device In the closed loop with the working fluid
  • the working medium heat exchange mode cools the working fluid in the piston type gas compression mechanism or is about to enter the piston type gas compression mechanism.
  • the two-channel entropy cycle engine is a power mechanism with a working cycle close to the Carnot cycle.
  • the temperature of the cold source is greatly decreased, that is, the temperature of the cold source is low, the thermal efficiency 77 is high, and the amount of heat discharged to the cold source is small. It is inferred that the cold source temperature 7 ⁇ can be greatly reduced by using a relatively low temperature low temperature substance, thereby greatly reducing the amount of heat discharged to the cold source and effectively improving the engine efficiency.
  • the storage of energy in a substance having a very low temperature corresponds to the concept of a novel battery which can be manufactured using a low-cost energy source such as garbage electricity, thereby effectively reducing the operating cost of the engine.
  • the low-temperature substance in the low-temperature cold source after the low-temperature substance in the low-temperature cold source exhibits a cooling action, it may be introduced into the working fluid closed circuit as a circulating medium of a two-channel entropy cycle engine, or may not be introduced into the working medium. In the loop.
  • the so-called two devices are in communication, meaning that the fluid can flow in one or two directions between the two devices.
  • communication is meant direct communication or indirect communication via a control mechanism, control unit or other control component.
  • the four-type door cylinder piston mechanism means that an air inlet, an exhaust port, a gas supply port and a refill port are provided on the cylinder, and the air inlet, the exhaust port, and the supply port are provided
  • the air port and the refill port are correspondingly arranged with a cylinder piston mechanism of an intake valve, an exhaust valve, a supply valve and a refill door.
  • the liquid oxygen includes commercial liquid oxygen or liquid oxygen prepared in the field.
  • the mass flow rate ⁇ 2 of the substance discharged from the internal combustion combustion chamber is greater than
  • the mass flow rate M of the substance introduced into the internal combustion combustion chamber outside the closed circuit of the working fluid means that, in addition to the substance introduced into the internal combustion combustion chamber from the closed circuit of the working fluid, a part of the substance is from the working medium Introducing the internal combustion combustion chamber into the closed circuit, since the internal combustion combustion chamber is disposed in the working fluid closed circuit, that is, at least a portion of the material discharged from the internal combustion combustion chamber flows back to the internal combustion
  • the combustion chamber, that is, the working medium has a reciprocating flow between the hot end mechanism and the cold end mechanism.
  • the substance introduced from the outside of the working fluid closed circuit to the internal combustion combustion chamber may be an oxidant, a reducing agent, a compressed gas or a high temperature gas.
  • the hot end mechanism refers to a gas working mechanism in which the internal combustion combustion chamber is disposed, or a working medium generated in a combustion chemical reaction in the internal combustion combustion chamber first enters, for example, the piston gas. Work organization.
  • the cold end mechanism refers to a gas compression mechanism into which the working medium flows out from the hot end mechanism, for example, the piston type gas compression mechanism.
  • the oxidant sensor refers to a device that detects the content of the oxidant in the closed circuit of the working fluid.
  • the oxidant sensor provides a signal to the oxidant control device, the oxidant control device according to a signal provided by the oxidant sensor and a preset static or dynamic oxidant content setting value in the working fluid closed circuit
  • the oxidant control valve is controlled to increase or decrease the amount of oxidant supplied to the working fluid closed circuit for the purpose of regulating the content of the oxidant in the closed loop of the working fluid.
  • the set value of the oxidant content in the specification may be a value or a numerical interval, for example: the oxidant content in the closed loop of the working fluid may be set at 5%, 10% or 10% ⁇ 12%. Wait.
  • the oxidant sensor may be disposed on a closed circuit remote from the internal combustion combustion chamber to ensure that the entire working fluid closed circuit operates in an oxygen-rich (oxygen content greater than zero) state, so that the internal combustion combustion chamber is stable. Combustion of chemical reactions while preventing carbon deposits.
  • the gas-liquid cylinder refers to a container which can accommodate a gas working medium and/or a liquid and can withstand a certain pressure, and the gas-liquid cylinder is divided into a gas end and a liquid end by the gas-liquid separating structure.
  • the gas end of the gas cylinder is provided with a gas working fluid circulation port for communicating with other devices or mechanisms in the closed circuit of the working fluid;
  • the liquid end of the gas liquid cylinder is provided with a liquid A flow port for communicating with a hydraulic power mechanism and/or a liquid working fluid return system.
  • the gas-liquid insulation structure refers to a structure that can reciprocate in the gas-liquid cylinder, such as a separator, a separator, a piston, etc., and functions to isolate the gas in the gas-liquid cylinder.
  • the gas-liquid insulation structure and the gas-liquid cylinder are sealingly fitted.
  • the gas-liquid cylinder may all be a gas working medium, or may be all liquid, or a gas worker. Both the substance and the liquid are present at the same time.
  • the liquid in the gas-liquid cylinder and the gas-liquid isolation structure are different from the conventional piston linkage mechanism, and the piston in the conventional piston linkage mechanism can be stopped by the thrust or pulling force of the connecting rod, thereby realizing Limiting the stroke of the piston, and in the gas-liquid cylinder, when the gas working fluid in the gas-liquid cylinder is doing positive work, the gas-liquid isolation structure is moved by the pressure to the bottom dead center, and the liquid is pressurized Forming the gas-liquid cylinder and pushing a hydraulic power mechanism (such as a liquid motor) to perform external work.
  • a hydraulic power mechanism such as a liquid motor
  • the liquid When the liquid is about to be exhausted, changing the liquid motor working mode or starting the liquid working fluid returning system, so that the liquid in the gas-liquid cylinder is not Further reducing, at this time, the liquid applies a braking force to the gas-liquid insulation structure in the gas-liquid cylinder to stop it to prevent it from hitting the wall of the bottom of the liquid end of the gas-liquid cylinder;
  • the gas-liquid isolation structure continuously moves toward the upper dead center, and when the vicinity of the top dead center is reached, the liquid is input into the gas cylinder or the liquid in the gas cylinder is stopped.
  • the liquid in the gas-liquid cylinder and the gas-liquid isolation structure still move due to the inertia to the dead center direction, and at this time, if the gas working fluid in the gas-liquid cylinder is not sufficiently pressurized High, the gas-liquid isolation structure continues to move upwards and hits the wall of the top of the gas cylinder.
  • the pressure of the gas working fluid in the gas-liquid cylinder needs to be sufficiently high to make the gas-liquid
  • the pressure of the isolation structure is greater than the sum of the inertial forces of the liquid in the gas cylinder and the gas-liquid isolation structure during reciprocation.
  • the sum of the inertial forces of the liquid in the gas-liquid cylinder and the gas-liquid isolation structure during reciprocation during the operation of the two-channel entropy cycle engine is varied, and therefore should be It is ensured that at any working moment, the inertia of the gas working fluid in the gas-liquid cylinder to the gas-liquid isolation structure is greater than the inertia of the liquid in the gas-liquid cylinder and the gas-liquid isolation structure.
  • the condition of the sum of forces is achieved, for example, by adjusting the working pressure in the closed circuit of the working fluid, adjusting the mass of the gas-liquid isolating structure, adjusting the density of the liquid, or adjusting the depth of the liquid, wherein the liquid depth refers to a liquid The depth of the liquid in the direction of reciprocation.
  • the so-called "adjusting the working pressure in the closed circuit of the working fluid” is to adjust the inflow and/or outflow of the working fluid.
  • the volume flow rate of the gaseous working fluid of the combined circuit can be realized, for example, by adjusting the switching interval of the working fluid outlet, the time of each opening, and/or the opening opening size of the working fluid outlet. .
  • the position of the internal combustion combustion chamber and the cooler on the closed circuit of the working fluid should be set according to a well-known thermodynamic cycle.
  • the working fluid in the working fluid closed circuit needs to be subjected to compression, heating, temperature rising and boosting, work and cooling, which requires the working fluid closed circuit to withstand a certain pressure
  • the pressure capacity of the closed loop of the working fluid can be set to be greater than 2 MPa, 2.5 MPa, 3 MPa, 3.5 MPa, 4 MPa, 4.5 MPa, 5 MPa, 5.5 MPa, 6 MPa, 6.5 MPa, 7 MPa, 7.5 MPa > 8 MPa, 8.5 MPa, 9 MPa, 9.5.
  • MPa 10 MPa, 10.5 MPa, l lMPa, 11.5 MPa, 12 MPa, 12.5 MPa, 13 MPa, 13.5 MPa, 14 MPa, 14.5 MPa, 15 MPa, 15.5 MPa, ⁇ Pa, 16.5 MPa, 17 MPa, 17.5 MPa, 18 MPa, 18.5 MPa, 19 MPa 19.5MPa, 20MPa, 20.5MPa, 21MPa, 22MPa, 23MPa, 24MPa, 25MPa, 26MPa, 27MPa, 28MPa, 29MPa, 30MPa, 31MPa, 32MPa, 33MPa, 34MPa, 35MPa, 36MPa, 37MPa, 38MPa, 39MPa or more than 40MPa. Accordingly, the pressure bearing capacity of the oxidant source and the fuel source is also set to the same numerical range as described above.
  • control valve is controlled by a minimum pressure in the closed circuit of the working fluid of more than 0.2 MPa, 0.3 MPa, 0.5 MPa, 1 MPa, 1.5 MPa, 2 MPa, 2.5 MPa, 3 MPa, 5 MPa, 8 MPa or more than 10 MPa. Controlled.
  • the piston type gas compression mechanism and the piston type gas work mechanism may not be wide, but rely on the phase difference between each other to form the compression and expansion work of the system.
  • thermodynamic processes and thermodynamic cycles are the most basic and important state parameters of the working fluid.
  • P-T diagrams with pressure P and temperature T as coordinates have not been used in the study of thermodynamic processes and thermodynamic cycles.
  • the inventors have for the first time proposed the idea of studying thermodynamic processes and thermodynamic cycles using P-T diagrams.
  • PT maps have obvious advantages over commonly used PV maps and ⁇ -s maps, which can more fully describe the working conditions of thermodynamic processes and thermodynamic cycles. The changes have enabled the inventors to have a deeper understanding of thermodynamic processes and thermodynamic cycles.
  • thermodynamics Using the PT diagram, the inventors summarized ten new ways of elaboration of the second law of thermodynamics. These new elaborations are equivalent to the previous methods of thermodynamics of Kelvin and Clausius, but more clearly reveal the work. The difference between the quality heating process and the compression process also points the way for the development of high-efficiency heat engines. This new method and new law will greatly promote the development of thermodynamics and the advancement of the heat engine industry. details as follows:
  • the PV map and the TS map have been widely used in thermodynamic research.
  • P and T are the most important state parameters of the working fluid
  • the inventors plotted the PT map with the pressure P and the temperature T as coordinates, and will take the Camot Cycle.
  • the Otto Cycle is identified in the PT diagram shown in FIG.
  • the PT map makes the changes in the working state of the thermodynamic process and the thermodynamic cycle more obvious, and makes the nature of the thermodynamic process and the thermodynamic cycle easier to understand.
  • the PT diagram of the Carnot Cycle shown in Figure 26 allows the inventors to easily conclude that the mission of the reversible adiabatic compression process of Carnot Cycle is to increase the temperature of the working fluid to a reversible adiabatic compression.
  • the temperature of its high temperature heat source to achieve high temperature Explain that the temperature of the heat source of the book is consistent with the constant temperature endothermic expansion process from the high temperature heat source. Furthermore, the inventors can clearly see that when the temperature of the high temperature heat source of the Carnot Cycle rises, the inventors must compress the working medium to a deeper level in the reversible adiabatic compression process of the Carnot Cycle to make it higher. The temperature is reached to reach the temperature of the high-temperature heat source after the temperature rise, so as to achieve the constant temperature endothermic expansion process of the high-temperature heat source after self-heating on the premise of keeping the temperature of the high-temperature heat source after the temperature rise, thereby achieving efficiency.
  • any process connecting two different adiabatic process curves is a non-adiabatic process (so-called A non-adiabatic process refers to a process with heat transfer, that is, an exothermic process and an endothermic process).
  • a non-adiabatic process refers to a process with heat transfer, that is, an exothermic process and an endothermic process.
  • the inventors have marked two state points, point A and point B. If a thermal process or a series of interconnected thermal processes arrives from point A to point B, the inventors refer to the process of connecting point A and point B, whereas the inventors refer to the process of connecting point B and point A. According to Fig.
  • the inventors can conclude that if point B is on the adiabatic process curve where point A is located, the process of connecting point A and point B is an adiabatic process; if point B is at point A On the right side of the adiabatic process curve, the process of connecting point A and point B is an endothermic process; if point B is to the left of the adiabatic process curve where point A is located, the process of connecting point A and point B is an exothermic process. Since the process of connecting the point A and the point B may be an exothermic process, an adiabatic process or an endothermic process, the inventors have defined point A as having a surplus temperature, an ideal temperature, and an insufficient temperature, respectively, with reference to point B.
  • the process of connecting point B and point A may be an exothermic process, an adiabatic process or an endothermic process, so the inventors have defined point B as having an excess temperature, an ideal temperature, and an insufficient temperature, respectively, with reference to point A.
  • thermodynamics
  • the difference between the heating process of the working fluid and the compression process of the working fluid is that the heating process must generate excess temperature, but the compression process is not.
  • thermodynamics research the PT diagram and the above-mentioned new elaboration method for the second law of thermodynamics should be widely applied.
  • the PT diagram and the new elaboration of the second law of thermodynamics are of great significance for the advancement of thermodynamics and the development of high-efficiency heat engines.
  • the temperature of that state is lower than that of the initial state.
  • the invention replaces the external combustion heating mode of the traditional hot air machine by using the internal combustion heating mode, and applies the direct heating of the internal combustion heating mode to the hot air machine, thereby overcoming the temperature and pressure of the working medium due to the difficulty of the conventional hot air machine.
  • the higher level affects the power and power density, which can effectively save energy and greatly reduce the size, weight and manufacturing cost of the mechanism, and has broad application prospects.
  • Embodiment 1 is a schematic structural view of Embodiment 1 of the present invention.
  • FIG. 2 is a schematic structural view of Embodiment 2 of the present invention
  • Figure 3 is a schematic structural view of Embodiment 3 of the present invention
  • Figure 4 is a schematic structural view of Embodiment 4 of the present invention.
  • Figure 5 is a schematic view showing the structure of Embodiment 5 of the present invention.
  • Figure 6 is a schematic view showing the structure of Embodiment 6 of the present invention.
  • Figure 7 is a schematic view showing the structure of Embodiment 7 of the present invention.
  • Figure 8 is a schematic view showing the structure of Embodiment 8 of the present invention.
  • Figure 9 is a schematic view showing the structure of Embodiment 9 of the present invention.
  • Figure 10 is a schematic view showing the structure of an embodiment of the present invention 10.
  • Figure 11 is a schematic structural view of Embodiment 11 of the present invention.
  • Figure 12 is a schematic view showing the structure of Embodiment 12 of the present invention.
  • Figure 13 is a schematic view showing the structure of Embodiment 13 of the present invention.
  • Figure 14 is a schematic view showing the structure of Embodiment 14 of the present invention.
  • Figure 15 is a schematic view showing the structure of Embodiment 15 of the present invention.
  • Figure 16 is a schematic view showing the structure of Embodiment 16 of the present invention.
  • Figure 17 is a schematic view showing the structure of Embodiment 17 of the present invention.
  • Figure 18 is a schematic view showing the structure of Embodiment 18 of the present invention.
  • Figure 19 is a schematic view showing the structure of Embodiment 19 of the present invention.
  • Figure 20 is a schematic view showing the structure of Embodiment 20 of the present invention.
  • Figure 21 is a schematic view showing the structure of Embodiment 21 of the present invention.
  • Figure 22 is a schematic view showing the structure of Embodiment 22 of the present invention.
  • Figure 23 is a schematic view showing the structure of Embodiment 23 of the present invention.
  • Figure 24 is a schematic view showing the structure of Embodiment 24 of the present invention.
  • Figure 25 is a schematic view showing the structure of Embodiment 25 of the present invention.
  • Figure 26 shows the PT diagram of the Carnot cycle and the Alto cycle, where , e i and e 2 are constants of different values, which are adiabatic indices, and cycles 0-2-3-0 are Carnot cycles, cycles 0-1-4-5-0 is the Carnot cycle after the temperature of the high temperature heat source rises, and the cycle 0-6-7-8-0 is the Alto cycle;
  • Figure 27 shows a PT diagram of a plurality of different adiabatic process curves, where C ', ⁇ 2 , 3 , and are constants of different values, are adiabatic indices, and A and B are state points;
  • Figure 28 shows the P-T diagram of the adiabatic process curve, where C is a constant, is the adiabatic index, and A and B are the state points.
  • the two-channel entropy cycle engine shown in FIG. 1 includes a piston gas compression mechanism 9, a piston gas work mechanism 10, and two communication passages 1, and the working fluid outlet of the piston gas compression mechanism 9 passes through the communication.
  • the passage 1 is in communication with the working fluid inlet of the piston gas working mechanism 10, and the working fluid outlet of the piston gas working mechanism 10 passes through the working fluid inlet of the other communication passage 1 and the piston gas compression mechanism 9.
  • the piston-type gas compression mechanism 9 communicates with the piston-type gas work mechanism 10 via the two communication passages 1 to form a working fluid closed circuit; the working fluid outlet of the piston-type gas compression mechanism 9 and the An internal combustion combustion chamber 3 is disposed on the communication passage 1 between the working fluid inlets of the piston gas working mechanism 10, and the working fluid outlet of the piston gas working mechanism 10 and the working inlet of the piston gas compression mechanism 9 A working fluid outlet 6 is disposed in the communication passage 1 between the two, and a control valve 17 is disposed on the working fluid outlet 6.
  • necessary components, units or systems should be provided where necessary according to known techniques, such as providing an oxidant inlet, a reducing agent inlet and a spark plug 15 on the internal combustion combustion chamber 3, and corresponding oxidant sources.
  • 4 and the fuel source 5 is in communication with the internal combustion combustion chamber 3, and correspondingly, the oxidant in the oxidant source 4 may be air, and the fuel in the fuel source 5 is gasoline.
  • the working fluid derived from the working fluid outlet 6 may be a gas or a liquid, and the working fluid outlet 6 discharges the working medium while carrying out the working part. Heat.
  • control valve 17 can be set as a pressure control valve, and the working fluid portion that causes the excessive pressure is led to close the working fluid.
  • the internal combustion combustion chamber 3 may be disposed at any other position within the working fluid closed circuit, and is preferably disposed upstream of the working fluid outlet of the piston gas compression mechanism 9.
  • the working fluid outlet 6 may be disposed at any other position in the closed circuit of the working fluid, preferably It is disposed on the working fluid closed circuit upstream of the working fluid outlet of the piston gas working mechanism 10 and downstream of the working fluid inlet of the internal combustion combustion chamber 3; the control valve 17 may not be provided.
  • the working process of the product of the present embodiment an oxidant and a fuel respectively supplied from the oxidant source 4 and the fuel source 5, a combustion reaction occurs in the internal combustion combustion chamber 3, and the combustion into the internal combustion combustion chamber 3
  • the original gaseous working medium in the closed circuit of the working medium is heated, and simultaneously enters the living along the communication channel 1 together with the product produced by the combustion.
  • the plug gas working mechanism 10 outputs external power; the working fluid after the work is discharged through the piston gas work mechanism 10, and then enters the piston gas compression mechanism 9 via another communication passage 1 to be compressed.
  • the compressed gas working medium is returned to the internal combustion combustion chamber 3 via the working fluid outlet of the piston type gas compression mechanism, and is heated according to the cycle; wherein when the working fluid closes the circuit, the pressure is too large,
  • the working fluid outlet 6 leads to a part of the working fluid.
  • the two-channel entropy cycle engine shown in FIG. 2 differs from the embodiment 1 in that: the two-channel entropy cycle engine further includes a cooler, the cooler is configured as a radiator 21, and the radiator 21 is disposed at
  • the communication channel between the working fluid outlet of the piston gas working mechanism 10 and the working fluid inlet of the piston gas compression mechanism 9 may be used as liquid oxygen in the oxidant source 4;
  • the working fluid outlet 6 is disposed on the communication passage 1 between the working fluid outlet of the piston type gas compression mechanism 9 and the working inlet of the internal combustion combustion chamber 3, and the working fluid outlet 6 is controlled to be 17 and stored.
  • the gas tank 60 is connected, the gas storage tank 60 is for storing high pressure gas and non-condensable gas, the fuel source 5 and the scattered gas
  • the degree of cooling of the working medium by the heater 21 determines the type and state of the derived working medium.
  • the derived working medium may be gaseous or liquid water, or a mixture thereof with a gas in a closed loop;
  • the derived working fluid further contains other products such as carbon dioxide, and the circulating gas in the closed circuit of the working fluid is set to helium.
  • the piston of the piston type gas compression mechanism 9 and the piston of the piston type gas work mechanism 10 are respectively connected via a connecting rod and a different connecting rod journal on the same crankshaft, and the phase difference between the two connecting rod journals is 90 degree.
  • control valve 17 can be selectively set as a pressure control valve, and the control valve 17 is controlled by a peak pressure control mechanism, and the pressure of the peak pressure control mechanism in the working fluid closed circuit exceeds Setting the value to open the control block 17 and closing the control valve 17 when the pressure in the closed circuit drops back to the set value; or subjecting the control valve 17 to the valley pressure control mechanism Controlling that the control valve 17 is opened when the pressure in the working fluid closed circuit is in a valley pressure state, and the control valve 17 is closed when the pressure in the working fluid closed circuit is to 0.2 MPa; or
  • the control valve 17 is controlled by an opening degree control mechanism, and the opening degree control mechanism controls the opening degree of the control valve 17 according to a pressure setting range in the working fluid closed circuit to make the working fluid outlet 6 In a normally open state at a certain degree of opening; alternatively, the pressure in the closed circuit of the working fluid is set to be greater than 0.3 MPa, 0.5 MPa, 1 MPa, 1.5 MPa, 2 MPa, 2.5 MPa, 3 MP
  • the cooler may be configured as another type of cooler, such as a heat exchanger cooler; the cooler may also be disposed at any other location of the working fluid closed circuit; The cooler and the gas storage tank 60 may be alternatively disposed; the control valve 17 may not be provided.
  • the phase difference between the two connecting rod journals may be set to any value in a range of more than 0 degrees and less than 180 degrees; or the piston of the piston type gas compression mechanism 9 and the piston gas working mechanism
  • the pistons of 10 can be connected to the same connecting rod journal of the same crankshaft via the connecting rods respectively.
  • the angle between the cylinder center lines of the two cylinders should be set to be less than 180 degrees.
  • the connection relationship between the piston of the piston type gas compression mechanism 9 and the piston and the crankshaft of the piston gas work mechanism 10 can be set with reference to the embodiment and its transformable embodiment.
  • the piston of the piston type gas compression mechanism 9 and the piston of the piston gas work mechanism 10 and the crankshaft may be in other connection relationship;
  • the control valve 17 can be controlled by the peak pressure control mechanism, controlled by the valley pressure control mechanism, or controlled by the opening degree control mechanism with reference to the present embodiment. .
  • the working fluid outlet 6 may be in communication with the gas storage tank 60 with reference to the present embodiment.
  • the two-channel entropy cycle engine shown in FIG. 3 differs from the embodiment 1 in that: the two-channel entropy cycle engine further includes a cooler, the cooler is configured as a radiator 21, and the radiator 21 is disposed at The piston of the piston type gas compression mechanism 9 is on the cylinder.
  • the heat sink 21 may also be disposed on the communication channel 1 at the working fluid outlet of the piston gas compression mechanism 9; the internal combustion combustion chamber 3 may also be disposed in the In the cylinder of the piston gas working mechanism 10, the working fluid flowing out of the internal combustion combustion chamber 3 is a working medium in a high energy state, and the purpose is to directly work by using the working medium in a high energy state.
  • the two-channel entropy cycle engine shown in FIG. 4 differs from Embodiment 1 in that: the two-channel entropy cycle engine further includes a cooler, and the cooler is set as a gas-liquid direct charge cooler 20, the gas
  • the liquid direct mixing cooler 20 is disposed on a communication passage between the working fluid outlet of the piston type gas working mechanism 10 and the working fluid inlet of the piston type gas compression mechanism 9, and the internal combustion combustion chamber 3 is disposed adjacent to
  • the internal combustion combustion chamber 31 is provided with a check width 7 on the communication passage 1 between the working fluid outlet of the piston type gas compression mechanism 9 and the side internal combustion combustion chamber 31, thereby causing the piston gas to be
  • the working fluid flowing out of the compression mechanism 9 is heated by the side internal combustion combustion chamber 31 and flows to the piston gas working mechanism 10.
  • the so-called gas-liquid direct-mixing cooler 20 means that a cooling liquid introduction port and a discharge port are provided on the closed circuit of the working fluid, and the principle is to absorb the gas in the closed circuit of the working fluid by using the introduced liquid. The heat is cooled and cooled, and the heated liquid is further discharged from the closed loop of the working fluid; a gas-liquid separator can be used for exporting to prevent the gas working fluid from flowing out.
  • gas-liquid direct mixing cooler 20 and the backstop 7 may alternatively be provided; the cooler may be provided as another type of cooler.
  • the internal combustion combustion chamber 3 can be referred to as the side combustion chamber 31 with reference to the present embodiment.
  • the two-channel entropy cycle engine shown in FIG. 5 differs from the third embodiment in that: the radiator 21 is modified in the working fluid outlet of the piston gas working mechanism 10 and the piston gas compression mechanism 9 Between the entrances of the working fluids In the communication passage 1, the internal combustion combustion chamber 3 is disposed in a cylinder of the piston gas working mechanism 10, and the working fluid outlet 6 is disposed in the radiator 21 and the piston type gas compression mechanism
  • the communication channel 1 between the working fluid inlets of the nine, the dual channel entropy cycle engine further includes a non-direct mixing condensing cooler 18, the working fluid outlet 6 and the non-direct mixing condensing cooler 18 Connected to the cooling medium inlet, a cryogenic liquid discharge port 62 is disposed on the non-direct mixed condensing cooler 18, and the cryogenic liquid discharge port 62 communicates with the cryogenic liquid working fluid storage tank 16, the non-direct mixing
  • the condensing cooler 18 further cools the working fluid flowing out of the piston gas working mechanism 10 and cooled by the radiator 21, and the generated gas
  • cryogenic liquid working fluid storage tank 16 may not be provided; the cryogenic liquid discharge port 62 may not be provided.
  • the non-direct mixed condensing cooler 18 and its related structure may be provided with reference to the present embodiment.
  • the two-channel entropy cycle engine shown in FIG. 6 differs from the embodiment 5 in that the cryogenic liquid working fluid storage tank 16 is eliminated, and the internal combustion combustion chamber 3 is modified in the piston type gas compression mechanism.
  • a non-condensing gas outlet 82 is added to the non-direct mixed condensing cooler 18 on the communication passage 1 between the working fluid outlet of the piston and the working fluid inlet of the piston gas working mechanism 10, the oxidant source 4 via the heated fluid passage of the non-direct mixing condensing cooler 18 in communication with the internal combustion combustion chamber 3, the oxidant acting as a refrigerant for the non-direct mixing condensing cooler 18, thereby effecting the working fluid outlet 6
  • the working fluid coming out is further cooled.
  • the working medium cooled by the non-direct mixed condensing cooler 18 is partially cooled to flow out of the condensed cooling liquid outlet 81, and the other part is cooled, and is still in the form of gas, which is non-condensable.
  • the non-condensable gas flows out from the non-condensable gas outlet 82.
  • the cryogenic liquid discharge port 62 is in communication with a cryogenic liquid working fluid storage tank 16 for storing a gas liquefaction;
  • the non-condensing gas outlet 82 is in communication with the non-condensable gas storage tank 70 for storing non-condensable gas, or the non-condensable gas outlet 82 is in communication with the piston type gas compression mechanism 9, and the non-condensable gas is further compressed. Re-entering the working fluid closed circuit, or the non-condensing gas outlet 82 may also be in communication with any other position of the working fluid closed circuit, as long as the non-condensable gas can be returned to the working fluid closed circuit.
