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WO2012024898A1 - Small temperature rise low-entropy mixed-fuel engine - Google Patents

Small temperature rise low-entropy mixed-fuel engine Download PDF

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Publication number
WO2012024898A1
WO2012024898A1 PCT/CN2011/001430 CN2011001430W WO2012024898A1 WO 2012024898 A1 WO2012024898 A1 WO 2012024898A1 CN 2011001430 W CN2011001430 W CN 2011001430W WO 2012024898 A1 WO2012024898 A1 WO 2012024898A1
Authority
WO
WIPO (PCT)
Prior art keywords
combustion chamber
temperature
combustion
source
expansion agent
Prior art date
Application number
PCT/CN2011/001430
Other languages
French (fr)
Chinese (zh)
Inventor
靳北彪
Original Assignee
Jin Beibiao
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from CN2011100359985A external-priority patent/CN102086823A/en
Application filed by Jin Beibiao filed Critical Jin Beibiao
Publication of WO2012024898A1 publication Critical patent/WO2012024898A1/en

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02CGAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C3/00Gas-turbine plants characterised by the use of combustion products as the working fluid
    • F02C3/20Gas-turbine plants characterised by the use of combustion products as the working fluid using a special fuel, oxidant, or dilution fluid to generate the combustion products
    • F02C3/30Adding water, steam or other fluids for influencing combustion, e.g. to obtain cleaner exhaust gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02CGAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C3/00Gas-turbine plants characterised by the use of combustion products as the working fluid
    • F02C3/20Gas-turbine plants characterised by the use of combustion products as the working fluid using a special fuel, oxidant, or dilution fluid to generate the combustion products
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M25/00Engine-pertinent apparatus for adding non-fuel substances or small quantities of secondary fuel to combustion-air, main fuel or fuel-air mixture
    • F02M25/022Adding fuel and water emulsion, water or steam
    • F02M25/025Adding water
    • F02M25/03Adding water into the cylinder or the pre-combustion chamber
    • 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

  • This invention relates to the field of thermal energy and power, and more particularly to an engine.
  • Kelvin's way of saying is "it is impossible to extract heat from a single heat source, so that it becomes completely useful without causing other changes.”
  • Sri Lanka's way of saying is “it is impossible to transfer heat from a low temperature object to a high temperature object without any other influence.”
  • the Power of Fire Carnot proposed that the heat engine must work between two heat sources, extract heat from the high-temperature heat source, and transfer a part of the heat absorbed to the low-temperature heat source. Mechanical work.
  • the understanding of Carnot's theorem is: the heat extracted from the high-temperature heat source during the isothermal expansion of the working medium at the high-temperature heat source temperature is regarded as the heat of "absorbing heat from the high-temperature heat source" in the Carnot's theorem; The amount of heat emitted by the environment is considered to be the part of the heat in the Carnot's theorem "transmitting a part of the absorbed heat to the low-temperature heat source”.
  • the high-temperature heat source is artificially manufactured, and the low-temperature heat source is self-manufactured according to the state of the working medium (temperature and pressure) under the high-temperature heat source and the thermodynamic properties of the working medium.
  • the state of the working medium temperature and pressure
  • the expansion agent absorbs heat at a high temperature heat source temperature to increase or vaporize (including a criticalization process and overheating).
  • the pressure parameter of the newly formed working medium (the so-called newly formed working medium including the original working medium and the expanding agent) reaches a state in which the temperature of the working medium is lower than even when the expansion is completed Substantially lower than the ambient temperature.
  • the work output by such a cyclic process must be close to, equal to or exceed the heat absorbed from the high temperature heat source. In other words, the efficiency must be close to, equal to or exceed 100%, if the temperature of the working fluid of the expansion work is lower than At ambient temperature, it is impossible to dissipate heat from a low temperature heat source but can absorb heat from a low temperature heat source or be exported.
  • the derived working fluid can be thrown into other heat sources at any temperature (including high temperature heat sources).
  • the high-temperature heat source of the internal combustion engine is the working fluid after the combustion of the fuel
  • the low-temperature heat source also referred to as the cold source
  • the state of the working fluid after the expansion work is the fuel. Determined by the state of the working fluid after combustion.
  • the combustion process is controlled so that the state parameter of the working fluid after the combustion of the fuel reaches a certain value, the temperature of the working fluid after the expansion work can be made lower or even lower than the ambient temperature, such a cycle.
  • the work output by the process must be close to, equal to or exceed the heat absorbed from the high temperature heat source. In other words, the efficiency must be close to, equal to or exceed 100%.
  • the temperature of the working fluid for expansion is lower than the ambient temperature, It is impossible to dissipate heat from a low temperature heat source but can absorb heat from a low temperature heat source or be derived, and the derived working fluid can be thrown into other heat sources at any temperature (including high temperature heat sources).
  • these two examples all create conditions that cannot be explained by existing thermodynamic theories and theorems. Therefore, the current understanding of the Carnot's theorem is misunderstood, so what is the so-called "heat from the high-temperature heat source” refers to which part of the heat, and the so-called “transfer a part of the absorbed heat to the low-temperature heat source" Which part of the heat is the part of the heat?
  • the heat of "absorbing heat from a high-temperature heat source” is the heat absorbed by the working medium from the high-temperature heat source during the process of heating the working medium from the temperature of the low-temperature heat source to the temperature of the high-temperature heat source (including the temperature of the high-temperature heat source)
  • the heat absorbed by the lower working medium from the high temperature heat source) shown as Q in Figure 11
  • the bottom heat of the working medium refers to the absolute zero degree contained in the working medium at the low temperature heat source temperature itself).
  • the calculated heat (shown as Qc in Figure 1) consists of two parts, and the so-called “transfer a part of the heat absorbed to the low-temperature heat source” is the heat that is discharged from the working medium to the environment ( As shown by q in Figure 1) and the bottom heat of the working fluid (shown as Qc in Figure 11), it consists of two parts.
  • the working fluid can