  • the two-channel entropy cycle engine shown in FIG. 7 differs from the embodiment 3 in that the cooler is relocated to the working fluid outlet 6 and the working inlet of the piston gas working mechanism 10. Between the communication passages 1, and two, that is, a non-direct mixing cooler 23 as the cooler is added, and the oxidant source 4 passes through the heated fluid passage of the non-direct mixing cooler 23. It is in communication with the internal combustion combustion chamber 3.
  • the heated fluid passage of the non-direct mixing cooler 23 may not be in communication with the oxidant source 4; the oxidant source 4 may be in direct communication with the internal combustion chamber 3.
  • the two-channel entropy cycle engine shown in FIG. 8 differs from the embodiment 7 in that: the radiator 21 and the Description
  • the communication passage 1 between the non-direct mixing condensing coolers 18 is provided with a cooling liquid discharge port 61, and the non-direct mixing cooler 23 is provided with a cryogenic liquid discharge port 62.
  • the mixed condensing cooler 18 is further cooled, and the liquefied working medium after being cooled is discharged through the cryogenic liquid discharge port 62.
  • the working fluid outlet 6 corresponds to a discharge port including the cooling liquid discharge port 61 and the cryogenic liquid discharge port 62.
  • the two-channel entropy cycle engine shown in FIG. 9 differs from Embodiment 3 in that: the two-channel entropy cycle engine further includes a direct connection passage 100, and the direct connection passage 100 communicates with the piston gas work mechanism 10
  • the working fluid outlet is connected to the working fluid inlet of the piston compression mechanism 9, and the direct connecting passage 100 is equivalent to the working fluid outlet of the piston gas working mechanism 10 and the working fluid inlet of the piston compression mechanism 9.
  • the communication passage 1 is divided into two branches, one of which is provided with a cooler (partial communication passage provided with a cooler), and the other branch (directly connected to the passage 100) is not provided.
  • the cooler is provided with a control width 17 for controlling the opening and closing of the two branches.
  • the function of the direct connection channel 100 is: when the temperature of the working fluid flowing out from the working fluid outlet of the piston gas working mechanism 10 is low, the control width 17 on the direct connection channel 100 is opened.
  • the control valve 17 on the communication passage 1 is closed, and the working fluid can flow through the direct connection passage 100 to the cylinder of the piston type gas compression mechanism 9; when working from the piston gas working mechanism 10
  • the temperature of the working fluid flowing out of the mass outlet is high, and when the cooling is required to be cooled by the cooler, the control valve 17 on the direct connecting passage 100 is closed, the control valve 17 on the communication passage 1 is opened, and the working medium is connected.
  • the passage 1 flows into the cylinder of the piston type gas compression mechanism 9.
  • the two-channel entropy cycle engine shown in FIG. 10 differs from the third embodiment in that: the heat sink 21 is modified in the working fluid outlet of the piston gas working mechanism 10 and the piston gas compression mechanism 9
  • the communication passage 1 between the working fluid inlets is provided on the communication passage 1 between the working fluid outlet of the piston gas working mechanism 10 and the working fluid inlet of the piston gas compression mechanism.
  • a piston type gas working mechanism 10 because of the high working energy of the gas working medium after one work, the work can be continued, and the two piston type gas working mechanisms 10 can be arranged in series to improve the efficiency of the engine.
  • the two-channel entropy cycle engine shown in FIG. 11 differs from the third embodiment in that: the radiator 21 is modified in the working fluid outlet of the piston gas working mechanism 10 and the piston gas compression mechanism 9
  • the oxidant source 4 communicates with the communication passage 1 between the radiator 21 and the working inlet of the piston gas compression mechanism 9 via an oxidant inlet
  • a cooling liquid discharge port 61 is provided on the communication passage 1 between the radiator 21 and the oxidant inlet
  • a liquid is provided on the communication passage 1 of the oxidant inlet and the piston type gas compression mechanism 9.
  • a carbon dioxide outlet 64 for further cooling the working fluid in the communication passage 1. — ⁇ L ⁇ ⁇ if
  • the two-channel entropy cycle engine shown in FIG. 12 differs from the embodiment 6 in that: in the working fluid closed circuit, the gas participating in the cycle contains argon gas, and the two-channel entropy cycle engine further includes non-condensing.
  • the gas storage tank 70, the non-condensing gas outlet 82 of the non-direct mixing condensing cooler 18 is connected to the non-condensable gas storage tank 70 via a control valve 17, and the non-condensable gas storage tank 70 and the working fluid closed circuit Connected.
  • control valve 17 can be modified to any other suitable control device.
  • Example 13
  • the two-channel entropy cycle engine shown in FIG. 13 differs from the third embodiment in that: the radiator 21 is modified in the working fluid outlet of the piston gas working mechanism 10 and the piston gas compression mechanism 9
  • the communication channel 1 between the working fluid inlets further includes a non-condensing gas returning compressor 71, and the air inlet of the non-condensing gas returning compressor 71 passes through the control valve 17 and the
  • the working fluid is in closed loop communication, and the gas outlet of the non-condensable gas returning compressor 71 is in communication with the non-condensable gas storage tank 70, and the non-condensable gas storage tank 70 is in communication with the working fluid closed circuit.
  • control valve 17 can be modified to any other suitable control device; the non-condensable return storage compressor 71 can be omitted.
  • the two-channel entropy cycle engine shown in FIG. 14 differs from the first embodiment in that: a regenerator 33 is provided on the communication passage 1, and the regenerator 33 is a heat exchange regenerator,
  • the communication passage 1 between the working fluid outlet of the piston type gas working mechanism 10 and the working medium inlet of the piston type gas compression mechanism 9 is set as the cooled fluid passage of the regenerator 33, the piston gas
  • the communication passage 1 between the working fluid outlet of the compression mechanism 9 and the working fluid inlet of the piston gas working mechanism 10 is set as the heated fluid passage of the regenerator 33.
  • the dual-channel entropy cycle engine shown in FIG. 15 differs from the embodiment 4 in that the dual-channel entropy cycle engine further includes an auxiliary gas work mechanism 102, and the auxiliary gas work mechanism 102 is set as a piston gas work mechanism.
  • the working fluid outlet 6 communicates with the inlet of the auxiliary gas working mechanism 102.
  • the working fluid derived from the working fluid outlet 6 is also in a high temperature and high pressure state, and the piston gas working mechanism can be pushed to continue work.
  • the auxiliary gas working mechanism 102 may be a gas working mechanism such as a Roots gas working mechanism, a screw gas working mechanism or a power turbine.
  • the two-channel entropy cycle engine shown in FIG. 16 differs from the third embodiment in that: the radiator 21 is modified in the working fluid outlet of the piston gas working mechanism 10 and the piston gas compression mechanism 9 On the communication passage 1 between the working fluid inlets, the working fluid outlet 6 is modified between the radiator 21 and the working fluid outlet of the piston gas working mechanism 10
  • the dual-channel entropy cycle engine further includes a direct-mix condensing cooler 19, the cooled fluid inlet of the direct-mix condensing cooler 19 is in communication with the working fluid outlet 6, the oxidant source 4 and the straight
  • the heated condensing cooler 19 is connected to the heated fluid inlet, and the direct mixing condensing cooler 19 is provided with a cryogenic liquid discharge port 62, and the cryogenic liquid discharge port 62 communicates with the cryogenic liquid working fluid storage tank 16
  • Straight-mixed condensing cooler 19 The description is provided with a non-condensing gas outlet 82, which is in communication with the working fluid closed circuit.
  • the heated fluid outlet of the direct mixing condensing cooler, 19 is set as the non-condensing gas outlet 82, that is, the oxidant source 4 passes through the heated fluid outlet of the direct mixing condensing cooler 19. It is in communication with the internal combustion combustion chamber 3.
  • the heated fluid outlet of the direct mixing condensing cooler 19 may be separated from the non-condensable gas outlet 82, and connected to the working fluid closed circuit via the non-condensing gas outlet 82. .
  • the two-channel entropy cycle engine shown in FIG. 17 differs from the embodiment 3 in that: the cooler is modified in the working fluid outlet of the piston gas working mechanism 10 and the piston gas compression mechanism 9 On the communication channel 1 between the working fluid inlets, and the cooler is changed to an adsorption cooler 22, the working fluid outlet of the piston gas working mechanism 10 and the piston gas compression mechanism 9 The communication passage 1 between the working fluid inlets is set as the cooled fluid passage of the adsorption cooler 22.
  • the two-channel entropy cycle engine shown in FIG. 18 differs from the third embodiment in that: the internal combustion combustion chamber 3 is disposed in the communication passage 1 in the form of a separate cavity to ensure that the working fluid burns more.
  • the stability is smoother, and a three-way catalyst 88 is disposed in the communication passage 1 between the internal combustion combustion chamber 3 and the working fluid inlet of the piston gas working mechanism 10.
  • the internal combustion combustion chamber 3 may be disposed in the communication passage 1 in the form of a separate cavity with reference to the present embodiment.
  • the two-channel entropy cycle engine shown in Fig. 19 differs from the embodiment 3 in that between the working fluid outlet of the piston gas working mechanism 10 and the working fluid inlet of the piston gas compression mechanism 9.
  • a three-way catalyst 88 is disposed in the communication passage 1 .
  • the two-channel entropy cycle engine shown in FIG. 20 differs from the first embodiment in that: the two-channel entropy cycle engine further includes a low-temperature cold source 50, the low-temperature cold source 50 and the piston-type gas compression mechanism 9
  • the cryogenic cold source 50 is for providing a low temperature substance for cooling the working fluid of the piston type gas compression mechanism 9, and the low temperature substance of the low temperature cold source 50 is set to liquid nitrogen.
  • the low temperature cold source 50 may also be connected to a communication channel between the working fluid outlet of the piston gas working mechanism 10 and the working fluid inlet of the piston gas compression mechanism 9 .
  • the cryogenic material is provided for cooling the working fluid that is about to enter the piston gas compression mechanism 9; the cryogenic cold source 50 may also be heat exchanged to the working fluid in the piston gas compression mechanism 9 or The working fluid that is about to enter the piston type gas compression mechanism 9 is cooled.
  • the two-channel entropy cycle engine shown in FIG. 21 differs from Embodiment 1 in that: the two-channel entropy cyclic transmission Description
  • the motive further includes a radiator 21, a turbine power mechanism 14 and an impeller compressor 13, the radiator 21 being disposed at a working fluid outlet of the piston gas working mechanism 10 and a working fluid inlet of the piston gas compression mechanism 9.
  • the working fluid outlet 6 communicates with the working fluid inlet of the turbine power mechanism 14 , and the working fluid outlet of the turbine power mechanism 14 is compressed by the auxiliary cooler 21 1 and the impeller.
  • the working fluid inlet of the machine 13 is in communication, and the working fluid outlet of the impeller compressor 13 is in communication with the communication passage 1; between the working fluid outlet of the turbine power mechanism 14 and the working fluid inlet of the impeller compressor 13
  • An auxiliary working fluid outlet 66 is provided on the passage.
  • the auxiliary working fluid outlet 66 shown in the drawing is provided on the passage between the auxiliary cooler 21 1 and the working inlet of the impeller compressor 13.
  • the turbine power mechanism 14 may be coaxially disposed with the impeller compressor 13 and output power thereto; the auxiliary working fluid outlet 66 may also be disposed at the turbine power mechanism 14 a working medium outlet and a passage between the auxiliary cooler 21 1; a working fluid outlet of the impeller compressor 13 communicates with a communication port provided on the closed circuit of the working fluid, the communication port and the working The mass outlets 6 are disposed at different locations on the closed circuit of the working fluid.
  • the two-channel entropy cycle engine shown in FIG. 22 differs from the third embodiment in that: the radiator 21 is modified in the working fluid outlet of the piston gas working mechanism 10 and the piston gas compression mechanism 9 On the communication passage 1 between the working fluid inlets, the working fluid outlet 6 is modified on a communication passage between the working fluid outlet of the piston gas working mechanism 10 and the radiator 21,
  • the oxidant source 4 is set as a four-type door cylinder piston mechanism 99, and the four-type door cylinder piston mechanism 99 is caused to perform the power stroke of the four-type door cylinder piston mechanism 99 according to the intake stroke-pressure gas supply stroke-gas back charge-
  • the exhaust stroke operation mode is controlled by four types of door control mechanisms that are cyclically operated.
  • the air supply port 993 is an oxidant outlet of the oxidant source 4, and the refill port 994 is in communication with the working fluid outlet 6.
  • the oxidant compressed by the four-type door cylinder piston mechanism 99 enters the internal combustion combustion chamber 3 through the air supply port 993, and the fuel source 5 injects fuel into the internal combustion combustion chamber 3, the oxidant And a combustion chemical reaction occurs between the fuel in the internal combustion combustion chamber 3, a large amount of heat generated to heat the working fluid in the closed circuit of the working fluid, and the mixed combustion product pushes the piston gas working mechanism 10 to perform work,
  • the working fluid flowing out of the piston gas working mechanism 10 enters the four-type door cylinder piston mechanism 99 through the working fluid outlet 6 , and the residual heat of the working medium pushes the four types of door cylinder piston mechanism 99 to work,
  • the exhaust port 992 discharges the four types of door cylinder piston mechanisms.
  • the oxidant source 4 can be separated from the four type of door cylinder piston mechanism 99.
  • the two-channel entropy cycle engine shown in FIG. 23 differs from the fourth embodiment in that: the cooler is a radiator 21, and the bypass internal combustion chamber 31 is set as a four-type door cylinder piston mechanism 99.
  • the oxidant source 4 and the fuel source 5 are in communication with the air inlet 991, and a spark plug 15 is disposed on the four-type door cylinder piston mechanism 99, and the oxidant source 4 and the fuel source 5 are in the four categories.
  • part of the high temperature and high pressure working fluid generated can be used to make the four types of door cylinder piston mechanism 99 work, and another part of the working medium enters the working fluid closed circuit through the air supply port 993.
  • the refilling port 994 is in communication with the working fluid outlet 6, and the part of the working fluid discharged from the working fluid outlet 6 is from the Refill port 994 import office
  • the four types of door cylinder piston mechanism 99 discharges part of the working medium through the exhaust port 992.
  • the two-channel entropy cycle engine shown in FIG. 24 differs from Embodiment 3 in that: the two-channel entropy cycle engine further includes an oxidant sensor 51 and an oxidant control device 52, and the oxidant sensor 51 includes an oxidant probe.
  • the oxidant probe is disposed in the communication passage 1, and the oxidant sensor 51 provides a signal to the oxidant control device 52.
  • the oxidant source 4 is in communication with the working fluid closed circuit via an oxidant control valve 53.
  • the oxidant control device 52 The oxidant control valve 5 is controlled to open or close to adjust the amount of oxidant in the closed circuit of the working fluid.
  • the two-channel entropy cycle engine shown in FIG. 25 differs from the embodiment 24 in that: the piston type gas compression mechanism 9 and the piston gas work mechanism 10 are each configured as a piston liquid mechanism 90, the piston liquid
  • the mechanism 90 includes a gas-liquid cylinder 91 and a gas-liquid isolation structure 92, and the gas-liquid insulation structure 92 is disposed in the gas-liquid cylinder 91.
  • the liquid end of the gas-liquid cylinder 91 is in communication with a hydraulic power mechanism 96, and the hydraulic power mechanism 96 outputs power externally.
  • the hydraulic power mechanism 96 is in communication with the liquid working fluid returning system 97.
  • the end is connected; the hydraulic power mechanism 96 and the liquid working fluid return system 97 are controlled by a process control mechanism 98.
  • the gas working medium of the gas-liquid cylinder 91 has a pressure greater than the sum of the inertial forces of the liquid in the gas-liquid cylinder 91 and the gas-liquid isolation structure 92 when the gas-liquid isolation structure 92 is reciprocated.
  • the gas-liquid isolation structure 92 does not hit the cylinder head of the gas-liquid cylinder 91.
  • one of the piston type gas compression mechanism 9 and the piston type gas work mechanism 10 is set as the piston liquid mechanism 90 and its corresponding auxiliary means.
  • the internal combustion combustion chamber 3 may be a continuous combustion chamber or a intermittent combustion chamber, and when it is a batch combustion chamber, different intermittent combustion timing relationships may be selected as needed.
  • the mass flow rate of the substance discharged from the internal combustion combustion chamber 3 is greater than the mass flow rate of the substance introduced into the internal combustion combustion chamber 3 from outside the working fluid circuit; and the side internal combustion is included In the structure of the chamber 31, the mass flow rate of the working fluid flowing into the piston type gas working mechanism 10 is made larger than the mass flow rate of the substance discharged from the side internal combustion combustion chamber 31.
  • the pressure of the working fluid closed circuit may be set to be at least greater than 2 MPa; alternatively, the pressure bearing capacity of the working fluid closed circuit is set to be greater than 2.5 MPa, 3 MPa, 3.5.
  • the pressure bearing capacity of the oxidant source 4 and the fuel source 5 is also set to the same numerical range as described above. Due to the need to spray the oxidant source 4 or the substance in the fuel source 5 into the closed loop of the working fluid, The specification therefore applies in a practical application that the pressure bearing capacity of the oxidant source 4 or the fuel source 5 is generally set to be greater than the pressure bearing capacity of the working fluid closed circuit.

Abstract

A dual-conduit entropy-cycle engine, comprising: a piston-type gas-compression mechanism (9), a piston-type gas work mechanism (10), and two communication conduits (1). The working-medium outlet of the piston-type gas-compression mechanism (9) is in communication with the working-medium inlet of the piston-type gas work mechanism (10) via a communication conduit (1). The working-medium outlet of the piston-type gas work mechanism (10) is in communication with the working-medium inlet of the piston-type gas-compression mechanism (9) via the other communication conduit (1). The piston-type gas-compression mechanism (9) is in communication with the piston-type gas work mechanism (10) via the two communication conduits (1) in such a manner as to form a closed circuit for a working medium. A combustion chamber (3) is provided inside said closed circuit. A working-medium lead-out port (6) is provided on said closed circuit. The present dual-conduit entropy-cycle engine is highly efficient and conserves energy.

Description

说 明 书 双通道熵循环发动机 技术领域  Description Book Dual Channel Entropy Cycle Engine Technical Field
本发明涉及热能与动力领域, 尤其是一种热气机。  The invention relates to the field of thermal energy and power, and in particular to a hot air machine.
背景技术 Background technique
近年来, 传统内燃机的高能耗、 高污染排放问题日显突出, 所以, 热气机得到了广泛 重视, 然而热气机都是以外燃加热方式对工质进行加热的, 众所周知, 外燃加热过程很难 得到温度较高的工质, 因此, 造成大量化学佣损失。 不仅如此, 由于外燃加热的速率有限, 对材料要求高, 负荷响应差, 所以严重制约了热气机的单机功率和整机功率密度, 最终使 热气机的用途严重受限。 因此, 需要发明一种新型发动机。  In recent years, the problem of high energy consumption and high pollution emission of traditional internal combustion engines has become increasingly prominent. Therefore, hot air machines have received extensive attention. However, hot air machines are heated by external combustion heating methods. It is well known that external combustion heating processes are difficult. A higher temperature working fluid is obtained, thus causing a large amount of chemical labor loss. Not only that, because the rate of external combustion heating is limited, the material requirements are high, and the load response is poor, so the single machine power and the whole machine power density of the heat engine are severely restricted, and the use of the heat engine is severely limited. Therefore, it is necessary to invent a new type of engine.
发明内容 Summary of the invention
本发明提供了一种功率大、 功率密度高的双通道熵循环发动机, 解决了传统热气机因 工质的温度和压力难以被加热到应有的高度而影响功率和功率密度的问题。  The invention provides a dual-channel entropy cycle engine with high power and high power density, which solves the problem that the temperature and pressure of the conventional heat engine are difficult to be heated to the proper height and affect the power and power density.
本发明提出的技术方案如下:  The technical solution proposed by the present invention is as follows:
方案 1. 一种双通道熵循环发动机, 包括活塞式气体压缩机构、 活塞式气体做功机构和 两条连通通道, 所述活塞式气体压缩机构的工质出口经一条所述连通通道与所述活塞式气 体做功机构的工质入口连通, 所述活塞式气体做功机构的工质出口经另一条所述连通通道 与所述活塞式气体压缩机构的工质入口连通; 所述活塞式气体压缩机构经两条所述连通通 道与所述活塞式气体做功机构连通构成工质闭合回路; 在所述工质闭合回路内设内燃燃烧 室, 在所述工质闭合回路上设工质导出口。  A dual-channel entropy cycle engine includes a piston gas compression mechanism, a piston gas work mechanism, and two communication passages, and a working fluid outlet of the piston gas compression mechanism passes through the communication passage and the piston a working gas inlet of the gas working mechanism is connected, and a working medium outlet of the piston gas working mechanism is connected to a working medium inlet of the piston gas compression mechanism via another communication passage; the piston gas compression mechanism is The two communication passages are connected to the piston gas working mechanism to form a working fluid closed circuit; an internal combustion combustion chamber is disposed in the working fluid closed circuit, and a working fluid outlet is disposed on the working fluid closed circuit.
方案 2. 在方案 1的基础上, 进一步可选择的, 所述内燃燃烧室设在以所述活塞式气体 压缩机构的工质出口为上游和以所述活塞式气体做功机构的工质出口为下游的所述工质闭 合回路内。  According to the second aspect of the invention, further, the internal combustion combustion chamber is disposed at an outlet of the working fluid outlet of the piston type gas compression mechanism and a working outlet of the piston gas working mechanism. The downstream working fluid is closed in the circuit.
方案 3. 在方案 1或方案 2的基础上, 进一步可选择的, 将所述内燃燃烧室设为旁置内 燃燃烧室。  Solution 3. On the basis of the first or second aspect, the internal combustion combustion chamber is further set as a side internal combustion combustion chamber.
方案 4. 在方案 1的基础上,进一步可选择的,所述双通道熵循环发动机还包括冷却器, 所述冷却器设置在所述工质闭合回路上。  Solution 4. On the basis of the solution 1, the dual-channel entropy cycle engine further includes a cooler, and the cooler is disposed on the working fluid closed circuit.
方案 5. 在方案 4的基础上, 进一步可选择的, 所述双通道熵循环发动机还包括直连通 道, 所述直连通道连通所述活塞式气体做功机构的工质出口与所述活塞式压缩机构的工质 入口, 所述冷却器设置在所述直连通道上或设所述活塞式气体做功机构的工质出口与所述 活塞式气体压缩机构的工质入口之间的所述连通通道上, 在所述直连通道上和在所述活塞 式气体做功机构的工质出口与所述活塞式气体压缩机构的工质入口之间的所述连通通道上 设控制阔。  On the basis of the fourth aspect, the dual-channel entropy cycle engine further includes a direct connection channel, and the direct connection channel communicates with the working fluid outlet of the piston gas working mechanism and the piston type a working fluid inlet of the compression mechanism, the cooler being disposed on the direct connection passage or the communication between the working fluid outlet of the piston gas working mechanism and the working fluid inlet of the piston gas compression mechanism On the passage, a control width is provided on the direct passage and on the communication passage between the working fluid outlet of the piston gas working mechanism and the working fluid inlet of the piston gas compression mechanism.
方案 6. 在方案 4的基础上, 进一步可选择的, 所述双通道熵循环发动机还包括氧化剂 源, 所述冷却器设置在所述活塞式气体做功机构的工质出口与所述活塞式气体压缩机构工 说 明 书 质入口之间的所述连通通道上, 所述氧化剂源经氧化剂入口与所述冷却器与所述活塞式气 体压缩机构的工质入口之间的所述连通通道连通, 在所述冷却器和所述氧化剂入口之间的 所述连通通道上设冷却液体排出口, 在所述氧化剂入 和所述活塞式气体压缩机构之间的 所述连通通道上设液体二氧化碳出口。 On the basis of the fourth aspect, further optionally, the two-channel entropy cycle engine further includes an oxidant source, and the cooler is disposed at a working fluid outlet of the piston gas working mechanism and the piston gas Compression mechanism Said communication channel between said mass inlets, said oxidant source being in communication with said communication passage between said oxidant inlet and said cooler and said working inlet of said piston-type gas compression mechanism, said cooler The communication passage between the oxidant inlet and the oxidant inlet is provided with a cooling liquid discharge port, and a liquid carbon dioxide outlet is provided on the communication passage between the oxidant inlet and the piston type gas compression mechanism.
方案 7. 在方案 4的基础上, 进一步可选择的, 所述冷却器设在以所述活塞式气体做功 机构的工质出口为上游和以所述内燃燃烧室的工质入口为下游的所述工质闭合回路上。  According to the fourth aspect, further, the cooler is disposed upstream of the working fluid outlet of the piston gas working mechanism and downstream of the working fluid inlet of the internal combustion combustion chamber. The working fluid is closed on the circuit.
方案 8. 在方案 4的基础上, 进一步可选择的, 所述冷却器设为散热器、 气液直混冷却 器、 吸附式制冷器或非直混冷却器。  Scheme 8. On the basis of Scheme 4, further optionally, the cooler is configured as a radiator, a gas-liquid direct mixing cooler, an adsorption refrigerator or a non-direct mixer cooler.
方案 9. 在方案 8的基础上, 进一步可选择的, 所述双通道熵循环发动机还包括氧化剂 源, 所述氧化剂源经所述非直混冷却器的被加热流体通道与所述内燃燃烧室连通。  In a further aspect of the invention, the dual-channel entropy cycle engine further includes an oxidant source, the oxidant source passing through the heated fluid passage of the non-direct-mixing cooler and the internal combustion chamber Connected.
方案 10.在方案 8或方案 9的基础上, 进一步可选择的, 在所述非直混冷却器上设深 冷液体排出口。  Scheme 10. On the basis of the scheme 8 or the scheme 9, further optionally, a cryogenic liquid discharge port is provided on the non-direct mixer cooler.
方案 1 1. 在方案 4、 方案 5、 方案 7、 方案 8或方案 9的基础上, 进一步可选择的, 所 述双通道熵循环发动机还包括冷却液体排出口, 所述冷却液体排出口设在所述冷却器和所 述工质导出口之间的所述连通通道上。  According to the solution 4, the solution 5, the solution 7, the solution 8 or the solution 9, the dual-channel entropy cycle engine further includes a cooling liquid discharge port, and the cooling liquid discharge port is disposed at The communication passage between the cooler and the working fluid outlet.
方案 12. 在方案 1或方案 2的基础上, 进一步可选择的, 所述双通道熵循环发动机还 包括氧化剂源, 所述氧化剂源与所述工质闭合回路连通。  Scheme 12. Further, based on the scheme 1 or the scheme 2, the dual-channel entropy cycle engine further includes an oxidant source, and the oxidant source is in communication with the working fluid closed loop.
方案 13. 在方案 12的基础上,进一步可选择的,所述氧化剂源与所述内燃燃烧室连通。 方案 14. 在方案 12的基础上, 进一步可选择的, 所述熵循环发动机还包括直混冷凝冷 却器, 所述直混冷凝冷却器的被冷却流体入口与所述工质导出口连通, 所述氧化剂源与所 述直混冷凝冷却器的被加热流体入口连通, 并经所述直混冷凝冷却器的被加热流体出口与 所述工质闭合回路连通。  Scheme 13. Further based on the scheme 12, the oxidant source is in communication with the internal combustion chamber. On the basis of the scheme 12, further optionally, the entropy cycle engine further includes a direct mixing condensing cooler, wherein the cooled fluid inlet of the direct mixing condensing cooler is in communication with the working fluid outlet. The oxidant source is in communication with the heated fluid inlet of the direct mixing condensing cooler and is in communication with the working fluid closed circuit via the heated fluid outlet of the direct mixing condensing cooler.
方案 15. 在方案 14的基础上, 进一步可选择的, 所述氧化剂源经所述直混冷凝冷却器 的被加热流体出口与所述内燃燃烧室连通。  In a further aspect of the invention, the oxidant source is in communication with the internal combustion combustion chamber via a heated fluid outlet of the direct mixing condensing cooler.
方案 16. 在方案 12的基础上, 进一步可选择的, 所述氧化剂源的压力大于 2MPa。 方案 17. 在方案 2的基础上, 进一步可选择的, 所述工质导出口设在以所述活塞式气 体做功机构 (10 ) 的工质出口为上游和以所述内燃燃烧室的工质入口为下游的所述工质闭 合回路上。  Scheme 16. Based on Scheme 12, further optionally, the pressure of the oxidant source is greater than 2 MPa. According to the second aspect of the invention, further, the working fluid outlet is disposed upstream of the working fluid outlet of the piston gas working mechanism (10) and the working fluid of the internal combustion combustion chamber The inlet is closed on the downstream working fluid.
方案 18. 在方案 1 的基础上, 进一步可选择的, 所述双通道熵循环发动机还包括非直 混冷凝冷却器, 所述非直混冷凝冷却器的被冷却工质入口与所述工质导出口连通。  According to the first aspect, further, the dual-channel entropy cycle engine further includes a non-direct-mixing condensing cooler, the cooled working fluid inlet of the non-direct-mixing condensing cooler and the working fluid The outlet is connected.
方案 19. 在方案 14的基础上, 进一步可选择的, 所述直混冷凝冷却器上设深冷液体排 出口。  Scheme 19. Based on the scheme 14, further optionally, the direct mixing condensing cooler is provided with a cryogenic liquid discharge port.
方案 20. 在方案 18的基础上, 进一步可选择的, 所述非直混冷凝冷却器设深冷液体排 出口。  Scheme 20. Based on Scheme 18, further optionally, the non-direct mixing condensing cooler is provided with a cryogenic liquid discharge port.
方案 21. 在方案 19或方案 20的基础上, 进一步可选择的, 所述双通道熵循环发动机 说 明 书 还包括深冷液体工质储罐, 所述深冷液体工质储罐与所述深冷液体排出口连通。 Scheme 21. Based on the scheme 19 or the scheme 20, further optionally, the dual channel entropy cycle engine The description also includes a cryogenic liquid working fluid storage tank in communication with the cryogenic liquid discharge port.
方案 22. 在方案 14的基础上,进一步可选择的,所述直混冷凝冷却器上设不凝气出口。 方案 23. 在方案 18的基础上,进一步可选择的,所述非直混冷凝冷却器设不凝气出口。 方案 24. 在方案 22或方案 23的基础上, 进一步可选择的, 所述不凝气出口与所述工 质闭合回路连通。  Scheme 22. Based on the scheme 14, further optionally, the direct mixing condensing cooler is provided with a non-condensing gas outlet. Scheme 23. On the basis of the scheme 18, further optionally, the non-direct mixing condensing cooler is provided with a non-condensing gas outlet. Scheme 24. On the basis of Option 22 or Scheme 23, further optionally, the non-condensable gas outlet is in communication with the closed circuit of the working fluid.
方案 25. 在方案 18的基础上, 进一步可选择的, 所述熵循环发动机还包括氧化剂源, 所述氧化剂源经所述非直混冷凝冷却器的被加热流体通道与所述内燃燃烧室连通。  In a further aspect, the entropy cycle engine further includes an oxidant source, the oxidant source being in communication with the internal combustion combustion chamber via a heated fluid passage of the non-direct mixing condensing cooler .
方案 26. 在方案 1的基础上, 进一步可选择的, 在所述工质导出口上设控制阀。  Scheme 26. On the basis of Option 1, a control valve is further provided on the working fluid outlet.
方案 27. 在方案 26的基础上, 进一步可选择的, 所述控制阀设为压力控制阔, 所述压 力控制阀控制所述工质导出口在所述工质闭合回路内的压力超过设定限度时导出工质。  According to the solution 26, further, the control valve is set to be pressure controlled, and the pressure control valve controls the pressure of the working fluid outlet in the closed loop of the working fluid to exceed a set value. The working fluid is exported when the limit is reached.
方案 28. 在方案 26的基础上, 进一步可选择的, 所述压力控制阀受使所述工质闭合回 路中的最低压力大于 0.2MPa的控制机构控制。  Solution 28. On the basis of the solution 26, further optionally, the pressure control valve is controlled by a control mechanism that causes a minimum pressure in the working fluid closed circuit to be greater than 0.2 MPa.
方案 29. 在方案 26的基础上, 进一步可选择的, 所述控制阀受开启度控制机构控制, 所述开启度控制机构根据所述工质闭合回路内的压力设定范围控制所述控制阀的开启度, 使所述工质导出口在某种开启度下处于常开状态。  On the basis of the solution 26, further optionally, the control valve is controlled by an opening degree control mechanism, and the opening degree control mechanism controls the control valve according to a pressure setting range in the working fluid closed circuit. The degree of opening allows the working fluid outlet to be in a normally open state at a certain degree of opening.
方案 30. 在方案 1或方案 17的基础上, 进一步可选择的, 所述双通道熵循环发动机还 包括附属气体做功机构, 所述工质导出口与所述附属气体做功机构的工质入口连通。  According to the first aspect or the seventh aspect, the dual-channel entropy cycle engine further includes an auxiliary gas working mechanism, and the working fluid outlet is connected to the working fluid inlet of the auxiliary gas working mechanism. .
方案 31. 在方案 1或方案 17的基础上, 进一步可选择的, 所述双通道熵循环发动机还 包括储气罐, 所述储气罐与所述工质导出口连通。  According to the first aspect or the seventh aspect, the two-channel entropy cycle engine further includes a gas storage tank, and the gas storage tank is in communication with the working fluid outlet.
方案 32. 在方案 1的基础上, 进一步可选择的, 在所述连通通道上设逆止阀。  Solution 32. On the basis of the solution 1, further optionally, a check valve is arranged on the communication passage.
方案 33. 在方案 1 的基础上, 进一步可选择的, 在以所述活塞式气体做功机构的工质 出口为上游、 以所述活塞式气体压缩机构的工质入口为下游的所述工质闭合回路上设另一 个活塞式气体做功机构。  The solution 33 is further selected, wherein the working fluid outlet of the piston gas working mechanism is upstream and the working fluid inlet of the piston gas compression mechanism is downstream. Another piston gas working mechanism is arranged on the closed circuit.
方案 34. 在方案 1或方案 33的基础上, 进一步可选择的, 所述活塞式气体做功机构对 所述活塞式气体压缩机构输出动力。  Solution 34. On the basis of the first or the third aspect, the piston gas working mechanism further outputs power to the piston gas compression mechanism.
方案 35. 在方案 1 的基础上, 进一步可选择的, 所述工质闭合回路中, 参与循环的气 体的一部分为不凝气。  Scheme 35. On the basis of the scheme 1, further optionally, in the closed circuit of the working fluid, a part of the gas participating in the circulation is non-condensable.
方案 36. 在方案 35的基础上, 进一步可选择的, 所述双通道熵循环发动机还包括不凝 气储罐, 所述不凝气储罐经控制装置与所述工质闭合回路连通。  The solution 36 is further optional. The dual-channel entropy cycle engine further includes a non-condensable storage tank, and the non-condensable storage tank is connected to the working fluid closed circuit via a control device.
方案 37. 在方案 36的基础上, 进一步可选择的, 所述双通道熵循环发动机还包括不凝 气回储压缩机, 所述不凝气回储压缩机的进气口与所述工质闭合回路连通, 所述不凝气回 储压缩机的气体出口与所述不凝气储罐连通。  In a further aspect, the dual-channel entropy cycle engine further includes a non-condensable gas returning compressor, the air inlet of the non-condensing gas returning compressor and the working fluid The closed loop is in communication, and the gas outlet of the non-condensable gas returning compressor is in communication with the non-condensable gas storage tank.
方案 38. 在方案 1的基础上, 进一步可选择的, 在所述工质闭合回路内设三元催化器。 方案 39. 在方案 1 的基础上, 进一步可选择的, 所述活塞式气体压缩机构的气缸中心 线和所述活塞式气体做功机构的气缸中心线之间的夹角小于 180度, 所述活塞式气体压缩 说 明 书 机构的活塞和所述活塞式气体做功机构的活塞分别经连杆与同一曲轴的同一连杆轴颈连 接。 Scheme 38. Based on the scheme 1, further optionally, a three-way catalyst is disposed in the closed loop of the working fluid. According to the solution 1, further, the angle between the cylinder center line of the piston gas compression mechanism and the cylinder center line of the piston gas working mechanism is less than 180 degrees, the piston Gas compression The piston of the book mechanism and the piston of the piston gas working mechanism are respectively connected to the same connecting rod journal of the same crankshaft via a connecting rod.
方案 40. 在方案 39的基础上, 进一步可选择的, 所述活塞式气体压缩机构的气缸中心 线和所述活塞式气体做功机构的气缸中心线之间的夹角为 90度。  Solution 40. Based on the solution 39, further optionally, an angle between a cylinder center line of the piston type gas compression mechanism and a cylinder center line of the piston gas working mechanism is 90 degrees.
方案 41. 在方案 1 的基础上, 进一步可选择的, 所述活塞式气体压缩机构的活塞和所 述活塞式气体做功机构的活塞分别经连杆与同一曲轴上的不同连杆轴颈连接, 两个所述连 杆轴颈的相位差大于 0度小于 180度。  On the basis of the first aspect, the piston of the piston type gas compression mechanism and the piston of the piston type gas working mechanism are respectively connected to the different connecting rod journals on the same crankshaft via a connecting rod. The phase difference between the two connecting rod journals is greater than 0 degrees and less than 180 degrees.
方案 42. 在方案 1 的基础上, 进一步可选择的, 所述双通道熵循环发动机还包括低温 冷源, 所述低温冷源用于提供低温物质, 所述低温物质用于冷却所述活塞式气体压缩机构 中或即将进入所述活塞式气体压缩机构的工质。  In a further aspect, the dual-channel entropy cycle engine further includes a low-temperature cold source for providing a low-temperature substance, and the low-temperature substance is used for cooling the piston type. The working fluid in the gas compression mechanism or about to enter the piston gas compression mechanism.
方案 43. 在方案 1 的基础上, 进一步可选择的, 所述双通道熵循环发动机还包括涡轮 动力机构和叶轮压气机, 所述工质导出口与所述涡轮动力机构的工质入口连通, 所述涡轮 动力机构的工质出口经附属冷却器与所述叶轮压气机的工质入口连通, 所述叶轮压气机的 工质出口与所述工质闭合回路连通; 所述涡轮动力机构的工质出口与所述叶轮压气机的工 质入口之间的通道上设附属工质导出口。  On the basis of the first aspect, the dual-channel entropy cycle engine further includes a turbine power mechanism and an impeller compressor, and the working fluid outlet is connected to the working fluid inlet of the turbine power mechanism. The working fluid outlet of the turbine power mechanism is connected to the working fluid inlet of the impeller compressor via an auxiliary cooler, and the working fluid outlet of the impeller compressor is in communication with the working fluid closed circuit; An auxiliary working fluid outlet is disposed on the passage between the mass outlet and the working fluid inlet of the impeller compressor.
方案 44. 在方案 1 的基础上, 进一步可选择的, 所述双通道熵循环发动机还包括四类 门气缸活塞机构, 所述四类门气缸活塞机构的供气口与所述工质闭合回路连通, 所述四类 门气缸活塞机构的回充口与所述工质导出口连通。  According to the solution 1, further, the dual-channel entropy cycle engine further includes a four-type door cylinder piston mechanism, and the air supply port of the four-type door cylinder piston mechanism and the working fluid closed circuit In communication, the refill port of the four-type door cylinder piston mechanism is in communication with the working fluid outlet.
方案 45. 在方案 44的基础上, 进一步可选择的, 所述双通道熵循环发动机还包括氧化 剂源, 所述氧化剂源设为所述四类门气缸活塞机构。  Scheme 45. Based on the scheme 44, further optionally, the dual channel entropy cycle engine further includes an oxidant source, and the oxidant source is configured as the four types of door cylinder piston mechanism.
方案 46. 在方案 3的基础上, 进一步可选择的, 所述旁置内燃燃烧室设为四类门气缸 活塞机构, 所述四类门气缸活塞机构的供气口与所述活塞式气体做功机构的气缸连通, 所 述四类门气缸活塞机构的回充口与所述工质导出口连通。  According to the solution 3, further, the side internal combustion combustion chamber is set as a four-type door cylinder piston mechanism, and the air supply port of the four types of door cylinder piston mechanism and the piston gas work The cylinders of the mechanism are in communication, and the refilling port of the four types of door cylinder piston mechanisms is in communication with the working fluid outlet.
方案 47. 在方案 12的基础上, 进一步可选择的, 所述双通道熵循环发动机还包括氧化 剂传感器和氧化剂控制装置, 所述氧化剂传感器设在所述工质闭合回路内, .所述氧化剂传 感器对所述氧化剂控制装置提供信号, 所述氧化剂源经氧化剂控制阀与所述工质闭合回路 连通, 所述氧化剂控制装置控制所述氧化剂控制阀。  In a further aspect, the dual-channel entropy cycle engine further includes an oxidant sensor and an oxidant control device, the oxidant sensor being disposed in the working fluid closed circuit, the oxidant sensor A signal is provided to the oxidant control device, the oxidant source being in communication with the working fluid closed circuit via an oxidant control valve, the oxidant control device controlling the oxidant control valve.
方案 48. 在方案 1 的基础上, 进一步可选择的, 所述活塞式气体压缩机构设为活塞液 体机构, 所述活塞液体机构包括气液缸和气液隔离结构, 所述气液隔离结构设在所述气液 缸内。  According to the first aspect, the piston gas compression mechanism is further configured as a piston liquid mechanism, and the piston liquid mechanism comprises a gas liquid cylinder and a gas-liquid isolation structure, wherein the gas-liquid isolation structure is Inside the gas-liquid cylinder.
方案 49. 在方案 1 的基础上, 进一步可选择的, 所述活塞式气体做功机构设为活塞液 体机构, 所述活塞液体机构包括气液缸和气液隔离结构, 所述气液隔离结构设在所述气液 缸内。  According to the solution 1, further, the piston gas working mechanism is set as a piston liquid mechanism, and the piston liquid mechanism comprises a gas liquid cylinder and a gas-liquid isolation structure, wherein the gas-liquid isolation structure is Inside the gas-liquid cylinder.
方案 50. 在方案 48或方案 49的基础上, 进一步可选择的, 所述气液缸的气体工质对 所述气液隔离结构的压力大于所述气液缸内的液体和所述气液隔离结构做往复运动时的惯 说 明 书 性力之和。 In a further aspect, the gas working fluid of the gas-liquid cylinder has a pressure greater than the liquid in the gas-liquid cylinder and the gas-liquid liquid. Isolation of the isolation structure when doing reciprocating motion Explain the sum of the power of the book.
方案 51. 在方案 1 的基础上, 进一步可选择的, 所述内燃燃烧室排出的物质的质量流 量大于从所述工质闭合回路外导入所述内燃燃烧室的物质的质量流量。  In a further aspect, based on the solution 1, the mass flow rate of the substance discharged from the internal combustion combustion chamber is greater than the mass flow rate of the substance introduced into the internal combustion combustion chamber from outside the closed circuit of the working medium.
方案 52. 在方案 3的基础上, 进一步可选择的, 流入所述活塞式气体做功机构的工质 的质量流量大于所述旁置内燃燃烧室排出的物质的质量流量。  Scheme 52. On the basis of the scheme 3, further, the mass flow rate of the working fluid flowing into the piston gas working mechanism is greater than the mass flow rate of the material discharged from the bypass internal combustion combustion chamber.
方案 53. 在方案 1 的基础上, 进一步可选择的, 所述工质闭合回路的承压能力大于 2MPa。  Programme 53. On the basis of Option 1, furthermore, the pressure-bearing capacity of the closed loop of the working fluid is greater than 2 MPa.
方案 54. 在方案 1 的基础上, 进一步可选择的, 在所述连通通道上设回热器, 所述活 塞式气体做功机构的工质出口与所述活塞式气体压缩机构的工质入口之间的所述连通通道 设为所述回热器的被冷却流体通道, 所述活塞式气体压缩机构的工质出口与所述活塞式气 体做功机构的工质入口之间的所述连通通道设为所述回热器的被加热流体通道。  According to the solution 1, further, optionally, a regenerator is disposed on the communication passage, a working fluid outlet of the piston gas working mechanism and a working fluid inlet of the piston gas compression mechanism The communication passage between the two is set as the cooled fluid passage of the regenerator, and the communication passage between the working fluid outlet of the piston type gas compression mechanism and the working fluid inlet of the piston gas working mechanism is It is the heated fluid passage of the regenerator.
方案 55. 在方案 1 的基础上, 进一步可选择的, 所述内燃燃烧室以独立腔体的形式设 置在所述连通通道内。  Solution 55. On the basis of the solution 1, further optionally, the internal combustion combustion chamber is disposed in the communication passage in the form of a separate cavity.
本发明的原理是: 用所述内燃燃烧室 (即向需要进行加热的热气机的工质内导入氧化 剂、 燃料并使其发生燃烧化学反应, 进而提高工质的温度) 取代传统热气机 (包括斯特林 发动机等所有类型的热气机) 的工质加热热交换器, 从而使工质的温度和压力可以达到更 高的水平, 实现热气机效率和功率密度的本质性提高, 而且可以大幅度减少机构的体积、 重量和制造成本。  The principle of the present invention is: replacing the conventional hot air machine with the internal combustion combustion chamber (that is, introducing an oxidant, a fuel into a working fluid of a hot air machine that needs to be heated, and causing a combustion chemical reaction to increase the temperature of the working medium) The working fluid of all types of hot air compressors such as Stirling engine heats the heat exchanger, so that the temperature and pressure of the working fluid can reach a higher level, achieving the essential improvement of the efficiency and power density of the hot air machine, and can be greatly improved. Reduce the size, weight and manufacturing costs of the mechanism.
利用所述内燃燃烧室对所述工质闭合回路内的工质进行内燃加热, 推动活塞式气体做 功机构的活塞对外做功, 通过将部分工质从所述工质闭合回路内导出实现所述工质闭合回 路内工质平衡, 在将所述工质闭合回路内的工质导出的过程的同时可导出部分热量; 本发 明中所述冷却器和回热器的作用与传统斯特林发动机中的冷却器和回热器的作用相同; 本 发明中所述冷凝冷却器的作用是将闭合回路中的部分工质进行冷凝液化, 以液体的形式从 所述工质闭合回路中导出, 这样不仅可以实现所述工质闭合回路内工质平衡, 也可以实现 不向环境排放气体的作用, 形成发动机整体零排放。  Using the internal combustion combustion chamber to perform internal combustion heating on the working fluid in the closed circuit of the working fluid, and pushing the piston of the piston gas working mechanism to perform external work, and realizing the work by guiding part of the working fluid from the closed loop of the working fluid In the closed loop, the working medium is balanced, and part of the heat can be derived while the working fluid in the closed circuit of the working fluid is derived; the function of the cooler and the regenerator in the present invention is compared with the traditional Stirling engine The function of the chiller and the regenerator is the same; the function of the condensing cooler in the present invention is to condense and liquefy part of the working fluid in the closed circuit, and to export it from the closed loop of the working fluid in the form of liquid, so that The working medium balance in the closed circuit of the working fluid can be realized, and the function of not discharging the gas to the environment can be realized, and the overall zero emission of the engine is formed.
本发明中, 所谓的附属气体做功机构是指一切可以利用气体工质膨胀和 /或流动产生动 力的机构, 例如活塞式气体做功机构、 叶轮式气体做功机构、 罗茨式气体做功机构等, 其 作用是利用所述双通道熵循环发动机内的处于高能状态下的气体工质进行做功。  In the present invention, the so-called accessory gas work mechanism refers to any mechanism that can generate power by gas working fluid expansion and/or flow, such as a piston gas work mechanism, an impeller gas work mechanism, a Roots gas work mechanism, etc. The function is to perform work by using the gas working medium in the high energy state in the two-channel entropy cycle engine.
本发明中, 所谓的连通通道是指连通所述活塞式气体压缩机构和所述活塞式气体做功 机构的工质流动的通道。  In the present invention, the so-called communication passage means a passage through which the working fluid of the piston type gas compression mechanism and the piston type gas working mechanism communicate.
本发明中, 所述工质闭合回路内的工质可以是氧化剂和燃料燃烧形成的烟气, 也可以 是烟气与事先存入的其它气体的混合物, 例如烟气与氦气的混合物、 烟气与氩气的混合物 等。  In the present invention, the working fluid in the closed circuit of the working fluid may be a flue gas formed by the combustion of the oxidant and the fuel, or a mixture of the flue gas and other gases previously stored, such as a mixture of flue gas and helium, and smoke. a mixture of gas and argon, and the like.
本发明中, 所述工质闭合回路是指工质可在所述活塞式气体压缩机构和所述活塞式气 体做功机构以及连通两者的所述连通通道中循环流动的空间。 说 明 书 本发明中, 所述内燃燃烧室是指氧化剂和燃料发生燃烧化学反应后所形成的高温产物 直接作为循环工质或与所述工质闭合回路内事先存在的其它气体混合后作为循环工质的燃 烧室。 In the present invention, the working fluid closed circuit refers to a space in which the working fluid can circulate in the communication passage of the piston type gas compression mechanism and the piston type gas work mechanism and the communication. In the present invention, the internal combustion combustion chamber means that the high temperature product formed by the combustion chemical reaction between the oxidant and the fuel is directly used as a circulating working medium or mixed with other gases existing in the closed circuit of the working fluid as a circulating working medium. The combustion chamber.
本发明中, 所述 "工质闭合回路内设内燃燃烧室"包括将所述内燃燃烧室直接设置在 所述工质闭合回路内, 也包括所述内燃燃烧室的高温燃烧产物的出 u与所述工质闭合回路 连通的结构, 即旁置内燃燃烧室结构。  In the present invention, the "internal combustion combustion chamber in the working fluid closed circuit" includes directly arranging the internal combustion combustion chamber in the working fluid closed circuit, and also includes the high temperature combustion product of the internal combustion combustion chamber. The structure in which the working fluid is closed in a loop, that is, the structure of the side-by-side internal combustion combustor.
本发明中, 所述旁置内燃燃烧室是指内燃燃烧室设为采用通道与所述工质闭合回路连 通的独立燃烧空间。  In the present invention, the side-by-side internal combustion combustion chamber means that the internal combustion combustion chamber is an independent combustion space in which a passage is connected to the working fluid closed circuit.
本发明中, 所述内燃燃烧室可以设为内燃连续燃烧室、 内燃间歇燃烧室或内燃正时燃 烧室; 所述内燃连续燃烧室是指其内可以连续发生放热化学反应的内燃燃烧室; 所述内燃 间歇燃烧室是指非连续发生放热化学反应的内燃燃烧室, 所述内燃间歇燃烧室可以是正时 间歇燃烧室, 所述双通道熵循环发动机的每个工作循环中燃烧室内只发生一次放热化学反 应, 放热化学反应只在一个冲程内发生; 或者可以是正时长间歇燃烧室, 所述双通道熵循 环发动机多个工作循环中燃烧室内发生一次放热化学反应: 或者可以是长正时间歇燃烧室, 所述双通道熵循环发动机连续的多个工作循环中燃烧室连续发生放热化学反应。  In the present invention, the internal combustion combustion chamber may be an internal combustion continuous combustion chamber, an internal combustion intermittent combustion chamber or an internal combustion timing combustion chamber; the internal combustion continuous combustion chamber refers to an internal combustion combustion chamber in which an exothermic chemical reaction may continuously occur; The internal combustion intermittent combustion chamber refers to an internal combustion combustion chamber that does not continuously generate an exothermic chemical reaction, and the internal combustion intermittent combustion chamber may be a timing intermittent combustion chamber, and only occurs in the combustion chamber in each working cycle of the two-channel entropy circulation engine. An exothermic chemical reaction, the exothermic chemical reaction occurs only in one stroke; or may be a positive-time intermittent combustion chamber in which an exothermic chemical reaction occurs in a plurality of working cycles: or may be long In the timing intermittent combustion chamber, the two-channel entropy cycle engine continuously generates an exothermic chemical reaction in the combustion chamber in a plurality of working cycles.
本发明中, 所谓的氧化剂源是指可以提供氧化剂的装置、 机构或储罐, 所述氧化剂源 中的氧化剂在进入所述内燃燃烧室时, 其压力应高于所述内燃燃烧室内的压力。  In the present invention, the term "oxidant source" means a device, mechanism or storage tank which can supply an oxidant, and the oxidant in the oxidant source should have a higher pressure than the pressure in the internal combustion combustion chamber when entering the internal combustion combustion chamber.
本发明中, 所述氧化剂是指液态或高压气态的能与燃料发生燃烧化学反应的物质, 例 如液氧、 高压氧气、 高压压縮空气、 液化空气、 双氧水、 双氧水溶液等。 当所述氧化剂是 液态时, 需通过高压液体泵供送; 当所述氧化剂是高压气态时, 可直接以高压形式送入。  In the present invention, the oxidizing agent refers to a substance which can react with a fuel in a liquid or high-pressure gas state, such as liquid oxygen, high-pressure oxygen, high-pressure compressed air, liquefied air, hydrogen peroxide, aqueous hydrogen peroxide, and the like. When the oxidant is in a liquid state, it is supplied by a high pressure liquid pump; when the oxidant is in a high pressure gas state, it can be directly fed in a high pressure form.
本发明中, 应根据公知技术不仅向所述内燃燃烧室提供氧化剂还应向所述内燃燃烧室 提供燃料。 所述燃料源是指可以提供燃料的装置、 机构或储罐, 所述燃料源中的燃料在进 入所述内燃燃烧室时, 其压力应高于所述内燃燃烧室内的压力, 所述燃料是指能与氧化剂 发生燃烧化学反应的物质, 例如碳氢化合物、 碳氢氧化合物或固体碳等; 其中所述碳氢化 合物包括汽油、 柴油、 重油、 煤油、 航空煤油等其它烃类; 所述碳氢氧化合物包括甲醇、 乙醇、 甲醚、 乙醚等; 固体碳具有燃烧后没有水生成和燃烧后产物中的二氧化碳浓度高, 易液化等优点; 固体碳可采用固体预先装配、 粉末化后喷入或粉末化后再用液体或气体二 氧化碳流化后喷入的方式输入热气机。  In the present invention, not only the oxidant should be supplied to the internal combustion combustion chamber but also the internal combustion combustion chamber should be supplied with fuel according to known techniques. The fuel source refers to a device, a mechanism or a storage tank that can provide fuel, and when the fuel in the fuel source enters the internal combustion combustion chamber, the pressure thereof should be higher than the pressure in the internal combustion combustion chamber, and the fuel is a substance capable of undergoing a combustion chemical reaction with an oxidant, such as a hydrocarbon, a carbon oxyhydroxide or a solid carbon; wherein the hydrocarbon includes gasoline, diesel, heavy oil, kerosene, aviation kerosene, and the like; The hydroxide includes methanol, ethanol, methyl ether, diethyl ether, etc.; the solid carbon has the advantages of high concentration of carbon dioxide in the product after combustion and combustion, and is easy to liquefy; the solid carbon can be pre-assembled, powdered and injected into the solid. Or powdered, and then injected into the hot air machine by fluidization of liquid or gaseous carbon dioxide.
本发明中, 所谓的工质导出口是指从所述双通道熵循环发动机工质系统中导出部分工 质的出口, 其目的是为了平衡导入的氧化剂和还原剂发生燃烧化学反应所产生的多余的工 质, 以维持所述双通道熵循环发动机工质系统的平衡。  In the present invention, the so-called working fluid outlet refers to the outlet of a part of the working fluid from the two-channel entropy circulating engine working fluid system, the purpose of which is to balance the excess of the introduced oxidant and reducing agent. The working fluid to maintain the balance of the dual channel entropy cycle engine working fluid system.
本发明中, 所述工质导出口可以是连续导出工质, 可以是间歇导出工质 (即根据工质 在所述工质闭合回路内积累的情况, 对工质进行导出), 也可以是按正时关系对工质进行导 出。  In the present invention, the working fluid outlet may be a continuous derivation working medium, and may be an intermittent derivation working medium (that is, the working medium is derivatized according to the working medium accumulated in the closed circuit of the working medium), or may be The working fluid is exported according to the timing relationship.
本发明中, 导出工质可以是在所述双通道熵循环发动机每个工作循环中、 工质导出口 说 明 书 处压力较低的时候导出一次工质; 还可以是正时导出工质, 间歇式地在所述双通道熵循环 发动机进行多个工作循环后在工质导出口处压力低的时候导出一次工质; 还可以采用限压 阔等压力控制装置在所述工质闭合回路内压力超过某设定限度的时候导出工质。 In the present invention, the derived working medium may be in each working cycle of the two-channel entropy cycle engine, the working fluid outlet When the pressure at the specification is low, the working medium is exported; or the working medium is derived at the timing, and the working is performed intermittently after the working pressure is low at the working outlet of the two-channel entropy cycle engine after multiple working cycles It is also possible to use a pressure limiting device such as a pressure limiting valve to derive the working medium when the pressure in the working fluid closed circuit exceeds a certain limit.
本发明中, 在所述工质导出口上设的控制阀: 所述控制阀受峰压控制机构控制, 所述 峰压控制机构在所述工质闭合回路内的压力超过设定值时使所述控制阔开启, 并当所述闭 合回路内的压力回降到所述设定值时使所述控制阀关闭; 或所述控制阀受谷压控制机构控 制, 在所述工质闭合回路内的压力处于谷压状态时使所述控制阀开启, 并当所述工质闭合 回路内的压力将至 0.2MPa时使所述控制阔关闭; 或所述控制阀受开启度控制机构控制, 所 述开启度控制机构根据所述工质闭合回路内的压力设定范围控制所述控制阀的开启度, 使 所述工质导出口在某种开启度下处于常开状态。  In the present invention, a control valve is provided on the working fluid outlet: the control valve is controlled by a peak pressure control mechanism, and the peak pressure control mechanism causes the pressure in the closed circuit of the working fluid to exceed a set value The control is wide open, and the control valve is closed when the pressure in the closed circuit drops back to the set value; or the control valve is controlled by the valley pressure control mechanism, and the working fluid is closed The control valve is opened when the pressure inside is in the valley pressure state, and the control is closed when the pressure in the working fluid closed circuit is to 0.2 MPa; or the control valve is controlled by the opening degree control mechanism, The opening degree control mechanism controls the opening degree of the control valve according to the pressure setting range in the working fluid closed circuit, so that the working fluid outlet is in a normally open state under a certain opening degree.
本发明中, 导出所述工质闭合回路内的工质可以以气体的形式导出也可以以液体的形 式导出。  In the present invention, the working fluid in the closed loop of the working fluid may be derived in the form of a gas or may be derived in the form of a liquid.
本发明中, 与所述工质导出口连通的所述储气罐可作为压缩气体源使用。  In the present invention, the gas storage tank that communicates with the working fluid outlet can be used as a compressed gas source.
本发明中, 所述冷却器是指一切能使工质冷却的装置, 例如直混式、 热交换器式和散 热器式冷却器。 所述直混式冷却器是指将被加热流体与被冷却工质直接混合, 两者直接进 行热交换而达到工质冷却的装置; 所述热交换器是指采用其它流体做热的接受介质, 与工 质进行热交换达到冷却工质的装置; 所述散热器是采用环境气体作为热接受介质, 使工质 热量扩散至环境中, 达到冷却工质的装置。 其中所述热交换器和所述散热器均属于非直混 式冷却器, 即被加热流体与被冷却工质不混合。  In the present invention, the cooler refers to any device capable of cooling the working fluid, such as a direct mixing type, a heat exchanger type, and a radiator type cooler. The direct-mixing cooler refers to a device that directly mixes a heated fluid with a cooled working fluid, and directly performs heat exchange to achieve working fluid cooling; the heat exchanger refers to a receiving medium that uses other fluids as heat. And a device for performing heat exchange with the working medium to reach a cooling medium; the heat sink is a device that uses an ambient gas as a heat receiving medium to diffuse the heat of the working medium into the environment to reach a cooling working medium. Wherein the heat exchanger and the heat sink are both non-direct mixed coolers, that is, the heated fluid is not mixed with the cooled working medium.
本发明中, 所述冷凝冷却器包括直混冷凝冷却器和非直混冷凝冷却器, 所述直混冷凝 冷却器是指被加热流体和被冷却流体在其中混合, 使被冷却流体发生部分或全部冷凝, 使 被加热流体升温的装置; 所述非直混冷凝冷却器是指具有被加热流体通道和被冷却流体通 道, 所述被加热流体通道中的被加热流体和所述被冷却流体通道内的被冷却流体在其中发 生热量交换但不进行混合的装置, 例如热交换器式和散热器式冷凝冷却器; 所述非直混冷 凝冷却器和直混冷凝冷却器在必要的时候可以具有气液分离器的功能。  In the present invention, the condensing cooler comprises a direct mixing condensing cooler and a non-direct mixing condensing cooler, wherein the straight mixed condensing cooler means that the heated fluid and the cooled fluid are mixed therein to cause a portion of the cooled fluid to be generated or a device that condenses all of the temperature to heat the heated fluid; the non-direct mixed condensing cooler means having a heated fluid passage and a cooled fluid passage, the heated fluid in the heated fluid passage and the cooled fluid passage Means in which the cooled fluid is subjected to heat exchange but not mixed, such as a heat exchanger type and a radiator type condensing cooler; the non-direct mixed condensing cooler and the direct mixing condensing cooler may have when necessary The function of the gas-liquid separator.
本发明中, 所述工质闭合回路中的循环气体可以选自氩气、 氦气、 氧气等气体。  In the present invention, the circulating gas in the working fluid closed circuit may be selected from the group consisting of argon gas, helium gas, oxygen gas and the like.
本发明中, 所谓的不凝气是指惰性气体、 氮气等在所述双通道熵循环发动机中经冷却 后不液化的气体, 优选的所述不凝气为氩气。  In the present invention, the term "non-condensable gas" means a gas which is not liquefied after being cooled in the two-channel entropy cycle engine by an inert gas, nitrogen gas or the like, and preferably the non-condensable gas is argon gas.
本发明中, 设置所述不凝气回储压缩机的作用是, 当系统不工作时, 将不凝气从所述 工质闭合回路中抽出, 并存储在所述不凝气储罐中。  In the present invention, the function of providing the non-condensable gas returning compressor is to extract non-condensable gas from the working fluid closed circuit and store it in the non-condensable gas storage tank when the system is not operating.
本发明中, 所述低温冷源是指能提供温度在 0°C以下的低温物质的装置、 机构或储罐, 例如采用商业购买方式获得的储存有低温物质的储罐, 所述低温物质可以是液氮、 液氧、 液氦或液化空气等。 当本发明中氧化剂为液氧时, 液氧可直接作为所述低温物质。  In the present invention, the low-temperature cold source refers to a device, a mechanism or a storage tank capable of providing a low-temperature substance having a temperature below 0 ° C, for example, a storage tank stored with a low-temperature substance obtained by a commercially available method, the low-temperature substance may be It is liquid nitrogen, liquid oxygen, liquid helium or liquefied air. When the oxidizing agent in the present invention is liquid oxygen, liquid oxygen can be directly used as the low temperature substance.
本发明中, 所述低温冷源以直接与所述工质闭合回路连通使所述低温物质与所述工质 闭合回路内的工质混合的方式, 或者以经换热装置使所述低温物质与所述工质闭合回路内 的工质换热的方式, 对所述活塞式气体压缩机构中或即将进入所述活塞式气体压缩机构的 工质进行冷却处理。 所述双通道熵循环发动机是一种工作循环接近卡诺循环的动力机构, 其热效率的计算可以参考卡诺循环热效率计算公式: β = ' 从中可知, 当冷源温度7 下降时, 热效率 升高, 而且向冷源排放的热量减少, 如果冷源温度 ^下降幅度很大, 即冷 源温度很低, 则热效率77很高, 向冷源排放的热量很小。 由此推断, 可用温度相当低的低温 物质使冷源温度7^大幅下降, 从而大幅减少向冷源排放的热量, 有效提高发动机效率。 In the present invention, the low-temperature cold source is directly connected to the working fluid closed circuit to mix the low-temperature substance with the working medium in the working fluid closed circuit, or to make the low-temperature substance through a heat exchange device In the closed loop with the working fluid The working medium heat exchange mode cools the working fluid in the piston type gas compression mechanism or is about to enter the piston type gas compression mechanism. The two-channel entropy cycle engine is a power mechanism with a working cycle close to the Carnot cycle. The calculation of the thermal efficiency can refer to the calculation formula of the Carnot cycle thermal efficiency: β = ' It can be seen that when the temperature of the cold source 7 decreases, the thermal efficiency increases. Moreover, the amount of heat discharged to the cold source is reduced. If the temperature of the cold source is greatly decreased, that is, the temperature of the cold source is low, the thermal efficiency 77 is high, and the amount of heat discharged to the cold source is small. It is inferred that the cold source temperature 7 ^ can be greatly reduced by using a relatively low temperature low temperature substance, thereby greatly reducing the amount of heat discharged to the cold source and effectively improving the engine efficiency.
温度越低的低温物质(例如液氧、液氮或液氦等),在制造过程中需要消耗越多的能量, 但是就单位质量而言,对发动机热说效率 提升的贡献越大, 就好比将能量存储在温度很低的 物质中, 相当于一种新型电池的概念, 所述低温物质可以使用垃圾电等成本很低的能源来 制造, 从而有效降低发动机的使用成本。  The lower the temperature, the lower the temperature (such as liquid oxygen, liquid nitrogen or liquid helium), the more energy is consumed in the manufacturing process, but in terms of unit mass, the contribution to the efficiency of the engine heat is greater, just like The storage of energy in a substance having a very low temperature corresponds to the concept of a novel battery which can be manufactured using a low-cost energy source such as garbage electricity, thereby effectively reducing the operating cost of the engine.
本发明中, 所述低温冷源中的所述低温物质发挥冷却作用后, 既可导入所述工质闭合 回路中, 作为双通道熵循环发动机的循环工质, 也可不导入所述工质闭合回路中。  In the present invention, after the low-temperature substance in the low-temperature cold source exhibits a cooling action, it may be introduced into the working fluid closed circuit as a circulating medium of a two-channel entropy cycle engine, or may not be introduced into the working medium. In the loop.
本发明中, 所谓的两个装置连通, 是指流体可以在两个装置之间单向或者双向流通。 所谓的连通是指直接连通或经控制机构、 控制单元或其他控制部件间接连通。  In the present invention, the so-called two devices are in communication, meaning that the fluid can flow in one or two directions between the two devices. By communication is meant direct communication or indirect communication via a control mechanism, control unit or other control component.
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本发明中, 所述四类门气缸活塞机构是指气缸上设有进气口、 排气口、 供气口和回充 口, 在所述进气口、 所述排气口、 所述供气口和所述回充口处依次对应设置进气门、 排气 门、 供气门和回充门的气缸活塞机构。  In the present invention, the four-type door cylinder piston mechanism means that an air inlet, an exhaust port, a gas supply port and a refill port are provided on the cylinder, and the air inlet, the exhaust port, and the supply port are provided The air port and the refill port are correspondingly arranged with a cylinder piston mechanism of an intake valve, an exhaust valve, a supply valve and a refill door.
本发明中, 所述液氧包括商业液氧或现场制备的液氧。  In the present invention, the liquid oxygen includes commercial liquid oxygen or liquid oxygen prepared in the field.
本发明中, 通过调整所述工质闭合回路的工作压力以及热端机构的排量, 以控制热端 机构的质量排量,使所述内燃燃烧室排出的物质的质量流量 Μ2大于从所述工质闭合回路外 导入所述内燃燃烧室的物质的质量流量 M 也就是说除了从所述工质闭合回路外导入所述 内燃燃烧室的物质外, 还有一部分物质是从所述工质闭合回路中导入所述内燃燃烧室的, 由于所述内燃燃烧室是设置在所述工质闭合回路内的, 所以也就是说从所述内燃燃烧室排 出的物质至少有一部分流回所述内燃燃烧室, 即实现了工质在热端机构和冷端机构之间有 往复流动。 从所述工质闭合回路外向所述内燃燃烧室导入的物质可以是氧化剂、 还原剂、 压缩气体或高温燃气等。 In the present invention, by adjusting the working pressure of the working fluid closed circuit and the displacement of the hot end mechanism to control the mass displacement of the hot end mechanism, the mass flow rate Μ 2 of the substance discharged from the internal combustion combustion chamber is greater than The mass flow rate M of the substance introduced into the internal combustion combustion chamber outside the closed circuit of the working fluid means that, in addition to the substance introduced into the internal combustion combustion chamber from the closed circuit of the working fluid, a part of the substance is from the working medium Introducing the internal combustion combustion chamber into the closed circuit, since the internal combustion combustion chamber is disposed in the working fluid closed circuit, that is, at least a portion of the material discharged from the internal combustion combustion chamber flows back to the internal combustion The combustion chamber, that is, the working medium has a reciprocating flow between the hot end mechanism and the cold end mechanism. The substance introduced from the outside of the working fluid closed circuit to the internal combustion combustion chamber may be an oxidant, a reducing agent, a compressed gas or a high temperature gas.
本发明中, 所述热端机构是指所述内燃燃烧室设在其中, 或者所述内燃燃烧室中发生 燃烧化学反应后产生的工质首先进入其中的气体做功机构, 例如所述活塞式气体做功机构。  In the present invention, the hot end mechanism refers to a gas working mechanism in which the internal combustion combustion chamber is disposed, or a working medium generated in a combustion chemical reaction in the internal combustion combustion chamber first enters, for example, the piston gas. Work organization.
本发明中, 所述冷端机构是指工质从所述热端机构流出后进入的气体压缩机构, 例如 所述活塞式气体压缩机构。  In the present invention, the cold end mechanism refers to a gas compression mechanism into which the working medium flows out from the hot end mechanism, for example, the piston type gas compression mechanism.
本发明中, 所述氧化剂传感器是指对所述工质闭合回路中的氧化剂的含量进行检测的 装置。 所述氧化剂传感器对所述氧化剂控制装置提供信号, 所述氧化剂控制装置根据所述 氧化剂传感器提供的信号以及预先设定的所述工质闭合回路中静态或动态的氧化剂含量设 定值对所述氧化剂控制阀进行控制以增加或减少向所述工质闭合回路中供给氧化剂的量, 达到调控所述工质闭合回路中氧化剂的含量的目的。 说 明 书 所述氧化剂含量的设定值可以是一个数值, 也可以是一个数值区间, 例如: 所述工质 闭合回路中的氧化剂含量的设定值可以为 5 %、 10 %或 10%〜12%等。 In the present invention, the oxidant sensor refers to a device that detects the content of the oxidant in the closed circuit of the working fluid. The oxidant sensor provides a signal to the oxidant control device, the oxidant control device according to a signal provided by the oxidant sensor and a preset static or dynamic oxidant content setting value in the working fluid closed circuit The oxidant control valve is controlled to increase or decrease the amount of oxidant supplied to the working fluid closed circuit for the purpose of regulating the content of the oxidant in the closed loop of the working fluid. The set value of the oxidant content in the specification may be a value or a numerical interval, for example: the oxidant content in the closed loop of the working fluid may be set at 5%, 10% or 10%~12%. Wait.
所述氧化剂传感器可以设在远离所述内燃燃烧室的闭合回路上, 可保证整个所述工质 闭合回路是在富氧 (氧含量大于零) 状态下工作, 使所述内燃燃烧室内发生稳定的燃烧化 学反应, 同时还可以防止积碳的发生。  The oxidant sensor may be disposed on a closed circuit remote from the internal combustion combustion chamber to ensure that the entire working fluid closed circuit operates in an oxygen-rich (oxygen content greater than zero) state, so that the internal combustion combustion chamber is stable. Combustion of chemical reactions while preventing carbon deposits.
本发明中, 所述气液缸是指可以容纳气体工质和 /或液体, 并能承受一定压力的容器, 所述气液缸被所述气液隔离结构分隔成气体端和液体端, 所述气液缸的气体端设有气体工 质流通口, 所述气体工质流通口用于与所述工质闭合回路中的其他装置或机构连通; 所述 气液缸的液体端设有液体流通口, 所述液体流通口用于与液压动力机构和 /或液体工质回送 系统连通。  In the present invention, the gas-liquid cylinder refers to a container which can accommodate a gas working medium and/or a liquid and can withstand a certain pressure, and the gas-liquid cylinder is divided into a gas end and a liquid end by the gas-liquid separating structure. The gas end of the gas cylinder is provided with a gas working fluid circulation port for communicating with other devices or mechanisms in the closed circuit of the working fluid; the liquid end of the gas liquid cylinder is provided with a liquid A flow port for communicating with a hydraulic power mechanism and/or a liquid working fluid return system.
本发明中, 所述气液隔离结构是指可以在所述气液缸中做往复运动的结构体, 如隔离 板、 隔离膜、 活塞等, 其作用是隔离所述气液缸中的气体工质和液体, 优选地, 所述气液 隔离结构和所述气液缸密封滑动配合。 在所述活塞液体机构工作过程中, 根据所述气液隔 离结构处于所述气液缸内的不同位置, 所述气液缸内可能全部是气体工质, 也可能全部是 液体, 或者气体工质和液体同时存在。  In the present invention, the gas-liquid insulation structure refers to a structure that can reciprocate in the gas-liquid cylinder, such as a separator, a separator, a piston, etc., and functions to isolate the gas in the gas-liquid cylinder. Preferably, the gas-liquid insulation structure and the gas-liquid cylinder are sealingly fitted. During the operation of the piston liquid mechanism, according to the gas-liquid isolation structure being at different positions in the gas-liquid cylinder, the gas-liquid cylinder may all be a gas working medium, or may be all liquid, or a gas worker. Both the substance and the liquid are present at the same time.
本发明中, 所述气液缸内的液体和所述气液隔离结构与传统的活塞连杆机构不同, 传 统的活塞连杆机构中的活塞可受连杆的推力或拉力停下, 从而实现对活塞行程的限制, 而 在所述气液缸中, 当所述气液缸内的气体工质做正功时, 所述气液隔离结构受压力向下止 点方向移动, 将液体以高压形式排出所述气液缸并推动液压动力机构 (例如液体马达) 对 外做功, 当液体即将排尽时, 改变液体马达工作模式或启动液体工质回送系统, 使所述气 液缸内的液体不再减少, 此时液体会对所述气液缸内的所述气液隔离结构施加制动力, 使 其停止, 以防止其撞击气液缸的液体端底部的壁; 当不断向所述气液缸内输入液体时, 所 述气液隔离结构会不断向上止点方向移动, 当到达上止点附近时, 停止向所述气液缸内输 入液体或者使所述气液缸内的液体减少 (流出), 尽管如此, 所述气液缸内的液体和所述气 液隔离结构仍然会由于惯性向上止点方向运动, 此时, 如果所述气液缸内的气体工质的压 力不够高, 则会导致所述气液隔离结构继续向上运动而撞击气液缸顶部的壁, 为了避免这 种撞击, 需要使气液缸内气体工质的压力足够高, 使其对所述气液隔离结构的压力大于所 述气液缸内的液体和所述气液隔离结构做往复运动时的惯性力之和。  In the present invention, the liquid in the gas-liquid cylinder and the gas-liquid isolation structure are different from the conventional piston linkage mechanism, and the piston in the conventional piston linkage mechanism can be stopped by the thrust or pulling force of the connecting rod, thereby realizing Limiting the stroke of the piston, and in the gas-liquid cylinder, when the gas working fluid in the gas-liquid cylinder is doing positive work, the gas-liquid isolation structure is moved by the pressure to the bottom dead center, and the liquid is pressurized Forming the gas-liquid cylinder and pushing a hydraulic power mechanism (such as a liquid motor) to perform external work. When the liquid is about to be exhausted, changing the liquid motor working mode or starting the liquid working fluid returning system, so that the liquid in the gas-liquid cylinder is not Further reducing, at this time, the liquid applies a braking force to the gas-liquid insulation structure in the gas-liquid cylinder to stop it to prevent it from hitting the wall of the bottom of the liquid end of the gas-liquid cylinder; When the liquid is input into the cylinder, the gas-liquid isolation structure continuously moves toward the upper dead center, and when the vicinity of the top dead center is reached, the liquid is input into the gas cylinder or the liquid in the gas cylinder is stopped. Reducing (flowing out), however, the liquid in the gas-liquid cylinder and the gas-liquid isolation structure still move due to the inertia to the dead center direction, and at this time, if the gas working fluid in the gas-liquid cylinder is not sufficiently pressurized High, the gas-liquid isolation structure continues to move upwards and hits the wall of the top of the gas cylinder. In order to avoid such impact, the pressure of the gas working fluid in the gas-liquid cylinder needs to be sufficiently high to make the gas-liquid The pressure of the isolation structure is greater than the sum of the inertial forces of the liquid in the gas cylinder and the gas-liquid isolation structure during reciprocation.
本发明中, 在所述双通道熵循环发动机的工作过程中所述气液缸内的液体和所述气液 隔离结构做往复运动时的惯性力之和是变化的, 因此在工程设计中应保证在任何工作吋刻 都满足 "所述气液缸内的气体工质对所述气液隔离结构的压力大于所述气液缸内的液体和 所述气液隔离结构做往复运动时的惯性力之和" 的条件, 例如通过调整所述工质闭合回路 中的工作压力、 调整气液隔离结构的质量、 调整液体密度或调整液体深度等方式来实现, 其中, 所述液体深度是指液体在做往复运动方向上的液体的深度。  In the present invention, the sum of the inertial forces of the liquid in the gas-liquid cylinder and the gas-liquid isolation structure during reciprocation during the operation of the two-channel entropy cycle engine is varied, and therefore should be It is ensured that at any working moment, the inertia of the gas working fluid in the gas-liquid cylinder to the gas-liquid isolation structure is greater than the inertia of the liquid in the gas-liquid cylinder and the gas-liquid isolation structure. The condition of the sum of forces is achieved, for example, by adjusting the working pressure in the closed circuit of the working fluid, adjusting the mass of the gas-liquid isolating structure, adjusting the density of the liquid, or adjusting the depth of the liquid, wherein the liquid depth refers to a liquid The depth of the liquid in the direction of reciprocation.
所谓的 "调整所述工质闭合回路中的工作压力"是通过调整流入和 /或流出所述工质闭 说 明 书 合回路的气体工质的体积流量来实现的, 例如可以通过调整所述工质导出口的开关间隔、 每次开启的时间和 /或所述工质导出口处控制阔的开口大小来实现。 The so-called "adjusting the working pressure in the closed circuit of the working fluid" is to adjust the inflow and/or outflow of the working fluid. The volume flow rate of the gaseous working fluid of the combined circuit can be realized, for example, by adjusting the switching interval of the working fluid outlet, the time of each opening, and/or the opening opening size of the working fluid outlet. .
本发明中, 所述内燃燃烧室和所述冷却器在所述工质闭合回路上的位置应根据公知的 热力学循环来设置。  In the present invention, the position of the internal combustion combustion chamber and the cooler on the closed circuit of the working fluid should be set according to a well-known thermodynamic cycle.
本发明中, 所述工质闭合回路内的工质需要经过压缩、 加热升温升压、 做功以及被冷 却的过程, 这就要求所述工质闭合回路能承受一定压力, 选择性地, 所述工质闭合回路的 承压能力可设为大于 2MPa、 2.5MPa、 3MPa、 3.5MPa、 4MPa、 4.5MPa、 5MPa、 5.5MPa、 6MPa、 6.5MPa、 7MPa、 7.5MPa> 8MPa、 8.5MPa、 9MPa、 9.5MPa、 10MPa、 10.5MPa、 l lMPa、 11.5MPa、 12MPa、 12.5MPa、 13MPa、 13.5MPa、 14MPa、 14.5MPa、 15MPa、 15.5MPa、丽 Pa、 16.5MPa、 17MPa、 17.5MPa、 18MPa、 18.5MPa、 19MPa、 19.5MPa、 20MPa、 20.5MPa、 21MPa、 22MPa、 23MPa、 24MPa、 25MPa、 26MPa、 27MPa、 28MPa、 29MPa、 30MPa、 31MPa、 32MPa、 33MPa、 34MPa、 35MPa、 36MPa、 37MPa、 38MPa、 39MPa或大于 40MPa。 相应地, 所述 氧化剂源和所述燃料源的承压能力也设为上述同样的数值范围。  In the present invention, the working fluid in the working fluid closed circuit needs to be subjected to compression, heating, temperature rising and boosting, work and cooling, which requires the working fluid closed circuit to withstand a certain pressure, optionally, The pressure capacity of the closed loop of the working fluid can be set to be greater than 2 MPa, 2.5 MPa, 3 MPa, 3.5 MPa, 4 MPa, 4.5 MPa, 5 MPa, 5.5 MPa, 6 MPa, 6.5 MPa, 7 MPa, 7.5 MPa > 8 MPa, 8.5 MPa, 9 MPa, 9.5. MPa, 10 MPa, 10.5 MPa, l lMPa, 11.5 MPa, 12 MPa, 12.5 MPa, 13 MPa, 13.5 MPa, 14 MPa, 14.5 MPa, 15 MPa, 15.5 MPa, 丽 Pa, 16.5 MPa, 17 MPa, 17.5 MPa, 18 MPa, 18.5 MPa, 19 MPa 19.5MPa, 20MPa, 20.5MPa, 21MPa, 22MPa, 23MPa, 24MPa, 25MPa, 26MPa, 27MPa, 28MPa, 29MPa, 30MPa, 31MPa, 32MPa, 33MPa, 34MPa, 35MPa, 36MPa, 37MPa, 38MPa, 39MPa or more than 40MPa. Accordingly, the pressure bearing capacity of the oxidant source and the fuel source is also set to the same numerical range as described above.
本发明中, 所述控制阀受使所述工质闭合回路中的最低压力大于 0.2MPa、 0.3MPa、 0.5MPa、 lMPa、 1.5MPa、 2MPa、 2.5MPa、 3MPa、 5MPa、 8MPa或大于 lOMPa控制机构 所控制。  In the present invention, the control valve is controlled by a minimum pressure in the closed circuit of the working fluid of more than 0.2 MPa, 0.3 MPa, 0.5 MPa, 1 MPa, 1.5 MPa, 2 MPa, 2.5 MPa, 3 MPa, 5 MPa, 8 MPa or more than 10 MPa. Controlled.
本发明中, 所述活塞式气体压缩机构和所述活塞式气体做功机构之间可以不设阔, 而 依靠相互之间的相位差来形成系统的压缩和膨胀做功。  In the present invention, the piston type gas compression mechanism and the piston type gas work mechanism may not be wide, but rely on the phase difference between each other to form the compression and expansion work of the system.
本发明人提出如下所述 P-T图和热力学第二定律的新的阐述方式:  The inventors propose a new way of clarifying the P-T diagram and the second law of thermodynamics as follows:
压力和温度是工质的最基本、 最重要的状态参数。 然而, 在至今为止的热力学研究中, 没有将以压力 P和温度 T为坐标的 P-T图用于对热力学过程及热力循环的研究中。 在热力 学诞生以来的两百多年里, 本发明人第一次提出用 P-T 图研究热力学过程和热力循环的思 想。 在利用 P-T图研究热力学过程和热力循环中, 本发明人发现 P-T图比常用的 P-V图和 τ-s图都具有明显的优势, 它能更本质地描述热力学过程和热力循环中工质状态的变化, 使 本发明人对热力学过程和热力循环有更深刻的理解。 利用 P-T 图, 本发明人总结了十条热 力学第二定律的新的阐述方式, 这些新的阐述方式与以往的开尔文和克劳修斯的热力学阐 述方式虽然等价, 但是更明确的揭示了对工质的加热过程和压缩过程的区别, 也为高效热 机的开发指明了方向。 这一新方法和新定律, 将大大促进热力学的发展和热机工业的进步。 具体如下:  Pressure and temperature are the most basic and important state parameters of the working fluid. However, in the thermodynamic studies to date, P-T diagrams with pressure P and temperature T as coordinates have not been used in the study of thermodynamic processes and thermodynamic cycles. For more than two hundred years since the birth of thermodynamics, the inventors have for the first time proposed the idea of studying thermodynamic processes and thermodynamic cycles using P-T diagrams. In the study of thermodynamic processes and thermodynamic cycles using PT maps, the inventors have found that PT maps have obvious advantages over commonly used PV maps and τ-s maps, which can more fully describe the working conditions of thermodynamic processes and thermodynamic cycles. The changes have enabled the inventors to have a deeper understanding of thermodynamic processes and thermodynamic cycles. Using the PT diagram, the inventors summarized ten new ways of elaboration of the second law of thermodynamics. These new elaborations are equivalent to the previous methods of thermodynamics of Kelvin and Clausius, but more clearly reveal the work. The difference between the quality heating process and the compression process also points the way for the development of high-efficiency heat engines. This new method and new law will greatly promote the development of thermodynamics and the advancement of the heat engine industry. details as follows:
P-V图和 T-S图在热力学研究中早己被广泛应用, 然而鉴于 P、 T是工质最重要的状态 参数,所以本发明人以压力 P和温度 T为坐标绘制了 P-T图,并将 Camot Cycle和 Otto Cycle 标识在图 26所示的 P-T图中。 很明显地, P-T图使热力学过程和热力循环中工质状态的变 化更加显而易见, 也使热力学过程和热力循环的本质更易理解。 例如: 图 26所示的 Carnot Cycle的 P-T图, 可以使本发明人容易地得出这样的结论: Carnot Cycle的可逆绝热压缩过 程的使命是以可逆绝热压缩的方式将工质的温度升高至其高温热源的温度, 以实现与高温 说 明 书 热源的温度保持一致的前提下自高温热源恒温吸热膨胀过程。 此外, 本发明人还可以明显 地看出: 当 Carnot Cycle的高温热源的温度升高时, 本发明人必须在 Carnot Cycle的可逆绝 热压缩过程中将工质更加深度地压缩, 使其达到更高的温度, 以达到升温后的高温热源的 温度, 以实现与升温后的高温热源的温度保持一致的前提下自升温后的高温热源恒温吸热 膨胀过程, 从而实现效率的提 。 The PV map and the TS map have been widely used in thermodynamic research. However, since P and T are the most important state parameters of the working fluid, the inventors plotted the PT map with the pressure P and the temperature T as coordinates, and will take the Camot Cycle. And the Otto Cycle is identified in the PT diagram shown in FIG. Obviously, the PT map makes the changes in the working state of the thermodynamic process and the thermodynamic cycle more obvious, and makes the nature of the thermodynamic process and the thermodynamic cycle easier to understand. For example: The PT diagram of the Carnot Cycle shown in Figure 26 allows the inventors to easily conclude that the mission of the reversible adiabatic compression process of Carnot Cycle is to increase the temperature of the working fluid to a reversible adiabatic compression. The temperature of its high temperature heat source to achieve high temperature Explain that the temperature of the heat source of the book is consistent with the constant temperature endothermic expansion process from the high temperature heat source. Furthermore, the inventors can clearly see that when the temperature of the high temperature heat source of the Carnot Cycle rises, the inventors must compress the working medium to a deeper level in the reversible adiabatic compression process of the Carnot Cycle to make it higher. The temperature is reached to reach the temperature of the high-temperature heat source after the temperature rise, so as to achieve the constant temperature endothermic expansion process of the high-temperature heat source after self-heating on the premise of keeping the temperature of the high-temperature heat source after the temperature rise, thereby achieving efficiency.
根据绝热过程方程 /» = C ^ (其中, C是常数, 是工质的绝热指数), 本发明人将不 同 C值的绝热过程方程的曲线绘制在图 27中。 根据数学分析, 并如图 27所示, 任何两条 绝热过程曲线都不相交。 这意味着: 在同一条绝热过程曲线上的过程是绝热过程, 而与任 何绝热过程曲线相交的过程是非绝热过程, 换句话说, 任何连接两条不同绝热过程曲线的 过程是非绝热过程 (所谓的非绝热过程是指具有热量传递的过程, 即放热的过程和吸热的 过程)。 在图 28中, 本发明人标注了两个状态点, 即点 A和点 B。 如果一个热力过程或一 系列相互连接的热力过程从点 A出发到达点 B,则本发明人称之为连接点 A和点 B的过程, 反之本发明人称之为连接点 B和点 A的过程。根据图 28所示,本发明人可以得出这样的结 论: 如点 B在点 A所在的绝热过程曲线上, 则连接点 A和点 B的过程是绝热过程; 如点 B 在点 A所在的绝热过程曲线的右侧, 则连接点 A和点 B的过程是吸热过程; 如点 B在点 A 所在的绝热过程曲线的左侧, 则连接点 A和点 B的过程是放热过程。 由于连接点 A和点 B 的过程可能是放热过程、 绝热过程或吸热过程, 所以本发明人以点 B为参照, 将点 A分别 定义为具有过剩温度、 理想温度和不足温度。 同理, 连接点 B和点 A的过程可能是放热过 程、绝热过程或吸热过程, 所以本发明人以点 A为参照, 将点 B分别定义为具有过剩温度、 理想温度和不足温度。 According to the adiabatic process equation /» = C ^ (where C is a constant, which is the adiabatic index of the working fluid), the inventors plotted the curves of the adiabatic process equations of different C values in Fig. 27. According to the mathematical analysis, and as shown in Fig. 27, any two adiabatic process curves do not intersect. This means that the process on the same adiabatic process curve is an adiabatic process, and the process of intersecting any adiabatic process curve is a non-adiabatic process. In other words, any process connecting two different adiabatic process curves is a non-adiabatic process (so-called A non-adiabatic process refers to a process with heat transfer, that is, an exothermic process and an endothermic process). In Fig. 28, the inventors have marked two state points, point A and point B. If a thermal process or a series of interconnected thermal processes arrives from point A to point B, the inventors refer to the process of connecting point A and point B, whereas the inventors refer to the process of connecting point B and point A. According to Fig. 28, the inventors can conclude that if point B is on the adiabatic process curve where point A is located, the process of connecting point A and point B is an adiabatic process; if point B is at point A On the right side of the adiabatic process curve, the process of connecting point A and point B is an endothermic process; if point B is to the left of the adiabatic process curve where point A is located, the process of connecting point A and point B is an exothermic process. Since the process of connecting the point A and the point B may be an exothermic process, an adiabatic process or an endothermic process, the inventors have defined point A as having a surplus temperature, an ideal temperature, and an insufficient temperature, respectively, with reference to point B. Similarly, the process of connecting point B and point A may be an exothermic process, an adiabatic process or an endothermic process, so the inventors have defined point B as having an excess temperature, an ideal temperature, and an insufficient temperature, respectively, with reference to point A.
通过这些分析和定义, 本发明人得出如下十条关于热力学第二定律的新的阐述方式: Through these analyses and definitions, the inventors have come up with the following ten new ways of clarifying the second law of thermodynamics:
1、 没有吸热过程的参与, 不可能将放热过程恢复至其始点。 1. Without the participation of the endothermic process, it is impossible to restore the exothermic process to its starting point.
2、 没有放热过程的参与, 不可能将吸热过程恢复至其始点。  2. Without the participation of the exothermic process, it is impossible to restore the endothermic process to its starting point.
3、 没有非绝热过程的参与, 不可能将非绝热过程恢复至其始点。  3. Without the participation of non-adiabatic processes, it is impossible to restore the non-adiabatic process to its starting point.
4、 仅用绝热过程, 不可能将非绝热过程恢复至其始点。  4. It is impossible to restore the non-adiabatic process to its starting point using only the adiabatic process.
5、 用放热过程以外的热力过程使吸热过程的压力恢复到其始点的压力时, 其温度一定 高于其始点的温度。  5. When the pressure of the endothermic process is restored to the pressure at the starting point by a thermal process other than the exothermic process, the temperature must be higher than the temperature at the starting point.
6、 用吸热过程以外的热力过程使放热过程的压力恢复到其始点的压力时, 其温度一定 低于其始点的温度。  6. When the pressure of the exothermic process is restored to the pressure at the starting point by a thermal process other than the endothermic process, the temperature must be lower than the temperature at the starting point.
7、 吸热过程不可能不产生过剩温度。  7. It is impossible for the endothermic process to not generate excess temperature.
8、 放热过程不可能不产生不足温度。  8. The exothermic process is unlikely to produce insufficient temperature.
9、 任何在压缩过程中不放热的热机的效率不可能达到卡诺循环的效率。  9. The efficiency of any heat engine that does not exotherm during compression cannot achieve the efficiency of the Carnot cycle.
10、 对工质的加热过程和对工质的压缩过程的区别在于: 加热过程一定产生过剩温度, 而压缩过程则不然。  10. The difference between the heating process of the working fluid and the compression process of the working fluid is that the heating process must generate excess temperature, but the compression process is not.
关于热力学第二定律的十条新的阐述方式, 是等价的, 也是可以经数学证明的, 这十 说 明 书 条阐述方式中的任何一条均可单独使用。 本发明人建议: 在热力学研究过程中, 应广泛应 用 P-T图及上述关于热力学第二定律的新的阐述方式。 P-T图以及关于热力学第二定律的新 的阐述方式对热力学的进步和高效热机的开发具有重大意义。 The ten new ways of elaboration on the second law of thermodynamics are equivalent and can also be proved by mathematics. Any of the ways in which the book is described can be used separately. The inventors suggest that: In the process of thermodynamics research, the PT diagram and the above-mentioned new elaboration method for the second law of thermodynamics should be widely applied. The PT diagram and the new elaboration of the second law of thermodynamics are of great significance for the advancement of thermodynamics and the development of high-efficiency heat engines.
热力学第二定律的新的阐述方式的英文表达:  The English expression of the new elaboration of the second law of thermodynamics:
1. It is impossible to return a heat rejection process to its initial state without a heat injection process involved.  1. It is impossible to return a heat rejection process to its initial state without a heat injection process involved.
2. It is impossible to return a heat injection process to its initial state without a heat rejection process involved.  2. It is impossible to return a heat injection process to its initial state without a heat rejection process involved.
3. It is impossible to return a non-adiabatic process to its initial state without a non-adiabatic process involved.  3. It is impossible to return a non-adiabatic process to its initial state without a non-adiabatic process involved.
4. It is impossible to return a non-adiabatic process to its initial state only by adiabatic process.  4. It is impossible to return a non-adiabatic process to its initial state only by adiabatic process.
5. If the final pressure of heat injection process is returned to its initial pressure by process other than heat rejection process, the temperature of that state is higher than that of the initial state.  5. If the final pressure of heat injection process is returned to its initial pressure by process other than heat rejection process, the temperature of that state is higher than that of the initial state.
6. If the final pressure of heat rejection process is returned to its initial pressure by process other than heat injection process, the temperature of that state is lower than that of the initial state.  If the final pressure of the heat rejection process is returned to its initial pressure by process other than heat injection process, the temperature of that state is lower than that of the initial state.
7. It is impossible to make heat injection process not generate excess-temperature. 8. It is impossible to make heat rejection process not generate insufficient- temperature. It is impossible to make heat injection process not generate excess-temperature. 8. It is impossible to make heat rejection process not generate excess-temperature.
9. It is impossible for any device that operates on a cycle to reach the efficiency indicated by Carnot cycle without heat rejection in compression process. 9. It is impossible for any device that operates on a cycle to reach the efficiency indicated by Carnot cycle without heat rejection in compression process.
10. The difference between heat injection process and compression process which are applied to working fluid of thermodynamic process or cycle is that heat injection process must generate excess-temperature, but compression process must not.  The difference between heat injection process and compression process which are applied to working fluid of thermodynamic process or cycle is that heat injection process must generate excess-temperature, but compression process must not.
本发明中, 根据热能与动力领域的公知技术, 在必要的地方设置必要的部件、 单元或 系统。  In the present invention, necessary components, units or systems are provided where necessary in accordance with known techniques in the field of thermal energy and power.
本发明的有益效果如下:  The beneficial effects of the present invention are as follows:
本发明通过利用内燃加热方式代替传统热气机的外燃加热方式, 将内燃加热方式的直 接加热以致加热效率高的优势应用到热气机上, 克服了传统热气机中因工质的温度和压力 难以达到更高水平而影响功率和功率密度的问题, 从而可以有效节约能源并大幅度减少机 构的体积、 重量和制造成本, 具有广阔的应用前景。  The invention replaces the external combustion heating mode of the traditional hot air machine by using the internal combustion heating mode, and applies the direct heating of the internal combustion heating mode to the hot air machine, thereby overcoming the temperature and pressure of the working medium due to the difficulty of the conventional hot air machine. The higher level affects the power and power density, which can effectively save energy and greatly reduce the size, weight and manufacturing cost of the mechanism, and has broad application prospects.
附图说明  DRAWINGS
图 1所示的是本发明实施例 1的结构示意图;  1 is a schematic structural view of Embodiment 1 of the present invention;
图 2所示的是本发明实施例 2的结构示意图; 图 3所示的是本发明实施例 3的结构示意图; 2 is a schematic structural view of Embodiment 2 of the present invention; Figure 3 is a schematic structural view of Embodiment 3 of the present invention;
图 4所示的是本发明实施例 4的结构示意图;  Figure 4 is a schematic structural view of Embodiment 4 of the present invention;
图 5所示的是本发明实施例 5的结构示意图;  Figure 5 is a schematic view showing the structure of Embodiment 5 of the present invention;
图 6所示的是本发明实施例 6的结构示意图;  Figure 6 is a schematic view showing the structure of Embodiment 6 of the present invention;
图 7所示的是本发明实施例 7的结构示意图;  Figure 7 is a schematic view showing the structure of Embodiment 7 of the present invention;
图 8所示的是本发明实施例 8的结构示意图;  Figure 8 is a schematic view showing the structure of Embodiment 8 of the present invention;
图 9所示的是本发明实施例 9的结构示意图;  Figure 9 is a schematic view showing the structure of Embodiment 9 of the present invention;
图 10所示的是本发明实施例说 10的结构示意图;  Figure 10 is a schematic view showing the structure of an embodiment of the present invention 10;
图 1 1所示的是本发明实施例 11的结构示意图;  Figure 11 is a schematic structural view of Embodiment 11 of the present invention;
图 12所示的是本发明实施例 12的结构示意图;  Figure 12 is a schematic view showing the structure of Embodiment 12 of the present invention;
图 13所示的是本发明实施例 13的结构示意图;  Figure 13 is a schematic view showing the structure of Embodiment 13 of the present invention;
图 14所示的是本发明实施例 14的结构示意图;  Figure 14 is a schematic view showing the structure of Embodiment 14 of the present invention;
图 15所示的是本发明实施例 15的结构示意图;  Figure 15 is a schematic view showing the structure of Embodiment 15 of the present invention;
图 16所示的是本发明实施例 16的结构示意图;  Figure 16 is a schematic view showing the structure of Embodiment 16 of the present invention;
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图 17所示的是本发明实施例 17的结构示意图;  Figure 17 is a schematic view showing the structure of Embodiment 17 of the present invention;
图 18所示的是本发明实施例 18的结构示意图;  Figure 18 is a schematic view showing the structure of Embodiment 18 of the present invention;
图 19所示的是本发明实施例 19的结构示意图;  Figure 19 is a schematic view showing the structure of Embodiment 19 of the present invention;
图 20所示的是本发明实施例 20的结构示意图;  Figure 20 is a schematic view showing the structure of Embodiment 20 of the present invention;
图 21所示的是本发明实施例 21的结构示意图;  Figure 21 is a schematic view showing the structure of Embodiment 21 of the present invention;
图 22所示的是本发明实施例 22的结构示意图;  Figure 22 is a schematic view showing the structure of Embodiment 22 of the present invention;
图 23所示的是本发明实施例 23的结构示意图;  Figure 23 is a schematic view showing the structure of Embodiment 23 of the present invention;
图 24所示的是本发明实施例 24的结构示意图;  Figure 24 is a schematic view showing the structure of Embodiment 24 of the present invention;
图 25所示的是本发明实施例 25的结构示意图;  Figure 25 is a schematic view showing the structure of Embodiment 25 of the present invention;
图 26所示的是卡诺循环和奥拓循环的 P-T图, 其中, , ei和 e 2是不同数值的常数, 是绝热指数, 循环 0-1-2-3-0 是卡诺循环, 循环 0-1-4-5-0 是高温热源温度升高后的卡诺 循环, 循环 0-6-7-8-0 是奥拓循环; Figure 26 shows the PT diagram of the Carnot cycle and the Alto cycle, where , e i and e 2 are constants of different values, which are adiabatic indices, and cycles 0-2-3-0 are Carnot cycles, cycles 0-1-4-5-0 is the Carnot cycle after the temperature of the high temperature heat source rises, and the cycle 0-6-7-8-0 is the Alto cycle;
图 27所示的是多条不同绝热过程曲线的 P-T图, 其中, C', ^2, 3 , 和 是不同 数值的常数, 是绝热指数, A和 B是状态点; Figure 27 shows a PT diagram of a plurality of different adiabatic process curves, where C ', ^ 2 , 3 , and are constants of different values, are adiabatic indices, and A and B are state points;
图 28所示的是绝热过程曲线的 P-T图, 其中, C是常数, 是绝热指数, A和 B是状 态点,  Figure 28 shows the P-T diagram of the adiabatic process curve, where C is a constant, is the adiabatic index, and A and B are the state points.
图中:  In the picture:
1连通通道、 3内燃燃烧室、 4氧化剂源、 5燃料源、 6工质导出口、 7逆止阔、 9活塞 式气体压缩机构、 10活塞式气体做功机构、 13叶轮压气机、 14涡轮动力机构、 15火花塞、 16深冷液体工质储罐、 17控制阀、 18非直混冷凝冷却器、 19直混冷凝冷却器、 20气液直 混冷却器、 21散热器、 21 1附属冷却器、 22吸附式制冷器、 23非直混冷却器、 30热交换器、 说 明 书 1 communication channel, 3 internal combustion combustion chamber, 4 oxidant source, 5 fuel source, 6 working fluid outlet, 7 reverse valve wide, 9 piston gas compression mechanism, 10 piston gas working mechanism, 13 impeller compressor, 14 turbine power Mechanism, 15 spark plugs, 16 cryogenic liquid working fluid storage tanks, 17 control valves, 18 non-direct mixing condensing coolers, 19 straight mixing condensing coolers, 20 gas-liquid direct mixing coolers, 21 radiators, 21 1 subsidiary coolers 22 adsorption chillers, 23 non-direct mixing chillers, 30 heat exchangers, Instruction manual
31旁置内燃燃烧室、 33回热器、 51氧化剂传感器、 52氧化剂控制装置、 53氧化剂控制阔、 60储气罐、 61冷却液体排出口、 62深冷液体排出口、 64液体二氧化碳出口、 66附属工质 导出口、 70不凝气储罐、 71不凝气回储压缩机、 72不凝气回收压缩机、 77曲轴箱、 81冷 凝冷却液体出口、 82不凝气出口、 88三元催化器、 90活塞液体机构、 91气液缸、 92气液 隔离结构、 96液压动力机构、 97液体工质回送系统、 98过程控制机构、 99四类门气缸活 塞机构、 991进气口、 992排气口、 993供气口、 994回充口、 100直连通道、 102附属气体 做功机构。  31 side internal combustion combustion chamber, 33 regenerator, 51 oxidant sensor, 52 oxidant control unit, 53 oxidant control wide, 60 gas storage tank, 61 cooling liquid discharge port, 62 cryogenic liquid discharge port, 64 liquid carbon dioxide outlet, 66 Auxiliary working fluid outlet, 70 non-condensable storage tank, 71 non-condensable gas storage compressor, 72 non-condensable gas recovery compressor, 77 crankcase, 81 condensing cooling liquid outlet, 82 non-condensing gas outlet, 88 three-way catalysis , 90 piston liquid mechanism, 91 gas cylinder, 92 gas-liquid isolation structure, 96 hydraulic power mechanism, 97 liquid working fluid return system, 98 process control mechanism, 99 four-class door cylinder piston mechanism, 991 air inlet, 992 row Air port, 993 air supply port, 994 refill port, 100 direct connection channel, 102 accessory gas work mechanism.
具体实施方式  detailed description
实施例 1  Example 1
如图 1所示的双通道熵循环发动机, 包括活塞式气体压缩机构 9、活塞式气体做功机构 10和两条连通通道 1, 所述活塞式气体压缩机构 9的工质出口经一条所述连通通道 1与所 述活塞式气体做功机构 10的工质入口连通, 所述活塞式气体做功机构 10的工质出口经另 一条所述连通通道 1与所述活塞式气体压缩机构 9的工质入口连通; 所述活塞式气体压缩 机构 9经两条所述连通通道 1与所述活塞式气体做功机构 10连通构成工质闭合回路; 在所 述活塞式气体压缩机构 9的工质出口和所述活塞式气体做功机构 10的工质入口之间的所述 连通通道 1上设内燃燃烧室 3, 在所述活塞式气体做功机构 10工质出口和所述活塞式气体 压縮机构 9工质入口之间的连通通道 1上设工质导出口 6,在所述工质导出口 6上设控制阀 17。  The two-channel entropy cycle engine shown in FIG. 1 includes a piston gas compression mechanism 9, a piston gas work mechanism 10, and two communication passages 1, and the working fluid outlet of the piston gas compression mechanism 9 passes through the communication. The passage 1 is in communication with the working fluid inlet of the piston gas working mechanism 10, and the working fluid outlet of the piston gas working mechanism 10 passes through the working fluid inlet of the other communication passage 1 and the piston gas compression mechanism 9. Connected; the piston-type gas compression mechanism 9 communicates with the piston-type gas work mechanism 10 via the two communication passages 1 to form a working fluid closed circuit; the working fluid outlet of the piston-type gas compression mechanism 9 and the An internal combustion combustion chamber 3 is disposed on the communication passage 1 between the working fluid inlets of the piston gas working mechanism 10, and the working fluid outlet of the piston gas working mechanism 10 and the working inlet of the piston gas compression mechanism 9 A working fluid outlet 6 is disposed in the communication passage 1 between the two, and a control valve 17 is disposed on the working fluid outlet 6.
本发明的方案具体实施时, 应根据公知技术在必要的地方设置必要的部件、 单元或系 统, 比如在所述内燃燃烧室 3上设氧化剂入口、 还原剂入口以及火花塞 15, 并相应的氧化 剂源 4和燃料源 5与所述内燃燃烧室 3连通, 相应的, 可以将所述氧化剂源 4中的氧化剂 为空气, 所述燃料源 5内的燃料为汽油。  In the specific implementation of the present invention, necessary components, units or systems should be provided where necessary according to known techniques, such as providing an oxidant inlet, a reducing agent inlet and a spark plug 15 on the internal combustion combustion chamber 3, and corresponding oxidant sources. 4 and the fuel source 5 is in communication with the internal combustion combustion chamber 3, and correspondingly, the oxidant in the oxidant source 4 may be air, and the fuel in the fuel source 5 is gasoline.
为了便于排出所述工质闭合回路中的过剩的工质, 所述工质导出口 6 导出的工质可以 是气体也可以是液体, 所述工质导出口 6排出工质的同时带出部分热量。  In order to facilitate the discharge of excess working fluid in the working fluid closed circuit, the working fluid derived from the working fluid outlet 6 may be a gas or a liquid, and the working fluid outlet 6 discharges the working medium while carrying out the working part. Heat.
具体实施时, 可以将所述控制阀 17可设为压力控制阀, 将导致压力过高的工质部分导 出所述工质闭合回路。  In a specific implementation, the control valve 17 can be set as a pressure control valve, and the working fluid portion that causes the excessive pressure is led to close the working fluid.
作为可以变换的实施方式, 所述内燃燃烧室 3 可以设置在所述工质闭合回路内的其它 任何位置上, 并最好设置在以所述活塞式气体压縮机构 9 的工质出口为上游和以所述活塞 式气体做功机构 10的工质出口为下游的所述工质闭合回路内; 所述工质导出口 6可以设置 在所述工质闭合回路内的其它任何位置上, 最好设置在以所述活塞式气体做功机构 10的工 质出口为上游和以所述内燃燃烧室 3 的工质入口为下游的所述工质闭合回路上; 所述控制 阀 17可以不设。  As an alternative embodiment, the internal combustion combustion chamber 3 may be disposed at any other position within the working fluid closed circuit, and is preferably disposed upstream of the working fluid outlet of the piston gas compression mechanism 9. And in the working fluid closed loop which is downstream of the working fluid outlet of the piston gas working mechanism 10; the working fluid outlet 6 may be disposed at any other position in the closed circuit of the working fluid, preferably It is disposed on the working fluid closed circuit upstream of the working fluid outlet of the piston gas working mechanism 10 and downstream of the working fluid inlet of the internal combustion combustion chamber 3; the control valve 17 may not be provided.
本实施例产品的工作过程: 由所述氧化剂源 4和所述燃料源 5分别提供的氧化剂和燃 料, 在所述内燃燃烧室 3中发生燃烧反应, 对进入所述内燃燃烧室 3的所述工质闭合回路 中原有的气体工质进行加热, 同时与燃烧所产生的产物一起沿所述连通通道 1 进入所述活 塞式气体做功机构 10 , 对外输出动力; 做功后的气体工质经所述活塞式气体做功机构 10排 出, 再经由另一条所述连通通道 1进入所述活塞式气体压缩机构 9中被压缩, 压縮后的气 体工质经所述活塞式气体压缩机构 9工质出口返回至所述内燃燃烧室 3被加热, 依此循环 进行; 其中当所述工质闭合回路中压力过大, 可经由所述工质导出口 6导出部分工质。 The working process of the product of the present embodiment: an oxidant and a fuel respectively supplied from the oxidant source 4 and the fuel source 5, a combustion reaction occurs in the internal combustion combustion chamber 3, and the combustion into the internal combustion combustion chamber 3 The original gaseous working medium in the closed circuit of the working medium is heated, and simultaneously enters the living along the communication channel 1 together with the product produced by the combustion. The plug gas working mechanism 10 outputs external power; the working fluid after the work is discharged through the piston gas work mechanism 10, and then enters the piston gas compression mechanism 9 via another communication passage 1 to be compressed. The compressed gas working medium is returned to the internal combustion combustion chamber 3 via the working fluid outlet of the piston type gas compression mechanism, and is heated according to the cycle; wherein when the working fluid closes the circuit, the pressure is too large, The working fluid outlet 6 leads to a part of the working fluid.
具体实施时, 可选择地, 所述氧化剂源 4 中的氧化剂还可以设为液氧、 高压氧气、 高 压压缩空气、 液态空气、 双氧水、 双氧水溶液等; 所述燃料源 5中的燃料还可以设为柴油、 重油、 煤油、 航空煤油、 甲醇、 乙醇、 甲醚、 乙醚等。  In a specific implementation, the oxidant in the oxidant source 4 may also be set as liquid oxygen, high pressure oxygen, high pressure compressed air, liquid air, hydrogen peroxide, aqueous hydrogen peroxide solution, etc.; the fuel in the fuel source 5 may also be set For diesel, heavy oil, kerosene, aviation kerosene, methanol, ethanol, methyl ether, ether, etc.
实施例 2 说  Example 2
如图 2所示的双通道熵循环发动机, 其与实施例 1 的区别在于: 所述双通道熵循环发 动机还包括冷却器, 所述冷却器设为散热器 21, 所述散热器 21设在所述活塞式气体做功机 构 10的工质出口与所述活塞式气体压缩机构 9的工质入口之间的所述连通通道 1上, 所述 氧化剂源 4中的氧化剂可以设为液氧;所述工质导出口 6设置在所述活塞式气体压缩机构 9 工质出口与所述内燃燃烧室 3工质入口之间的连通通道 1上, 所述工质导出口 6经控制阔 17与储气罐 60连通, 所述储气罐 60用来储存高压气体和不凝气, 所述燃料源 5和所述散  The two-channel entropy cycle engine shown in FIG. 2 differs from the embodiment 1 in that: the two-channel entropy cycle engine further includes a cooler, the cooler is configured as a radiator 21, and the radiator 21 is disposed at The communication channel between the working fluid outlet of the piston gas working mechanism 10 and the working fluid inlet of the piston gas compression mechanism 9 may be used as liquid oxygen in the oxidant source 4; The working fluid outlet 6 is disposed on the communication passage 1 between the working fluid outlet of the piston type gas compression mechanism 9 and the working inlet of the internal combustion combustion chamber 3, and the working fluid outlet 6 is controlled to be 17 and stored. The gas tank 60 is connected, the gas storage tank 60 is for storing high pressure gas and non-condensable gas, the fuel source 5 and the scattered gas
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热器 21对工质的冷却程度决定导出工质的种类和状态, 当燃料设为氢气的时候, 导出的工 质可以为气态或液态水, 或其与闭合回路中气体的混合物; 当燃料设为碳氢化合物时, 导 出的工质中还含有二氧化碳等其他产物, 所述工质闭合回路内的循环气体设为氦气。 The degree of cooling of the working medium by the heater 21 determines the type and state of the derived working medium. When the fuel is set to hydrogen, the derived working medium may be gaseous or liquid water, or a mixture thereof with a gas in a closed loop; In the case of a hydrocarbon, the derived working fluid further contains other products such as carbon dioxide, and the circulating gas in the closed circuit of the working fluid is set to helium.
所述活塞式气体压缩机构 9的活塞和所述活塞式气体做功机构 10的活塞分别经连杆与 同一曲轴上的不同连杆轴颈连接, 此两所述连杆轴颈的相位差为 90度。  The piston of the piston type gas compression mechanism 9 and the piston of the piston type gas work mechanism 10 are respectively connected via a connecting rod and a different connecting rod journal on the same crankshaft, and the phase difference between the two connecting rod journals is 90 degree.
具体实施时, 可选择的将所述控制阀 17设为压力控制阀, 并使所述控制阀 17受峰压 控制机构控制, 所述峰压控制机构在所述工质闭合回路内的压力超过设定值时使所述控制 阔 17开启, 并当所述闭合回路内的压力回降到所述设定值时使所述控制阀 17关闭; 或使 所述控制阀 17受谷压控制机构控制, 在所述工质闭合回路内的压力处于谷压状态时使所述 控制阀 17开启, 并当所述工质闭合回路内的压力将至 0.2MPa时使所述控制阀 17关闭; 或 使所述控制阀 17受开启度控制机构控制, 所述开启度控制机构根据所述工质闭合回路内的 压力设定范围控制所述控制阀 17的开启度, 使所述工质导出口 6在某种开启度下处于常开 状态; 可选择地, 将工质闭合回路内的压力设定为大于 0.3MPa、 0.5MPa、 lMPa、 1.5MPa、 2MPa、 2.5MPa、 3MPa、 5MPa、 8MPa或大于 10MPa。  In a specific implementation, the control valve 17 can be selectively set as a pressure control valve, and the control valve 17 is controlled by a peak pressure control mechanism, and the pressure of the peak pressure control mechanism in the working fluid closed circuit exceeds Setting the value to open the control block 17 and closing the control valve 17 when the pressure in the closed circuit drops back to the set value; or subjecting the control valve 17 to the valley pressure control mechanism Controlling that the control valve 17 is opened when the pressure in the working fluid closed circuit is in a valley pressure state, and the control valve 17 is closed when the pressure in the working fluid closed circuit is to 0.2 MPa; or The control valve 17 is controlled by an opening degree control mechanism, and the opening degree control mechanism controls the opening degree of the control valve 17 according to a pressure setting range in the working fluid closed circuit to make the working fluid outlet 6 In a normally open state at a certain degree of opening; alternatively, the pressure in the closed circuit of the working fluid is set to be greater than 0.3 MPa, 0.5 MPa, 1 MPa, 1.5 MPa, 2 MPa, 2.5 MPa, 3 MPa, 5 MPa, 8 MPa or greater 10 MPa.
作为可以变换的实施方式, 所述冷却器可以设为其他形式的冷却器, 比如热交换器式 冷却器; 所述冷却器还可以设置在所述工质闭合回路的其它任何位置上; 所述冷却器和所 述储气罐 60可以择一设置; 所述控制阀 17可以不设。  As an alternative embodiment, the cooler may be configured as another type of cooler, such as a heat exchanger cooler; the cooler may also be disposed at any other location of the working fluid closed circuit; The cooler and the gas storage tank 60 may be alternatively disposed; the control valve 17 may not be provided.
可选择地, 两个所述连杆轴颈的相位差可以设为大于 0度小于 180度的范围内的任何 数值; 或者所述活塞式气体压缩机构 9的活塞和所述活塞式气体做功机构 10的活塞可以分 别经连杆与同一曲轴的同一连杆轴颈连接, 此时应将两者的气缸中心线之间的夹角设为小 于 180度。 说 明 书 本发明的所有实施方式中, 所述活塞式气体压縮机构 9 的活塞和所述活塞式气体做功 机构 10的活塞与曲轴的连接关系都可以参照本实施例及其可变换的实施方式设置, 当然, 本发明的所有实施方式中, 包括本实施例, 也可以使所述活塞式气体压缩机构 9 的活塞和 所述活塞式气体做功机构 10的活塞与曲轴之间采用其它的连接关系; 所有设有所述控制阀 17的实施例的可变换的实施方式中,都可以参照本实施 使所述控制阀 17受峰压控制机构 控制、 受谷压控制机构控制或受开启度控制机构控制。 Alternatively, the phase difference between the two connecting rod journals may be set to any value in a range of more than 0 degrees and less than 180 degrees; or the piston of the piston type gas compression mechanism 9 and the piston gas working mechanism The pistons of 10 can be connected to the same connecting rod journal of the same crankshaft via the connecting rods respectively. At this time, the angle between the cylinder center lines of the two cylinders should be set to be less than 180 degrees. In all embodiments of the present invention, the connection relationship between the piston of the piston type gas compression mechanism 9 and the piston and the crankshaft of the piston gas work mechanism 10 can be set with reference to the embodiment and its transformable embodiment. And of course, in all embodiments of the present invention, including the embodiment, the piston of the piston type gas compression mechanism 9 and the piston of the piston gas work mechanism 10 and the crankshaft may be in other connection relationship; In all of the alternative embodiments of the embodiment in which the control valve 17 is provided, the control valve 17 can be controlled by the peak pressure control mechanism, controlled by the valley pressure control mechanism, or controlled by the opening degree control mechanism with reference to the present embodiment. .
本发明的所有所述工质导出口 6没有连接其他装置的实施方式中, 都可以参考本实施 例将所述工质导出口 6与所述储气罐 60连通。  In the embodiment in which all of the working fluid outlets 6 of the present invention are not connected to other devices, the working fluid outlet 6 may be in communication with the gas storage tank 60 with reference to the present embodiment.
实施例 3  Example 3
如图 3所示的双通道熵循环发动机, 其与实施例 1 的区别在于: 所述双通道熵循环发 动机还包括冷却器, 所述冷却器设为散热器 21, 所述散热器 21设置在所述活塞式气体压缩 机构 9的气缸上。  The two-channel entropy cycle engine shown in FIG. 3 differs from the embodiment 1 in that: the two-channel entropy cycle engine further includes a cooler, the cooler is configured as a radiator 21, and the radiator 21 is disposed at The piston of the piston type gas compression mechanism 9 is on the cylinder.
具体实施时, 可选择地, 所述散热器 21还可设置在所述活塞式气体压缩机构 9的工质 出口处的所述连通通道 1上; 所述内燃燃烧室 3也可设在所述活塞式气体做功机构 10的气 缸内, 所述内燃燃烧室 3 内流出的工质是处于高能状态的工质, 目的是利用处于高能状态 的工质直接做功。  In a specific implementation, the heat sink 21 may also be disposed on the communication channel 1 at the working fluid outlet of the piston gas compression mechanism 9; the internal combustion combustion chamber 3 may also be disposed in the In the cylinder of the piston gas working mechanism 10, the working fluid flowing out of the internal combustion combustion chamber 3 is a working medium in a high energy state, and the purpose is to directly work by using the working medium in a high energy state.
实施例 4  Example 4
如图 4所示的双通道熵循环发动机, 其与实施例 1 的区别在于: 所述双通道熵循环发 动机还包括冷却器, 所述冷却器设为气液直混冷却器 20, 所述气液直混冷却器 20设在所述 活塞式气体做功机构 10的工质出口和所述活塞式气体压缩机构 9的工质入口之间的连通通 道上, 所述内燃燃烧室 3设为旁置内燃燃烧室 31, 在所述活塞式气体压缩机构 9的工质出 口与所述旁置内燃燃烧室 31之间的所述连通通道 1上设逆止阔 7, 从而使得从所述活塞式 气体压缩机构 9流出的工质经所述旁置内燃燃烧室 31加热后流向所述活塞式气体做功机构 10。  The two-channel entropy cycle engine shown in FIG. 4 differs from Embodiment 1 in that: the two-channel entropy cycle engine further includes a cooler, and the cooler is set as a gas-liquid direct charge cooler 20, the gas The liquid direct mixing cooler 20 is disposed on a communication passage between the working fluid outlet of the piston type gas working mechanism 10 and the working fluid inlet of the piston type gas compression mechanism 9, and the internal combustion combustion chamber 3 is disposed adjacent to The internal combustion combustion chamber 31 is provided with a check width 7 on the communication passage 1 between the working fluid outlet of the piston type gas compression mechanism 9 and the side internal combustion combustion chamber 31, thereby causing the piston gas to be The working fluid flowing out of the compression mechanism 9 is heated by the side internal combustion combustion chamber 31 and flows to the piston gas working mechanism 10.
本发明中, 所谓的气液直混冷却器 20是指在所述工质闭合回路上设冷却液体导入口和 导出口, 其原理是利用导入的液体吸收所述工质闭合回路内的气体工质的热量并使其降温, 升温后的液体再从所述工质闭合回路上导出; 在导出时可采用气液分离器以防止气体工质 流出。  In the present invention, the so-called gas-liquid direct-mixing cooler 20 means that a cooling liquid introduction port and a discharge port are provided on the closed circuit of the working fluid, and the principle is to absorb the gas in the closed circuit of the working fluid by using the introduced liquid. The heat is cooled and cooled, and the heated liquid is further discharged from the closed loop of the working fluid; a gas-liquid separator can be used for exporting to prevent the gas working fluid from flowing out.
作为可以变换的实施方式, 所述气液直混冷却器 20和所述逆止阔 7可以择一设置; 所 述冷却器可以设为其它形式的冷却器。  As an alternative embodiment, the gas-liquid direct mixing cooler 20 and the backstop 7 may alternatively be provided; the cooler may be provided as another type of cooler.
本发明的所有实施方式中, 都可以参照本实施例将所述内燃燃烧室 3 设为所述旁置燃 烧室 31。  In all of the embodiments of the present invention, the internal combustion combustion chamber 3 can be referred to as the side combustion chamber 31 with reference to the present embodiment.
实施例 5  Example 5
如图 5所示的双通道熵循环发动机, 其与实施例 3的区别在于: 所述散热器 21改设在 所述活塞式气体做功机构 10的工质出口和所述活塞式气体压缩机构 9的工质入口之间的所 说 明 书 ; 述连通通道 1上, 所述内燃燃烧室 3设置在所述活塞式气体做功机构 10的气缸内, 所述工 质导出口 6设在所述散热器 21和所述活塞式气体压缩机构 9的工质入口之间的所述连通通 道 1上, 所述双通道熵循环发动机还包括非直混冷凝冷却器 18, 所述工质导出口 6与所述 非直混冷凝冷却器 18的被冷却工质入口连通, 在所述非直混冷凝冷却器 18上设深冷液体 排出口 62, 所述深冷液体排出口 62与深冷液体工质储罐 16连通, 所述非直混冷凝冷却器 18对从所述活塞式气体做功机构 10流出并经所述散热器 21降温的工质进行进一步冷却, 产生的气体液化物 (如液体二氧化碳等)存入深冷液体工质储罐 16中, 此时, 所述非直混 冷凝冷却器 18的冷媒为冷凝温度较低的液氧液氮等。 The two-channel entropy cycle engine shown in FIG. 5 differs from the third embodiment in that: the radiator 21 is modified in the working fluid outlet of the piston gas working mechanism 10 and the piston gas compression mechanism 9 Between the entrances of the working fluids In the communication passage 1, the internal combustion combustion chamber 3 is disposed in a cylinder of the piston gas working mechanism 10, and the working fluid outlet 6 is disposed in the radiator 21 and the piston type gas compression mechanism The communication channel 1 between the working fluid inlets of the nine, the dual channel entropy cycle engine further includes a non-direct mixing condensing cooler 18, the working fluid outlet 6 and the non-direct mixing condensing cooler 18 Connected to the cooling medium inlet, a cryogenic liquid discharge port 62 is disposed on the non-direct mixed condensing cooler 18, and the cryogenic liquid discharge port 62 communicates with the cryogenic liquid working fluid storage tank 16, the non-direct mixing The condensing cooler 18 further cools the working fluid flowing out of the piston gas working mechanism 10 and cooled by the radiator 21, and the generated gas liquefied material (such as liquid carbon dioxide, etc.) is stored in the cryogenic liquid working fluid storage tank. In the above, at this time, the refrigerant of the non-direct mixed condensing cooler 18 is liquid oxygen liquid nitrogen or the like having a low condensation temperature.
作为可以变换的实施方式, 所述深冷液体工质储罐 16可以不设; 所述深冷液体排出口 62可以不设。  As an alternative embodiment, the cryogenic liquid working fluid storage tank 16 may not be provided; the cryogenic liquid discharge port 62 may not be provided.
本发明的所有所述工质导出口 6没有连通其它装置的实施方式中, 都可以参照本实施 例设置所述非直混冷凝冷却器 18及其相关结构。  In the embodiment in which all of the working fluid outlets 6 of the present invention are not connected to other devices, the non-direct mixed condensing cooler 18 and its related structure may be provided with reference to the present embodiment.
实施例 6  Example 6
如图 6所示的双通道熵循环发动机, 其与实施例 5的区别在于: 取消了所述深冷液体 工质储罐 16 , 所述内燃燃烧室 3改设在所述活塞式气体压缩机构 9的工质出口和所述活塞 式气体做功机构 10的工质入口之间的所述连通通道 1上, 在所述非直混冷凝冷却器 18上 增设不凝气出口 82,所述氧化剂源 4经所述非直混冷凝冷却器 18的被加热流体通道与所述 内燃燃烧室 3连通, 氧化剂可作为所述非直混冷凝冷却器 18的冷媒, 从而实现对所述工质 导出口 6出来的工质进行进一步冷却。 经所述非直混冷凝冷却器 18冷却后的工质, ·部分 被冷却为气体液化物从所述冷凝冷却液体出口 81流出, 另外一部分被冷却后仍然为气体形 式的为不凝气, 所述不凝气从所述不凝气出口 82流出。  The two-channel entropy cycle engine shown in FIG. 6 differs from the embodiment 5 in that the cryogenic liquid working fluid storage tank 16 is eliminated, and the internal combustion combustion chamber 3 is modified in the piston type gas compression mechanism. A non-condensing gas outlet 82 is added to the non-direct mixed condensing cooler 18 on the communication passage 1 between the working fluid outlet of the piston and the working fluid inlet of the piston gas working mechanism 10, the oxidant source 4 via the heated fluid passage of the non-direct mixing condensing cooler 18 in communication with the internal combustion combustion chamber 3, the oxidant acting as a refrigerant for the non-direct mixing condensing cooler 18, thereby effecting the working fluid outlet 6 The working fluid coming out is further cooled. The working medium cooled by the non-direct mixed condensing cooler 18 is partially cooled to flow out of the condensed cooling liquid outlet 81, and the other part is cooled, and is still in the form of gas, which is non-condensable. The non-condensable gas flows out from the non-condensable gas outlet 82.
具体实施时, 可选择地, 所述深冷液体排出口 62与深冷液体工质储罐 16连通, 所述 深冷液体工质储罐 16用来存储气体液化物; 所述不凝气出口 82与不凝气储罐 70连通, 所 述不凝气储罐 70用来存储不凝气, 或不凝气出口 82与所述活塞式气体压缩机构 9连通, 不凝气被进一步压缩后可重新进入工质闭合回路, 或所述不凝气出口 82还可以和所述工质 闭合回路的其他任何位置连通, 只要能将不凝气送回所述工质闭合回路中即可。  In a specific implementation, optionally, the cryogenic liquid discharge port 62 is in communication with a cryogenic liquid working fluid storage tank 16 for storing a gas liquefaction; the non-condensing gas outlet 82 is in communication with the non-condensable gas storage tank 70 for storing non-condensable gas, or the non-condensable gas outlet 82 is in communication with the piston type gas compression mechanism 9, and the non-condensable gas is further compressed. Re-entering the working fluid closed circuit, or the non-condensing gas outlet 82 may also be in communication with any other position of the working fluid closed circuit, as long as the non-condensable gas can be returned to the working fluid closed circuit.
实施例 7  Example 7
如图 7所示的双通道熵循环发动机, 其与实施例 3的区别在于: 将所述冷却器改设在 所述工质导出口 6和所述活塞式气体做功机构 10的工质入口之间的所述连通通道 1上, 并 设为两个, 即增设一个作为所述冷却器的非直混冷却器 23, 所述氧化剂源 4经所述非直混 冷却器 23的被加热流体通道与所述内燃燃烧室 3连通。  The two-channel entropy cycle engine shown in FIG. 7 differs from the embodiment 3 in that the cooler is relocated to the working fluid outlet 6 and the working inlet of the piston gas working mechanism 10. Between the communication passages 1, and two, that is, a non-direct mixing cooler 23 as the cooler is added, and the oxidant source 4 passes through the heated fluid passage of the non-direct mixing cooler 23. It is in communication with the internal combustion combustion chamber 3.
作为可以变换的实施方式, 所述非直混冷却器 23的被加热流体通道可以不与所述氧化 剂源 4连通; 所述氧化剂源 4可以直接与所述内燃燃烧室 3连通。  As an alternative embodiment, the heated fluid passage of the non-direct mixing cooler 23 may not be in communication with the oxidant source 4; the oxidant source 4 may be in direct communication with the internal combustion chamber 3.
实施例 8  Example 8
如图 8所示的双通道熵循环发动机, 其与实施例 7的区别在于: 在所述散热器 21和所 说 明 书 述非直混冷凝冷却器 18之间的连通通道 1 上设冷却液体排出口 61, 在所述非直混冷却器 23设深冷液体排出口 62。 The two-channel entropy cycle engine shown in FIG. 8 differs from the embodiment 7 in that: the radiator 21 and the Description The communication passage 1 between the non-direct mixing condensing coolers 18 is provided with a cooling liquid discharge port 61, and the non-direct mixing cooler 23 is provided with a cryogenic liquid discharge port 62.
所述工质经散热器冷却后, 冷凝温度较高的物质 (如水等) 已被冷凝, 可从所述冷却 液体排出口 61 以液态的形式排出; 不易被冷凝的工质在所述非直混冷凝冷却器 18中进一 步冷却, 被冷却后液化的工质经深冷液体排出口 62排出。 其中, 所述工质导出口 6相当于 包含所述冷却液体排出口 61和所述深冷液体排出口 62两个导出工质的排出口。  After the working medium is cooled by the radiator, a substance having a higher condensation temperature (such as water) has been condensed, and can be discharged from the cooling liquid discharge port 61 in a liquid form; the working medium which is not easily condensed is in the non-straight The mixed condensing cooler 18 is further cooled, and the liquefied working medium after being cooled is discharged through the cryogenic liquid discharge port 62. The working fluid outlet 6 corresponds to a discharge port including the cooling liquid discharge port 61 and the cryogenic liquid discharge port 62.
实施例 9  Example 9
如图 9所示的双通道熵循环发动机, 其与实施例 3的区别在于: 所述双通道熵循环发 动机还包括直连通道 100, 所述直连通道 100连通所述活塞式气体做功机构 10的工质出口 与所述活塞式压缩机构 9的工质入口, 所述直连通道 100相当于将所述活塞式气体做功机 构 10的工质出口与所述活塞式压缩机构 9的工质入口之间的所述连通通道 1分成了两条支 路, 其中一条支路 (设有冷却器的部分连通通道) 上设有所述冷却器, 另一条支路 (直连 通道 100)上未设置所述冷却器; 所述两条支路上均设有控制阔 17, 所述控制阔 17用于控 制所述两条支路的启闭。  The two-channel entropy cycle engine shown in FIG. 9 differs from Embodiment 3 in that: the two-channel entropy cycle engine further includes a direct connection passage 100, and the direct connection passage 100 communicates with the piston gas work mechanism 10 The working fluid outlet is connected to the working fluid inlet of the piston compression mechanism 9, and the direct connecting passage 100 is equivalent to the working fluid outlet of the piston gas working mechanism 10 and the working fluid inlet of the piston compression mechanism 9. The communication passage 1 is divided into two branches, one of which is provided with a cooler (partial communication passage provided with a cooler), and the other branch (directly connected to the passage 100) is not provided. The cooler is provided with a control width 17 for controlling the opening and closing of the two branches.
设所述直连通道 100的作用是: 当从所述活塞式气体做功机构 10的工质出口流出的工 质温度较低, 此时所述直连通道 100上的控制阔 17打开, 所述连通通道 1上的控制阀 17 关闭, 所述工质则可经所述直连通道 100流至所述活塞式气体压縮机构 9的气缸中; 当从 所述活塞式气体做功机构 10的工质出口流出的工质温度较高, 需要经冷却器进行冷却时, 所述直连通道 100上的控制阀 17关闭, 所述连通通道 1上的控制阀 17打开, 所述工质则 经连通通道 1流至所述活塞式气体压缩机构 9的气缸中。  The function of the direct connection channel 100 is: when the temperature of the working fluid flowing out from the working fluid outlet of the piston gas working mechanism 10 is low, the control width 17 on the direct connection channel 100 is opened. The control valve 17 on the communication passage 1 is closed, and the working fluid can flow through the direct connection passage 100 to the cylinder of the piston type gas compression mechanism 9; when working from the piston gas working mechanism 10 The temperature of the working fluid flowing out of the mass outlet is high, and when the cooling is required to be cooled by the cooler, the control valve 17 on the direct connecting passage 100 is closed, the control valve 17 on the communication passage 1 is opened, and the working medium is connected. The passage 1 flows into the cylinder of the piston type gas compression mechanism 9.
实施例 10  Example 10
如图 10所示的双通道熵循环发动机, 其与实施例 3的区别在于: 所述散热器 21改设 在所述活塞式气体做功机构 10的工质出口与所述活塞式气体压缩机构 9的工质入口之间的 所述连通通道 1上, 在所述活塞式气体做功机构 10的工质出口和所述活塞式气体压缩机构 的工质入口之间的所述连通通道 1上设另一个活塞式气体做功机构 10; 由于一次做功后 的气体工质, 还具有很高的能量, 还可以继续做功, 所述两个活塞式气体做功机构 10串联 设置的方式可以提高发动机的效率。  The two-channel entropy cycle engine shown in FIG. 10 differs from the third embodiment in that: the heat sink 21 is modified in the working fluid outlet of the piston gas working mechanism 10 and the piston gas compression mechanism 9 The communication passage 1 between the working fluid inlets is provided on the communication passage 1 between the working fluid outlet of the piston gas working mechanism 10 and the working fluid inlet of the piston gas compression mechanism. A piston type gas working mechanism 10; because of the high working energy of the gas working medium after one work, the work can be continued, and the two piston type gas working mechanisms 10 can be arranged in series to improve the efficiency of the engine.
实施例 11  Example 11
如图 11所示的双通道熵循环发动机, 其与实施例 3的区别在于: 所述散热器 21改设 在所述活塞式气体做功机构 10的工质出口和所述活塞式气体压缩机构 9的工质入口之间的 所述连通通道 1上, 所述氧化剂源 4经氧化剂入口与所述散热器 21和所述活塞式气体压缩 机构 9工质入口之间的所述连通通道 1连通, 在所述散热器 21和所述氧化剂入口之间的所 述连通通道 1上设冷却液体排出口 61, 在所述氧化剂入口和所述活塞式气体压缩机构 9的 所述连通通道 1上设液体二氧化碳出口 64, 所述氧化剂源 4用于对所述连通通道 1中的工 质进行进一步冷却。 — 垦 L υ ^ if The two-channel entropy cycle engine shown in FIG. 11 differs from the third embodiment in that: the radiator 21 is modified in the working fluid outlet of the piston gas working mechanism 10 and the piston gas compression mechanism 9 On the communication passage 1 between the working fluid inlets, the oxidant source 4 communicates with the communication passage 1 between the radiator 21 and the working inlet of the piston gas compression mechanism 9 via an oxidant inlet, a cooling liquid discharge port 61 is provided on the communication passage 1 between the radiator 21 and the oxidant inlet, and a liquid is provided on the communication passage 1 of the oxidant inlet and the piston type gas compression mechanism 9. A carbon dioxide outlet 64 for further cooling the working fluid in the communication passage 1. — 垦L υ ^ if
说 明 书 实施例 12  Description Book Example 12
如图 12所示的双通道熵循环发动机,其与实施例 6的区别在于:所述工质闭合回路中, 参与循环的气体中包含有氩气, 所述双通道熵循环发动机还包括不凝气储罐 70, 所述非直 混冷凝冷却器 18的不凝气出口 82经控制阀 17与所述不凝气储罐 70连通, 所述不凝气储 罐 70与所述工质闭合回路连通。  The two-channel entropy cycle engine shown in FIG. 12 differs from the embodiment 6 in that: in the working fluid closed circuit, the gas participating in the cycle contains argon gas, and the two-channel entropy cycle engine further includes non-condensing. The gas storage tank 70, the non-condensing gas outlet 82 of the non-direct mixing condensing cooler 18 is connected to the non-condensable gas storage tank 70 via a control valve 17, and the non-condensable gas storage tank 70 and the working fluid closed circuit Connected.
作为可以变换的实施方式, 所述控制阀 17可以改设为任何其它合适的控制装置。 实施例 13  As an alternative embodiment, the control valve 17 can be modified to any other suitable control device. Example 13
如图 13所示的双通道熵循环发动机, 其与实施例 3的区别在于: 所述散热器 21改设 在所述活塞式气体做功机构 10的工质出口和所述活塞式气体压缩机构 9的工质入口之间的 连通通道 1上, 所述双通道熵循环发动机还包括不凝气回储压缩机 71 , 所述不凝气回储压 缩机 71的进气口经控制阀 17与所述工质闭合回路连通, 所述不凝气回储压缩机 71的气体 出口与所述不凝气储罐 70连通, 所述不凝气储罐 70与所述工质闭合回路连通。  The two-channel entropy cycle engine shown in FIG. 13 differs from the third embodiment in that: the radiator 21 is modified in the working fluid outlet of the piston gas working mechanism 10 and the piston gas compression mechanism 9 The communication channel 1 between the working fluid inlets further includes a non-condensing gas returning compressor 71, and the air inlet of the non-condensing gas returning compressor 71 passes through the control valve 17 and the The working fluid is in closed loop communication, and the gas outlet of the non-condensable gas returning compressor 71 is in communication with the non-condensable gas storage tank 70, and the non-condensable gas storage tank 70 is in communication with the working fluid closed circuit.
作为可以变换的实施方式, 所述控制阀 17可以改设为任何其它合适的控制装置; 所述 不凝气回储压缩机 71可以不设。  As an alternative embodiment, the control valve 17 can be modified to any other suitable control device; the non-condensable return storage compressor 71 can be omitted.
实施例 14  Example 14
如图 14所示的双通道熵循环发动机, 其与实施例 1的区别在于: 在所述连通通道 1上 设回热器 33, 所述回热器 33 为热交换式回热器, 所述活塞式气体做功机构 10的工质出口 与所述活塞式气体压缩机构 9的工质入口之间的所述连通通道 1设为所述回热器 33的被冷 却流体通道, 所述活塞式气体压缩机构 9的工质出口与所述活塞式气体做功机构 10的工质 入口之间的所述连通通道 1设为所述回热器 33的被加热流体通道。  The two-channel entropy cycle engine shown in FIG. 14 differs from the first embodiment in that: a regenerator 33 is provided on the communication passage 1, and the regenerator 33 is a heat exchange regenerator, The communication passage 1 between the working fluid outlet of the piston type gas working mechanism 10 and the working medium inlet of the piston type gas compression mechanism 9 is set as the cooled fluid passage of the regenerator 33, the piston gas The communication passage 1 between the working fluid outlet of the compression mechanism 9 and the working fluid inlet of the piston gas working mechanism 10 is set as the heated fluid passage of the regenerator 33.
实施例 15  Example 15
如图 15所示的双通道熵循环发动机, 其与实施例 4的区别在于: 所述双通道熵循环发 动机还包括附属气体做功机构 102, 所述附属气体做功机构 102设为活塞式气体做功机构, 所述工质导出口 6与所述附属气体做功机构 102的进气口连通。 从所述工质导出口 6导出 的工质还处于高温高压状态, 可推动所述活塞式气体做功机构继续做功。  The dual-channel entropy cycle engine shown in FIG. 15 differs from the embodiment 4 in that the dual-channel entropy cycle engine further includes an auxiliary gas work mechanism 102, and the auxiliary gas work mechanism 102 is set as a piston gas work mechanism. The working fluid outlet 6 communicates with the inlet of the auxiliary gas working mechanism 102. The working fluid derived from the working fluid outlet 6 is also in a high temperature and high pressure state, and the piston gas working mechanism can be pushed to continue work.
选择型的, 所述附属气体做功机构 102还可以设为罗茨式气体做功机构、 螺杆式气体 做功机构或动力涡轮等其它形式的气体做功机构。  Alternatively, the auxiliary gas working mechanism 102 may be a gas working mechanism such as a Roots gas working mechanism, a screw gas working mechanism or a power turbine.
实施例 16  Example 16
如图 16所示的双通道熵循环发动机, 其与实施例 3的区别在于: 所述散热器 21改设 在所述活塞式气体做功机构 10的工质出口和所述活塞式气体压缩机构 9的工质入口之间的 所述连通通道 1上,所述工质导出口 6改设在所述散热器 21与所述活塞式气体做功机构 10 的工质出口之间的所述连通通道 1上,所述双通道熵循环发动机还包括直混冷凝冷却器 19, 所述直混冷凝冷却器 19的被冷却流体入口与所述工质导出口 6连通, 所述氧化剂源 4与所 述直混冷凝冷却器 19的被加热流体入口连通, 所述直混冷凝冷却器 19上设有深冷液体排 出口 62 , 所述深冷液体排出口 62与深冷液体工质储罐 16连通, 所述直混冷凝冷却器 19上 说 明 书 设有不凝气出口 82, 所述不凝气出口 82与所述工质闭合回路连通。氧化剂和不凝气经由所 述不凝气出口 82导入所述工质闭合回路中, 可选择地导到所述内燃燃烧室 3中。 The two-channel entropy cycle engine shown in FIG. 16 differs from the third embodiment in that: the radiator 21 is modified in the working fluid outlet of the piston gas working mechanism 10 and the piston gas compression mechanism 9 On the communication passage 1 between the working fluid inlets, the working fluid outlet 6 is modified between the radiator 21 and the working fluid outlet of the piston gas working mechanism 10 The dual-channel entropy cycle engine further includes a direct-mix condensing cooler 19, the cooled fluid inlet of the direct-mix condensing cooler 19 is in communication with the working fluid outlet 6, the oxidant source 4 and the straight The heated condensing cooler 19 is connected to the heated fluid inlet, and the direct mixing condensing cooler 19 is provided with a cryogenic liquid discharge port 62, and the cryogenic liquid discharge port 62 communicates with the cryogenic liquid working fluid storage tank 16 Straight-mixed condensing cooler 19 The description is provided with a non-condensing gas outlet 82, which is in communication with the working fluid closed circuit. An oxidant and non-condensable gas are introduced into the working fluid closed circuit via the non-condensable gas outlet 82, optionally into the internal combustion combustion chamber 3.
本实施例中, 将所述直混冷凝冷却器、 19的被加热流体出口设为所述不凝气出口 82 , 即 所述氧化剂源 4经所述直混冷凝冷却器 19的被加热流体出口与所述内燃燃烧室 3连通。  In this embodiment, the heated fluid outlet of the direct mixing condensing cooler, 19 is set as the non-condensing gas outlet 82, that is, the oxidant source 4 passes through the heated fluid outlet of the direct mixing condensing cooler 19. It is in communication with the internal combustion combustion chamber 3.
作为可以变换的实施方式, 可以将所述直混冷凝冷却器 19的被加热流体出口与所述不 凝气出口 82分置, 并经所述不凝气出口 82与所述工质闭合回路连通。  As an alternative embodiment, the heated fluid outlet of the direct mixing condensing cooler 19 may be separated from the non-condensable gas outlet 82, and connected to the working fluid closed circuit via the non-condensing gas outlet 82. .
实施例 17  Example 17
如图 17所示的双通道熵循环发动机, 其与实施例, 3的区别在于: 所述冷却器改设在所 述活塞式气体做功机构 10的工质出口和所述活塞式气体压缩机构 9的工质入口之间的所述 连通通道 1上, 且所述冷却器改设为吸附式冷却器 22, 所述活塞式气体做功机构 10的工质 出口和所述活塞式气体压缩机构 9的工质入口之间的所述连通通道 1设为所述吸附式冷却 器 22的被冷却流体通道。  The two-channel entropy cycle engine shown in FIG. 17 differs from the embodiment 3 in that: the cooler is modified in the working fluid outlet of the piston gas working mechanism 10 and the piston gas compression mechanism 9 On the communication channel 1 between the working fluid inlets, and the cooler is changed to an adsorption cooler 22, the working fluid outlet of the piston gas working mechanism 10 and the piston gas compression mechanism 9 The communication passage 1 between the working fluid inlets is set as the cooled fluid passage of the adsorption cooler 22.
实施例 18  Example 18
如图 18所示的双通道熵循环发动机, 其与实施例 3的区别在于: 所述内燃燃烧室 3以 独立腔体的形式设置在所述连通通道 1 内, 以保证所述工质燃烧更稳定更顺畅, 在所述内 燃燃烧室 3和所述活塞式气体做功机构 10的工质入口之间的所述连通通道 1内设三元催化 器 88。  The two-channel entropy cycle engine shown in FIG. 18 differs from the third embodiment in that: the internal combustion combustion chamber 3 is disposed in the communication passage 1 in the form of a separate cavity to ensure that the working fluid burns more. The stability is smoother, and a three-way catalyst 88 is disposed in the communication passage 1 between the internal combustion combustion chamber 3 and the working fluid inlet of the piston gas working mechanism 10.
本发明的所有实施方式中, 都可以参考本实施例将所述内燃燃烧室 3 以独立腔体的形 式设置在所述连通通道 1内。  In all embodiments of the present invention, the internal combustion combustion chamber 3 may be disposed in the communication passage 1 in the form of a separate cavity with reference to the present embodiment.
实施例 19  Example 19
如图 19所示的双通道熵循环发动机, 其与实施例 3的区别在于: 在所述活塞式气体做 功机构 10的工质出口和所述活塞式气体压缩机构 9的工质入口之间的所述连通通道 1内设 三元催化器 88。  The two-channel entropy cycle engine shown in Fig. 19 differs from the embodiment 3 in that between the working fluid outlet of the piston gas working mechanism 10 and the working fluid inlet of the piston gas compression mechanism 9. A three-way catalyst 88 is disposed in the communication passage 1 .
实施例 20  Example 20
如图 20所示的双通道熵循环发动机, 其与实施例 1的区别在于: 所述双通道熵循环发 动机还包括低温冷源 50 , 所述低温冷源 50与所述活塞式气体压缩机构 9连通, 所述低温冷 源 50用于提供低温物质, 所述低温物质用于冷却所述活塞式气体压缩机构 9的工质, 所述 低温冷源 50中的低温物质设为液氮。  The two-channel entropy cycle engine shown in FIG. 20 differs from the first embodiment in that: the two-channel entropy cycle engine further includes a low-temperature cold source 50, the low-temperature cold source 50 and the piston-type gas compression mechanism 9 In connection, the cryogenic cold source 50 is for providing a low temperature substance for cooling the working fluid of the piston type gas compression mechanism 9, and the low temperature substance of the low temperature cold source 50 is set to liquid nitrogen.
具体实施时, 可选择地, 所述低温冷源 50还可以与所述活塞式气体做功机构 10的工 质出口和所述活塞式气体压縮机构 9 的工质入口之间的连通通道连通, 所提供的低温物质 用于以冷却即将进入所述活塞式气体压缩机构 9的工质; 所述低温冷源 50还可以采用热交 换的方式对所述活塞式气体压缩机构 9中的工质或即将进入所述活塞式气体压缩机构 9中 的工质进行冷却。  In a specific implementation, the low temperature cold source 50 may also be connected to a communication channel between the working fluid outlet of the piston gas working mechanism 10 and the working fluid inlet of the piston gas compression mechanism 9 . The cryogenic material is provided for cooling the working fluid that is about to enter the piston gas compression mechanism 9; the cryogenic cold source 50 may also be heat exchanged to the working fluid in the piston gas compression mechanism 9 or The working fluid that is about to enter the piston type gas compression mechanism 9 is cooled.
实施例 21  Example 21
如图 21所示的双通道熵循环发动机, 其与实施例 1的区别在于: 所述双通道熵循环发 说 明 书 The two-channel entropy cycle engine shown in FIG. 21 differs from Embodiment 1 in that: the two-channel entropy cyclic transmission Description
动机还包括散热器 21、 涡轮动力机构 14和叶轮压气机 13, 所述散热器 21设置在所述活塞 式气体做功机构 10的工质出口和所述活塞式气体压缩机构 9的工质入口之间的所述连通通 道 1上, 所述工质导出口 6与所述涡轮动力机构 14的工质入口连通, 所述涡轮动力机构 14 的工质出口经附属冷却器 21 1 与所述叶轮压气机 13的工质入口连通, 所述叶轮压气机 13 的工质出口与所述连通通道 1连通;所述涡轮动力机构 14的工质出口与所述叶轮压气机 13 的工质入口之间的通道上设有附属工质导出口 66。 The motive further includes a radiator 21, a turbine power mechanism 14 and an impeller compressor 13, the radiator 21 being disposed at a working fluid outlet of the piston gas working mechanism 10 and a working fluid inlet of the piston gas compression mechanism 9. The working fluid outlet 6 communicates with the working fluid inlet of the turbine power mechanism 14 , and the working fluid outlet of the turbine power mechanism 14 is compressed by the auxiliary cooler 21 1 and the impeller. The working fluid inlet of the machine 13 is in communication, and the working fluid outlet of the impeller compressor 13 is in communication with the communication passage 1; between the working fluid outlet of the turbine power mechanism 14 and the working fluid inlet of the impeller compressor 13 An auxiliary working fluid outlet 66 is provided on the passage.
图中所示的所述附属工质导出口 66设在所述附属冷却器 21 1与所述叶轮压气机 13的 工质入口之间的通道上。  The auxiliary working fluid outlet 66 shown in the drawing is provided on the passage between the auxiliary cooler 21 1 and the working inlet of the impeller compressor 13.
具体实施时, 可选择地, 所述涡轮动力机构 14可与所述叶轮压气机 13共轴设置, 并 对其输出动力; 所述附属工质导出口 66还可设在所述涡轮动力机构 14的工质出口与所述 附属冷却器 21 1之间的通道上; 所述叶轮压气机 13的工质出口与设在所述工质闭合回路上 的连通口连通, 该连通口和所述工质导出口 6设在所述工质闭合回路上的不同位置。  In a specific implementation, optionally, the turbine power mechanism 14 may be coaxially disposed with the impeller compressor 13 and output power thereto; the auxiliary working fluid outlet 66 may also be disposed at the turbine power mechanism 14 a working medium outlet and a passage between the auxiliary cooler 21 1; a working fluid outlet of the impeller compressor 13 communicates with a communication port provided on the closed circuit of the working fluid, the communication port and the working The mass outlets 6 are disposed at different locations on the closed circuit of the working fluid.
实施例 22  Example 22
如图 22所示的双通道熵循环发动机, 其与实施例 3的区别在于: 所述散热器 21改设 在所述活塞式气体做功机构 10的工质出口和所述活塞式气体压缩机构 9的工质入口之间的 所述连通通道 1上, 所述工质导出口 6改设在所述活塞式气体做功机构 10的工质出口和所 述散热器 21之间的连通通道上, 所述氧化剂源 4设为四类门气缸活塞机构 99, 所述四类门 气缸活塞机构 99受使所述四类门气缸活塞机构 99按照吸气冲程-压气供气冲程 -气体回充做 功冲程 -排气冲程工作模式循环工作的四类门控制机构控制, 所述供气口 993为所述氧化剂 源 4的氧化剂出口, 所述回充口 994与所述工质导出口 6连通。  The two-channel entropy cycle engine shown in FIG. 22 differs from the third embodiment in that: the radiator 21 is modified in the working fluid outlet of the piston gas working mechanism 10 and the piston gas compression mechanism 9 On the communication passage 1 between the working fluid inlets, the working fluid outlet 6 is modified on a communication passage between the working fluid outlet of the piston gas working mechanism 10 and the radiator 21, The oxidant source 4 is set as a four-type door cylinder piston mechanism 99, and the four-type door cylinder piston mechanism 99 is caused to perform the power stroke of the four-type door cylinder piston mechanism 99 according to the intake stroke-pressure gas supply stroke-gas back charge- The exhaust stroke operation mode is controlled by four types of door control mechanisms that are cyclically operated. The air supply port 993 is an oxidant outlet of the oxidant source 4, and the refill port 994 is in communication with the working fluid outlet 6.
被所述四类门气缸活塞机构 99压缩后的氧化剂, 经所述供气口 993进入所述内燃燃烧 室 3中, 所述燃料源 5向所述内燃燃烧室 3喷入燃料, 所述氧化剂和所述燃料在所述内燃 燃烧室 3 内发生燃烧化学反应, 产生的大量热量加热所述工质闭合回路中的工质, 混合燃 烧产物推动所述活塞式气体做功机构 10做功, 从所述活塞式气体做功机构 10流出的工质 经所述工质导出口 6进入所述四类门气缸活塞机构 99, 所述工质的余热推动所述四类门气 缸活塞机构 99做功后, 经所述排气口 992排出所述四类门气缸活塞机构。  The oxidant compressed by the four-type door cylinder piston mechanism 99 enters the internal combustion combustion chamber 3 through the air supply port 993, and the fuel source 5 injects fuel into the internal combustion combustion chamber 3, the oxidant And a combustion chemical reaction occurs between the fuel in the internal combustion combustion chamber 3, a large amount of heat generated to heat the working fluid in the closed circuit of the working fluid, and the mixed combustion product pushes the piston gas working mechanism 10 to perform work, The working fluid flowing out of the piston gas working mechanism 10 enters the four-type door cylinder piston mechanism 99 through the working fluid outlet 6 , and the residual heat of the working medium pushes the four types of door cylinder piston mechanism 99 to work, The exhaust port 992 discharges the four types of door cylinder piston mechanisms.
作为可以变换的实施方式,可以将所述氧化剂源 4与所述四类门气缸活塞机构 99分置。 实施例 23  As an alternative embodiment, the oxidant source 4 can be separated from the four type of door cylinder piston mechanism 99. Example 23
如图 23所示的双通道熵循环发动机, 其与实施例 4的区别在于: 所述冷却器设为散热 器 21 , 所述旁置内燃燃烧室 31设为四类门气缸活塞机构 99, 所述氧化剂源 4和所述燃料 源 5与所述进气口 991连通, 在所述四类门气缸活塞机构 99上设火花塞 15, 所述氧化剂源 4和所述燃料源 5在所述四类门气缸活塞机构 99内进行燃烧化学反应后, 产生的部分高温 高压工质可用来使四类门气缸活塞机构 99做功, 另外一部分工质经所述供气口 993进入所 述工质闭合回路,和被它加热的工质一起进入所述活塞式气体做功机构 10,所述回充口 994 与所述工质导出口 6连通, 从所述工质导出口 6导出的部分工质从所述回充口 994导入所 述四类门气缸活塞机构 99内, 所述四类门气缸活塞机构 99经所述排气口 992排出部分工 质。 The two-channel entropy cycle engine shown in FIG. 23 differs from the fourth embodiment in that: the cooler is a radiator 21, and the bypass internal combustion chamber 31 is set as a four-type door cylinder piston mechanism 99. The oxidant source 4 and the fuel source 5 are in communication with the air inlet 991, and a spark plug 15 is disposed on the four-type door cylinder piston mechanism 99, and the oxidant source 4 and the fuel source 5 are in the four categories. After the combustion chemical reaction is performed in the door cylinder piston mechanism 99, part of the high temperature and high pressure working fluid generated can be used to make the four types of door cylinder piston mechanism 99 work, and another part of the working medium enters the working fluid closed circuit through the air supply port 993. Entering the piston gas working mechanism 10 together with the working medium heated by the working fluid, the refilling port 994 is in communication with the working fluid outlet 6, and the part of the working fluid discharged from the working fluid outlet 6 is from the Refill port 994 import office In the four types of door cylinder piston mechanism 99, the four types of door cylinder piston mechanism 99 discharges part of the working medium through the exhaust port 992.
实施例 24  Example 24
如图 24所示的双通道熵循环发动机, 其与实施例 3的区别在于: 所述双通道熵循环发 动机还包括氧化剂传感器 51和氧化剂控制装置 52, 所述氧化剂传感器 51包含有氧化剂探 头, 所述氧化剂探头设在连通通道 1 内, 所述氧化剂传感器 51 对所述氧化剂控制装置 52 提供信号, 所述氧化剂源 4经氧化剂控制阀 53与所述工质闭合回路连通, 所述氧化剂控制 装置 52控制所述氧化剂控制阀 5说3打开或关闭, 以调整工质闭合回路中的氧化剂的量。  The two-channel entropy cycle engine shown in FIG. 24 differs from Embodiment 3 in that: the two-channel entropy cycle engine further includes an oxidant sensor 51 and an oxidant control device 52, and the oxidant sensor 51 includes an oxidant probe. The oxidant probe is disposed in the communication passage 1, and the oxidant sensor 51 provides a signal to the oxidant control device 52. The oxidant source 4 is in communication with the working fluid closed circuit via an oxidant control valve 53. The oxidant control device 52 The oxidant control valve 5 is controlled to open or close to adjust the amount of oxidant in the closed circuit of the working fluid.
实施例 25  Example 25
如图 25所示的双通道熵循环发动机, 其与实施例 24的区别在于: 所述活塞式气体压 缩机构 9和所述活塞式气体做功机构 10均设为活塞液体机构 90, 所述活塞液体机构 90包 括气液缸 91和气液隔离结构 92, 所述气液隔离结构 92设在所述气液缸 91内。所述气液缸 91的液体端与液压动力机构 96连通, 所述液压动力机构 96对外输出动力, 所述液压动力 机构 96与液体工质回送系统 97连通, 所述液体工质回送系统 97与所述气液缸 91的液体  The two-channel entropy cycle engine shown in FIG. 25 differs from the embodiment 24 in that: the piston type gas compression mechanism 9 and the piston gas work mechanism 10 are each configured as a piston liquid mechanism 90, the piston liquid The mechanism 90 includes a gas-liquid cylinder 91 and a gas-liquid isolation structure 92, and the gas-liquid insulation structure 92 is disposed in the gas-liquid cylinder 91. The liquid end of the gas-liquid cylinder 91 is in communication with a hydraulic power mechanism 96, and the hydraulic power mechanism 96 outputs power externally. The hydraulic power mechanism 96 is in communication with the liquid working fluid returning system 97. The liquid working fluid returning system 97 and The liquid of the gas cylinder 91
 Book
端连通; 所述液压动力机构 96和所述液体工质回送系统 97受过程控制机构 98控制。 所述 气液缸 91的气体工质对所述气液隔离结构 92的压力大于所述气液缸 91内的液体和所述气 液隔离结构 92做往复运动时的惯性力之和, 以使所述气液隔离结构 92不撞上所述气液缸 91的缸盖。 The end is connected; the hydraulic power mechanism 96 and the liquid working fluid return system 97 are controlled by a process control mechanism 98. The gas working medium of the gas-liquid cylinder 91 has a pressure greater than the sum of the inertial forces of the liquid in the gas-liquid cylinder 91 and the gas-liquid isolation structure 92 when the gas-liquid isolation structure 92 is reciprocated. The gas-liquid isolation structure 92 does not hit the cylinder head of the gas-liquid cylinder 91.
可选择地, 将所述活塞式气体压缩机构 9和所述活塞式气体做功机构 10中的一个设为 活塞液体机构 90及其相应的辅助装置。  Alternatively, one of the piston type gas compression mechanism 9 and the piston type gas work mechanism 10 is set as the piston liquid mechanism 90 and its corresponding auxiliary means.
在本发明的所有实施方式中, 所述的内燃燃烧室 3均可设为连续燃烧室或间歇燃烧室, 设为间歇燃烧室时, 可以根据需要选择不同的间歇燃烧时序关系。  In all of the embodiments of the present invention, the internal combustion combustion chamber 3 may be a continuous combustion chamber or a intermittent combustion chamber, and when it is a batch combustion chamber, different intermittent combustion timing relationships may be selected as needed.
在本发明的所有实施方式中, 所述内燃燃烧室 3 排出的物质的质量流量大于从所述工 质回路外导入所述内燃燃烧室 3的物质的质量流量; 在包含所述旁置内燃燃烧室 31的结构 中, 应使流入所述活塞式气体做功机构 10 的工质的质量流量大于所述旁置内燃燃烧室 31 排出的物质的质量流量。  In all embodiments of the present invention, the mass flow rate of the substance discharged from the internal combustion combustion chamber 3 is greater than the mass flow rate of the substance introduced into the internal combustion combustion chamber 3 from outside the working fluid circuit; and the side internal combustion is included In the structure of the chamber 31, the mass flow rate of the working fluid flowing into the piston type gas working mechanism 10 is made larger than the mass flow rate of the substance discharged from the side internal combustion combustion chamber 31.
在本发明的所有实施方式中, 都可以将所述工质闭合回路的压力设为至少大于 2MPa; 可选择地,将所述工质闭合回路的承压能力设为大于 2.5MPa、3MPa、3.5MPa、4MPa、4.5MPa、 5MPa、 5.5MPa、 6MPa、 6.5MPa、 7MPa、 7.5MPa、 8MPa 8.5MPa、 9MPa、 9.5MPa、 10MPa、 10.5MPa、 l lMPa、 1 1.5MPa、 12MPa、 12.5MPa、 13MPa、 13.5MPa、 14MPa、 14.5MPa、 15MPa、 15.5MPa、 16MPa、 16.5MPa、 17MPa、 17.5MPa、 18MPa、 18.5MPa、 19MPa、 19.5MPa、 20MPa、 20.5MPa、 21MPa、 22MPa、 23MPa、 24MPa、 25MPa、 26MPa、 27MPa、 28MPa、 29MPa、 30MPa、 31MPa、 32MPa、 33MPa、 34MPa、 35MPa、 36MPa> 37MPa、 38MPa、 39MPa或 大于 40MPa。 相应地, 所述氧化剂源 4和所述燃料源 5的承压能力也设为上述同样的数值 范围。 由于需要将所述氧化剂源 4或所述燃料源 5中的物质向所述工质闭合回路内喷射, 说 明 书 因此在实际应用中, 所述氧化剂源 4或所述燃料源 5的承压能力一般设为大于所述工质闭 合回路的承压能力。 In all embodiments of the present invention, the pressure of the working fluid closed circuit may be set to be at least greater than 2 MPa; alternatively, the pressure bearing capacity of the working fluid closed circuit is set to be greater than 2.5 MPa, 3 MPa, 3.5. MPa, 4 MPa, 4.5 MPa, 5 MPa, 5.5 MPa, 6 MPa, 6.5 MPa, 7 MPa, 7.5 MPa, 8 MPa 8.5 MPa, 9 MPa, 9.5 MPa, 10 MPa, 10.5 MPa, l lMPa, 1 1.5 MPa, 12 MPa, 12.5 MPa, 13 MPa, 13.5MPa, 14MPa, 14.5MPa, 15MPa, 15.5MPa, 16MPa, 16.5MPa, 17MPa, 17.5MPa, 18MPa, 18.5MPa, 19MPa, 19.5MPa, 20MPa, 20.5MPa, 21MPa, 22MPa, 23MPa, 24MPa, 25MPa, 26MPa, 27MPa, 28MPa, 29MPa, 30MPa, 31MPa, 32MPa, 33MPa, 34MPa, 35MPa, 36MPa> 37MPa, 38MPa, 39MPa or more than 40MPa. Accordingly, the pressure bearing capacity of the oxidant source 4 and the fuel source 5 is also set to the same numerical range as described above. Due to the need to spray the oxidant source 4 or the substance in the fuel source 5 into the closed loop of the working fluid, The specification therefore applies in a practical application that the pressure bearing capacity of the oxidant source 4 or the fuel source 5 is generally set to be greater than the pressure bearing capacity of the working fluid closed circuit.
显然, 本发明不限于以上实施例, 根据本领域的公知技术和本发明所公开的技术方案, 可以推导出或联想出许多变型方案, 所有这些变型方案, 也应认为是本发明的保护范围。  It is apparent that the present invention is not limited to the above embodiments, and many variations can be derived or conceived according to the well-known art in the art and the technical solutions disclosed in the present invention, and all such modifications are also considered to be the scope of protection of the present invention.

Claims

权 利 要求 书 Claim
1. 一种双通道熵循环发动机,包括活塞式气体压缩机构(9)、活塞式气体做功机构( 10) 和两条连通通道 (1), 其特征在于: 所述活塞式气体压缩机构 (9) 的工质出口经一条所述 连通通道 (1) 与所述活塞式气体做功机构 (10) 的工质入 U连通, 所述活塞式气体做功机 构 (10) 的工质出口经另一条所述连通通道 (1) 与所述活塞式气体压缩机构 (9) 的工质 入口连通; 所述活塞式气体压缩机构 (9) 经两条所述连通通道 (1) 与所述活塞式气体做 功机构 (10) 连通构成工质闭合回路; 在所述工质闭合回路内设内燃燃烧室 (3), 在所述 工质闭合回路上设工质导出口 (6)。 A two-channel entropy cycle engine comprising a piston type gas compression mechanism (9), a piston gas work mechanism (10) and two communication passages (1), characterized in that: the piston type gas compression mechanism (9) The working medium outlet is connected to the working medium of the piston gas working mechanism (10) via a communication passage (1), and the working fluid outlet of the piston gas working mechanism (10) passes through another The communication passage (1) is in communication with the working fluid inlet of the piston gas compression mechanism (9); the piston gas compression mechanism (9) performs work with the piston gas via the two communication passages (1) The mechanism (10) is connected to form a working fluid closed circuit; an internal combustion combustion chamber (3) is disposed in the working fluid closed circuit, and a working fluid outlet (6) is disposed on the working fluid closed circuit.
2. 如权利要求 1所述双通道熵循环发动机, 其特征在于: 所述内燃燃烧室(3)设在以 所述活塞式气体压缩机构 (9) 的工质出口为上游和以所述活塞式气体做功机构 (10) 的工 质出口为下游的所述工质闭合回路内。  2. The two-channel entropy cycle engine according to claim 1, wherein: said internal combustion combustion chamber (3) is disposed upstream of said working fluid outlet of said piston type gas compression mechanism (9) and said piston The working fluid outlet of the gas working mechanism (10) is in the closed loop of the working fluid downstream.
3. 如权利要求 1或 2所述双通道熵循环发动机, 其特征在于: 所述内燃燃烧室(3)设 为旁置内燃燃烧室 (31)。  3. A two-channel entropy cycle engine according to claim 1 or 2, characterized in that the internal combustion combustion chamber (3) is provided as a side-by-side internal combustion chamber (31).
4. 如权利要求 1所述双通道熵循环发动机, 其特征在于: 所述双通道熵循环发动机还 包括冷却器, 所述冷却器设置在所述工质闭合回路上。  4. The dual channel entropy cycle engine of claim 1 wherein: said dual channel entropy cycle engine further comprises a chiller disposed on said working fluid closed circuit.
5. 如权利要求 4所述双通道熵循环发动机, 其特征在于: 所述双通道熵循环发动机还 包括直连通道 (100), 所述直连通道 (100) 连通所述活塞式气体做功机构 (10) 的工质出 口与所述活塞式压缩机构 (9) 的工质入口, 所述冷却器设置在所述直连通道 (100) 上或 设所述活塞式气体做功机构 (10) 的工质出口与所述活塞式气体压缩机构 (9) 的工质入口 之间的所述连通通道(1)上, 在所述直连通道(100)上和在所述活塞式气体做功机构(10) 的工质出口与所述活塞式气体压缩机构 (9) 的工质入口之间的所述连通通道 (1) 上设控 制阀 (17)。  5. The dual channel entropy cycle engine of claim 4, wherein: the dual channel entropy cycle engine further comprises a direct connection channel (100), the direct connection channel (100) communicating with the piston gas working mechanism a working fluid outlet of (10) and a working fluid inlet of the piston compression mechanism (9), the cooler being disposed on the direct connection passage (100) or provided with the piston gas working mechanism (10) The communication passage (1) between the working fluid outlet and the working fluid inlet of the piston type gas compression mechanism (9), the direct connection passage (100) and the piston gas working mechanism ( A control valve (17) is disposed on the communication passage (1) between the working fluid outlet of 10) and the working fluid inlet of the piston gas compression mechanism (9).
6. 如权利要求 4所述双通道熵循环发动机, 其特征在于: 所述双通道熵循环发动机还 包括氧化剂源 (4), 所述冷却器设置在所述活塞式气体做功机构 (10) 的工质出口与所述 活塞式气体压缩机构 (9) 工质入口之间的所述连通通道 (1) 上, 所述氧化剂源 (4) 经氧 化剂入口与所述冷却器与所述活塞式气体压缩机构(9)的工质入口之间的所述连通通道( 1 ) 连通,在所述冷却器和所述氧化剂入口之间的所述连通通道(1)上设冷却液体排出口(61), 在所述氧化剂入口和所述活塞式气体压缩机构 (9) 之间的所述连通通道 (1) 上设液体二 氧化碳出口 (64)。  6. The dual channel entropy cycle engine according to claim 4, wherein: said two-channel entropy cycle engine further comprises an oxidant source (4), said cooler being disposed in said piston gas working mechanism (10) The communication passage (1) between the working fluid outlet and the piston gas compression mechanism (9) working fluid inlet, the oxidant source (4) passing through the oxidant inlet and the cooler and the piston gas The communication passage (1) between the working fluid inlets of the compression mechanism (9) is in communication, and a cooling liquid discharge port (61) is provided on the communication passage (1) between the cooler and the oxidant inlet. A liquid carbon dioxide outlet (64) is disposed on the communication passage (1) between the oxidant inlet and the piston gas compression mechanism (9).
7. 如权利要求 4所述双通道熵循环发动机, 其特征在于: 所述冷却器设在以所述活塞 式气体做功机构 (10) 的工质出口为上游和以所述内燃燃烧室 (3) 的工质入口为下游的所 述工质闭合回路上。  7. The dual channel entropy cycle engine according to claim 4, wherein: said cooler is disposed upstream of said working fluid outlet of said piston gas working mechanism (10) and said internal combustion combustion chamber (3) The working fluid inlet is closed on the downstream working fluid.
8. 如权利要求 4所述双通道熵循环发动机,其特征在于:所述冷却器设为散热器(21)、 气液直混冷却器 (20)、 吸附式制冷器 (22) 或非直混冷却器 (23)。  8. The dual channel entropy cycle engine according to claim 4, wherein the cooler is configured as a radiator (21), a gas-liquid direct mixing cooler (20), an adsorption refrigerator (22) or a non-straight Mix cooler (23).
9. 如权利要求 8所述双通道熵循环发动机, 其特征在于: 所述双通道熵循环发动机还 包括氧化剂源 (4), 所述氧化剂源 (4) 经所述非直混冷却器 (23) 的被加热流体通道与所 权利 要求 书 述内燃燃烧室 (3 ) 连通。 9. The dual channel entropy cycle engine of claim 8 wherein: said dual channel entropy cycle engine further comprises an oxidant source (4), said oxidant source (4) being passed through said non-direct mixer cooler (23) Heated fluid channel and The internal combustion combustion chamber (3) of the claims is in communication.
10. 如权利要求 8或 9所述双通道熵循环发动机,其特征在于:在所述非直混冷却器 ( 23 ) 上设深冷液体排出口 (62)。  10. A two-channel entropy cycle engine according to claim 8 or 9, characterized in that a cryogenic liquid discharge port (62) is provided on the non-direct mixing cooler (23).
11. 如权利要求 4、 5、 7、 8或 9所述双通道熵循环发动机, 其特征在于: 所述双通道 熵循环发动机还包括冷却液体排出口 (61 ), 所述冷却液体排出口 (61 ) 设在所述冷却器和 所述工质导出口 (6) 之间的所述连通通道 (1 ) 上。  11. The dual channel entropy cycle engine according to claim 4, 5, 7, 8 or 9, wherein: the two-channel entropy cycle engine further comprises a cooling liquid discharge port (61), and the cooling liquid discharge port ( 61) is disposed on the communication passage (1) between the cooler and the working fluid outlet (6).
12. 如权利要求 1或 2所述双通道熵循环发动机, 其特征在于: 所述双通道熵循环发动 机还包括氧化剂源 (4), 所述氧化剂源 (4 ) 与所述工质闭合回路连通。  12. The dual channel entropy cycle engine according to claim 1 or 2, wherein: the two-channel entropy cycle engine further comprises an oxidant source (4), the oxidant source (4) being in communication with the working fluid closed loop .
13. 如权利要求 12所述双通道熵循环发动机, 其特征在于: 所述氧化剂源(4)与所述 内燃燃烧室 (3 ) 连通。  13. A two-channel entropy cycle engine according to claim 12, characterized in that said oxidant source (4) is in communication with said internal combustion chamber (3).
14. 如权利要求 12所述双通道熵循环发动机, 其特征在于: 所述熵循环发动机还包括 直混冷凝冷却器(19),所述直混冷凝冷却器(19 )的被冷却流体入口与所述工质导出口(6 ) 连通, 所述氧化剂源 (4) 与所述直混冷凝冷却器 (19) 的被加热流体入口连通, 并经所述 直混冷凝冷却器 (19) 的被加热流体出口与所述工质闭合回路连通。  14. The dual channel entropy cycle engine of claim 12, wherein: said entropy cycle engine further comprises a direct mixing condensing cooler (19), said cooled fluid inlet of said direct mixing condensing cooler (19) The working fluid outlet (6) is in communication, the oxidant source (4) is in communication with the heated fluid inlet of the direct mixing condensing cooler (19), and is passed through the direct mixing condensing cooler (19) A heated fluid outlet is in communication with the working fluid closed circuit.
15. 如权利要求 14所述双通道熵循环发动机, 其特征在于: 所述氧化剂源(4 )经所述 直混冷凝冷却器 (19) 的被加热流体出口与所述内燃燃烧室 (3 ) 连通。  15. The two-channel entropy cycle engine according to claim 14, wherein: said oxidant source (4) passes through said heated fluid outlet of said direct mixing condensing cooler (19) and said internal combustion chamber (3) Connected.
16. 如权利要求 12所述双通道熵循环发动机, 其特征在于: 所述氧化剂源(4)的压力 大于 2MPa。  16. The two-channel entropy cycle engine of claim 12, wherein: said oxidant source (4) has a pressure greater than 2 MPa.
17. 如权利要求 2所述双通道熵循环发动机, 其特征在于: 所述工质导出口 (6 ) 设在 以所述活塞式气体做功机构 (10) 的工质出口为上游和以所述内燃燃烧室 (3 ) 的工质入口 为下游的所述工质闭合回路上。  17. The two-channel entropy cycle engine according to claim 2, wherein: said working fluid outlet (6) is disposed upstream of said working fluid outlet of said piston gas working mechanism (10) and said The working fluid inlet of the internal combustion combustion chamber (3) is on the downstream closed circuit of the working fluid.
18. 如权利要求 1所述双通道熵循环发动机, 其特征在于: 所述双通道熵循环发动机还 包括非直混冷凝冷却器 (18), 所述非直混冷凝冷却器 (18 ) 的被冷却工质入口与所述工质 导出口 (6) 连通。  18. The dual channel entropy cycle engine of claim 1 wherein: said dual channel entropy cycle engine further comprises a non-direct mixed condensing cooler (18), said non-direct mixed condensing cooler (18) being A cooling medium inlet is connected to the working fluid outlet (6).
19. 如权利要求 14所述双通道熵循环发动机, 其特征在于: 所述直混冷凝冷却器(19) 上设深冷液体排出口 (62)。  19. The two-channel entropy cycle engine according to claim 14, wherein: the direct-mix condensing cooler (19) is provided with a cryogenic liquid discharge port (62).
20. 如权利要求 18所述双通道熵循环发动机,其特征在于:所述非直混冷凝冷却器(18 ) 设深冷液体排出口 (62 )。  20. A two-channel entropy cycle engine according to claim 18, wherein said non-direct mixing condensing cooler (18) is provided with a cryogenic liquid discharge port (62).
21. 如权利要求 19或 20所述双通道熵循环发动机, 其特征在于: 所述双通道熵循环发 动机还包括深冷液体工质储罐 (16), 所述深冷液体工质储罐 (16 ) 与所述深冷液体排出口 21. The dual channel entropy cycle engine of claim 19 or 20, wherein: the dual channel entropy cycle engine further comprises a cryogenic liquid working fluid storage tank (16), the cryogenic liquid working fluid storage tank ( 16) with the cryogenic liquid discharge port
(62 )连通。 (62) Connected.
22 如权利要求 14所述双通道熵循环发动机, 其特征在于: 所述直混冷凝冷却器(19) 上设不凝气出口 (82)。  A two-channel entropy cycle engine according to claim 14, wherein: said direct mixing condensing cooler (19) is provided with a non-condensable gas outlet (82).
23. 如权利要求 18所述双通道熵循环发动机,其特征在于:所述非直混冷凝冷却器(18 ) 设不凝气出口 (82)。 权利 要 求 书 23. A two-channel entropy cycle engine according to claim 18, wherein said non-direct mixing condensing cooler (18) is provided with a non-condensing gas outlet (82). Claim
24. 如权利要求 22或 23所述双通道熵循环发动机,其特征在于:所述不凝气出口(82 ) 与所述工质闭合回路连通。  24. A two-channel entropy cycle engine according to claim 22 or 23, wherein said non-condensable gas outlet (82) is in communication with said working fluid closed circuit.
25. 如权利要求 18所述熵循环发动机, 其特征在于: 所述熵循环发动机还包括氧化剂 源 (4) , 所述氧化剂源 (4 ) 经所述非直混冷凝冷却器 (18 ) 的被加热流体通道与所述内燃 燃烧室 (3 ) 连通。  25. The entropy cycle engine of claim 18, wherein: said entropy cycle engine further comprises an oxidant source (4), said oxidant source (4) being passed through said non-direct mixing condensing cooler (18) A heating fluid passage is in communication with the internal combustion chamber (3).
26. 如权利要求 1所述双通道熵循环发动机, 其特征在于: 在所述工质导出口 (6 ) 上 设控制阀 (17)。  26. The dual channel entropy cycle engine of claim 1 wherein: a control valve (17) is provided on said working fluid outlet (6).
27. 如权利要求 26所述双通道熵循环发动机, 其特征在于: 所述控制阀 (17) 设为压 力控制阀, 所述压力控制阀控制所述工质导出口 (6) 在所述工质闭合回路内的压力超过设 定限度时导出工质。  27. The two-channel entropy cycle engine according to claim 26, wherein: said control valve (17) is set as a pressure control valve, and said pressure control valve controls said working fluid outlet (6) at said work The working fluid is derived when the pressure in the closed loop exceeds the set limit.
28. 如权利要求 26所述双通道熵循环发动机, 其特征在于: 所述压力控制阔受使所述 工质闭合回路中的最低压力大于 0.2MPa的控制机构控制。  28. The dual channel entropy cycle engine of claim 26 wherein: said pressure control is controlled by a control mechanism that causes a minimum pressure in said working fluid closed circuit to be greater than 0.2 MPa.
29. 如权利要求 26所述双通道熵循环发动机, 其特征在于: 所述控制阀 (17) 受幵启 度控制机构控制, 所述开启度控制机构根据所述工质闭合回路内的压力设定范围控制所述 控制阙 ( 17 ) 的开启度, 使所述工质导出口 (6) 在某种开启度下处于常开状态。  29. The dual channel entropy cycle engine according to claim 26, wherein: said control valve (17) is controlled by a threshold control mechanism, and said opening degree control mechanism is configured according to a pressure in said working fluid closed circuit The range is controlled to control the degree of opening of the control port (17) such that the working fluid outlet (6) is in a normally open state at a certain degree of opening.
30. 如权利要求 1或 17所述双通道熵循环发动机, 其特征在于: 所述双通道熵循环发 动机还包括附属气体做功机构(102),所述工质导出口(6)与所述附属气体做功机构(102 ) 的工质入口连通。  30. The dual channel entropy cycle engine according to claim 1 or 17, wherein: the dual channel entropy cycle engine further comprises an auxiliary gas work mechanism (102), and the working fluid outlet (6) and the subsidiary The working inlet of the gas working mechanism (102) is connected.
31. 如权利要求 1或 17所述双通道熵循环发动机, 其特征在于: 所述双通道熵循环发 动机还包括储气罐 (60), 所述储气罐 (60) 与所述工质导出口 (6) 连通。  31. The dual channel entropy cycle engine of claim 1 or 17, wherein: the dual channel entropy cycle engine further comprises a gas storage tank (60), the gas storage tank (60) and the working medium guide The exit (6) is connected.
32. 如权利要求 1所述双通道熵循环发动机, 其特征在于: 在所述连通通道 (1 ) 上设 逆止阀 (7)。  32. The two-channel entropy cycle engine according to claim 1, characterized in that: a check valve (7) is provided on the communication passage (1).
33. 如权利要求 1所述双通道熵循环发动机, 其特征在于: 在以所述活塞式气体做功机 构 (10) 的工质出口为上游、 以所述活塞式气体压缩机构 (9 ) 的工质入口为下游的所述工 质闭合回路上设另一个活塞式气体做功机构 (10)。  33. The two-channel entropy cycle engine according to claim 1, wherein: the working fluid outlet of the piston gas working mechanism (10) is upstream, and the piston gas compression mechanism (9) is The mass inlet is provided with another piston gas working mechanism (10) on the closed circuit of the working fluid downstream.
34. 如权利要求 1或 33所述熵循环发动机,其特征在于:所述活塞式气体做功机构( 10 ) 对所述活塞式气体压缩机构 (9) 输出动力。  The entropy cycle engine according to claim 1 or 33, characterized in that the piston type gas working mechanism (10) outputs power to the piston type gas compression mechanism (9).
35. 如权利要求 1所述双通道熵循环发动机, 其特征在于: 所述工质闭合回路中, 参与 循环的气体的一部分为不凝气。  35. The two-channel entropy cycle engine according to claim 1, wherein: in the closed circuit of the working fluid, a part of the gas participating in the circulation is non-condensable.
36. 如权利要求 35所述双通道熵循环发动机, 其特征在于: 所述双通道熵循环发动机 还包括不凝气储罐 (70), 所述不凝气储罐 (70 ) 经控制装置与所述工质闭合回路连通。  36. The dual channel entropy cycle engine of claim 35, wherein: the dual channel entropy cycle engine further comprises a non-condensable gas storage tank (70), and the non-condensable gas storage tank (70) is controlled by the control device The working fluid is in closed loop communication.
37. 如权利要求 36所述双通道熵循环发动机, 其特征在于: 所述双通道熵循环发动机 还包括不凝气回储压缩机 (71 ), 所述不凝气回储压缩机 (71 ) 的进气口与所述工质闭合回 路连通, 所述不凝气回储压缩机 (71 ) 的气体出口与所述不凝气储罐 (70)连通。  37. The dual channel entropy cycle engine of claim 36, wherein: said dual channel entropy cycle engine further comprises a non-condensable gas return compressor (71), said non-condensable gas returning compressor (71) The air inlet is in communication with the working fluid closed circuit, and the gas outlet of the non-condensable gas returning compressor (71) is in communication with the non-condensable gas storage tank (70).
38. 如权利要求 1所述双通道熵循环发动机, 其特征在于: 在所述工质闭合回路内设三 权利 要 求 书 元催化器 (88)。 38. The dual channel entropy cycle engine of claim 1 wherein: three in the closed loop of the working fluid The claim metacatalyst (88).
39.根据权利要求 1所述双通道熵循环发动机, 其特征在于: 所述活塞式气体压缩机构 (9)的气缸中心线和所述活塞式气体做功机构(10 )的气缸中心线之间的夹角小于 180度, 所述活塞式气体压缩机构 (9 ) 的活塞和所述活塞式气体做功机构 (10 ) 的活塞分别经连杆 与同一曲轴的同一连杆轴颈连接。  39. The two-channel entropy cycle engine according to claim 1, wherein: between a cylinder center line of said piston type gas compression mechanism (9) and a cylinder center line of said piston type gas work mechanism (10) The angle of the piston is less than 180 degrees, and the piston of the piston type gas compression mechanism (9) and the piston of the piston type gas work mechanism (10) are respectively connected to the same connecting rod journal of the same crankshaft via a connecting rod.
40. 如权利要求 39所述双通道熵循环发动机, 其特征在于: 所述活塞式气体压缩机构 (9) 的气缸中心线和所述活塞式气体做功机构 (10) 的气缸中心线之间的夹角为 90度。  40. The two-channel entropy cycle engine according to claim 39, wherein: between the cylinder center line of the piston type gas compression mechanism (9) and the cylinder center line of the piston gas work mechanism (10) The angle is 90 degrees.
41. 如权利要求 1所述双通道熵循环发动机,其特征在于:所述活塞式气体压缩机构(9 ) 的活塞和所述活塞式气体做功机构 (10 ) 的活塞分别经连杆与同一曲轴上的不同连杆轴颈 连接, 两个所述连杆轴颈的相位差大于 0度小于 180度。  The dual-channel entropy cycle engine according to claim 1, wherein the piston of the piston type gas compression mechanism (9) and the piston of the piston type gas work mechanism (10) pass through a connecting rod and a same crankshaft, respectively. The different connecting rod journals are connected, and the phase difference between the two connecting rod journals is greater than 0 degrees and less than 180 degrees.
42. 如权利要求 1所述双通道熵循环发动机, 其特征在于: 所述双通道熵循环发动机还 包括低温冷源 (50), 所述低温冷源 (50 ) 用于提供低温物质, 所述低温物质用于冷却所述 活塞式气体压缩机构 (9) 中或即将进入所述活塞式气体压缩机构 (9) 的工质。  42. The dual channel entropy cycle engine of claim 1 wherein: said dual channel entropy cycle engine further comprises a cryogenic cold source (50), said cryogenic cold source (50) for providing a cryogenic material, said The cryogenic material is used to cool the working fluid in the piston gas compression mechanism (9) or about to enter the piston gas compression mechanism (9).
43. 如权利要求 1所述双通道熵循环发动机, 其特征在于: 所述双通道熵循环发动机还 包括涡轮动力机构 (14 ) 和叶轮压气机 (13 ), 所述工质导出口 (6 ) 与所述涡轮动力机构 43. The dual channel entropy cycle engine of claim 1 wherein: said dual channel entropy cycle engine further comprises a turbine power mechanism (14) and an impeller compressor (13), said working fluid outlet (6) And the turbine power mechanism
( 14) 的工质入口连通, 所述涡轮动力机构 (14) 的工质出口经附属冷却器 (211 ) 与所述 叶轮压气机 (13 ) 的工质入口连通, 所述叶轮压气机 (13 ) 的工质出口与所述工质闭合回 路连通; 所述涡轮动力机构 (14 ) 的工质出口与所述叶轮压气机 (13 ) 的工质入口之间的 通道上设附属工质导出口 (66)。 The working fluid inlet of (14) is connected, and the working fluid outlet of the turbine power mechanism (14) is connected to the working fluid inlet of the impeller compressor (13) via an auxiliary cooler (211), the impeller compressor (13) The working medium outlet is in communication with the working fluid closed circuit; the working fluid outlet of the turbine power mechanism (14) and the working fluid inlet of the impeller compressor (13) are provided with an auxiliary working fluid outlet (66).
44. 如权利要求 1所述双通道熵循环发动机, 其特征在于: 所述双通道熵循环发动机还 包括四类门气缸活塞机构 (99), 所述四类门气缸活塞机构 (99 ) 的供气 LJ (993 ) 与所述 工质闭合回路连通, 所述四类门气缸活塞机构(99)的回充口(994 )与所述工质导出口(6) 连通。  44. The dual channel entropy cycle engine of claim 1 wherein: said dual channel entropy cycle engine further comprises a four type of door cylinder piston mechanism (99), said four types of door cylinder piston mechanism (99) The gas LJ (993) is in communication with the working fluid closed circuit, and the refill port (994) of the four-type door cylinder piston mechanism (99) is in communication with the working fluid outlet (6).
45. 如权利要求 44所述双通道熵循环发动机, 其特征在于: 所述双通道熵循环发动机 还包括氧化剂源 (4), 所述氧化剂源 (4) 设为所述四类门气缸活塞机构 (99)。  45. The dual channel entropy cycle engine of claim 44, wherein: said dual channel entropy cycle engine further comprises an oxidant source (4), said oxidant source (4) being set to said four type of door cylinder piston mechanism (99).
46. 如权利要求 3所述双通道熵循环发动机, 其特征在于: 所述旁置内燃燃烧室 (31 ) 设为四类门气缸活塞机构 (99), 所述四类门气缸活塞机构 (99 ) 的供气口 (993 ) 与所述 活塞式气体做功机构 (10) 的气缸连通, 所述四类门气缸活塞机构 (99) 的回充口 (994) 与所述工质导出口 (6 ) 连通。  46. The two-channel entropy cycle engine according to claim 3, wherein: said side internal combustion chamber (31) is set as a four-type door cylinder piston mechanism (99), said four-type door cylinder piston mechanism (99) The gas supply port (993) communicates with the cylinder of the piston gas working mechanism (10), and the refill port (994) of the four types of door cylinder piston mechanism (99) and the working fluid outlet (6) ) Connected.
47. 如权利要求 12所述双通道熵循环发动机, 其特征在于: 所述双通道熵循环发动机 还包括氧化剂传感器 (51 ) 和氧化剂控制装置 (52) , 所述氧化剂传感器 (51 ) 设在所述工 质闭合回路内, 所述氧化剂传感器 (51 ) 对所述氧化剂控制装置 (52 ) 提供信号, 所述氧 化剂源 (4) 经氧化剂控制阀 (53 ) 与所述工质闭合回路连通, 所述氧化剂控制装置 (52 ) 控制所述氧化剂控制阀 (53 )。  47. The dual channel entropy cycle engine of claim 12, wherein: said dual channel entropy cycle engine further comprises an oxidant sensor (51) and an oxidant control device (52), said oxidant sensor (51) being located at In the closed circuit of the working fluid, the oxidant sensor (51) provides a signal to the oxidant control device (52), and the oxidant source (4) is connected to the working fluid closed circuit via an oxidant control valve (53). The oxidant control device (52) controls the oxidant control valve (53).
48. 如权利要求 1所述双通道熵循环发动机,其特征在于:所述活塞式气体压缩机构(9) 权利 要 求 书 设为活塞液体机构 (90), 所述活塞液体机构包括气液缸 (91) 和气液隔离结构 (92), 所 述气液隔离结构 (92) 设在所述气液缸 (91) 内。 48. The dual channel entropy cycle engine of claim 1 wherein said piston gas compression mechanism (9) The claim is set as a piston liquid mechanism (90), the piston liquid mechanism includes a gas-liquid cylinder (91) and a gas-liquid isolation structure (92), and the gas-liquid isolation structure (92) is disposed in the gas-liquid cylinder (91) ) Inside.
49. 如权利要求 1 所述双通道熵循环发动机, 其特征在于: 所述活塞式气体做功机构 (10)设为活塞液体机构(90),所述活塞液体机构包括气液缸(91)和气液隔离结构(92), 所述气液隔离结构 (92) 设在所述气液缸 (91) 内。  49. The two-channel entropy cycle engine according to claim 1, wherein: the piston gas work mechanism (10) is a piston liquid mechanism (90), and the piston liquid mechanism comprises a gas liquid cylinder (91) and gas. a liquid isolation structure (92), the gas-liquid isolation structure (92) is disposed in the gas-liquid cylinder (91).
50. 如权利要求 48或 49所述双通道熵循环发动机, 其特征在于: 所述气液缸(91) 的 气体工质对所述气液隔离结构 (92) 的压力大于所述气液缸 (91) 内的液体和所述气液隔 离结构 (92) 做往复运动时的惯性力之和。  50. The dual channel entropy cycle engine according to claim 48 or 49, wherein: the gas working fluid of the gas cylinder (91) has a pressure greater than the gas cylinder of the gas-liquid isolation structure (92) (91) The sum of the inertial forces in the liquid and the gas-liquid isolation structure (92) when reciprocating.
51. 如权利要求 1所述双通道熵循环发动机, 其特征在于: 所述内燃燃烧室 (3)排出 的物质的质量流量大于从所述工质闭合回路外导入所述内燃燃烧室(3)的物质的质量流量。  51. The two-channel entropy cycle engine according to claim 1, wherein: the mass flow rate of the substance discharged from the internal combustion combustion chamber (3) is greater than the introduction into the internal combustion combustion chamber from the closed circuit of the working fluid (3) The mass flow of the substance.
52. 如权利要求 3所述双通道熵循环发动机, 其特征在于: 流入所述活塞式气体做功机 构 (10) 的工质的质量流量大于所述旁置内燃燃烧室 (31) 排出的物质的质量流量。  52. The two-channel entropy cycle engine according to claim 3, wherein: a mass flow rate of the working fluid flowing into the piston gas working mechanism (10) is greater than a mass flow rate of the side internal combustion combustion chamber (31) Mass Flow.
53. 如权利要求 1所述双通道熵循环发动机, 其特征在于: 所述工质闭合回路的承压能 力大于 2MPa。  53. The dual channel entropy cycle engine of claim 1 wherein: said working fluid closed circuit has a pressure bearing capacity greater than 2 MPa.
54. 如权利要求 1所述双通道熵循环发动机, 其特征在于: 在所述连通通道 (1) 上设 回热器 (33), 所述活塞式气体做功机构 (10) 的工质出口与所述活塞式气体压缩机构 (9) 的工质入口之间的所述连通通道 (1) 设为所述回热器 (33) 的被冷却流体通道, 所述活塞 式气体压缩机构 (9) 的工质出口与所述活塞式气体做功机构 (10) 的工质入口之间的所述 连通通道 (1) 设为所述回热器 (33) 的被加热流体通道。  54. The two-channel entropy cycle engine according to claim 1, wherein: a regenerator (33) is disposed on the communication passage (1), and a working fluid outlet of the piston gas working mechanism (10) The communication passage (1) between the working fluid inlets of the piston type gas compression mechanism (9) is set as a cooled fluid passage of the regenerator (33), and the piston type gas compression mechanism (9) The communication passage (1) between the working fluid outlet and the working fluid inlet of the piston gas working mechanism (10) is set as the heated fluid passage of the regenerator (33).
55. 如权利要求 1所述双通道熵循环发动机, 其特征在于: 所述内燃燃烧室 (3) 以独 立腔体的形式设置在所述连通通道 (1) 内。  A two-channel entropy cycle engine according to claim 1, characterized in that said internal combustion chamber (3) is disposed in said communication passage (1) in the form of a separate cavity.
PCT/CN2012/001620 2011-12-01 2012-12-03 Dual-conduit entropy-cycle engine WO2013078775A1 (en)

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4364233A (en) * 1980-12-31 1982-12-21 Cummins Engine Company, Inc. Fluid engine
CN1243562A (en) * 1997-01-22 2000-02-02 居伊·内格尔 Method and device for recuperating ambient thermal energy for vehicle equipped with a pollution-free engine with secondary compressed air
CN2511795Y (en) * 2001-12-19 2002-09-18 周义农 Two stroke IC engine with scavenging cylinder
CN2881124Y (en) * 2005-10-31 2007-03-21 李建锋 Piston type engine
CN201013445Y (en) * 2007-03-06 2008-01-30 苗浩野 Piston four stroke engine
CN101418716A (en) * 2007-10-23 2009-04-29 赵元藩 Highly effective integration heat engine

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4364233A (en) * 1980-12-31 1982-12-21 Cummins Engine Company, Inc. Fluid engine
CN1243562A (en) * 1997-01-22 2000-02-02 居伊·内格尔 Method and device for recuperating ambient thermal energy for vehicle equipped with a pollution-free engine with secondary compressed air
CN2511795Y (en) * 2001-12-19 2002-09-18 周义农 Two stroke IC engine with scavenging cylinder
CN2881124Y (en) * 2005-10-31 2007-03-21 李建锋 Piston type engine
CN201013445Y (en) * 2007-03-06 2008-01-30 苗浩野 Piston four stroke engine
CN101418716A (en) * 2007-10-23 2009-04-29 赵元藩 Highly effective integration heat engine

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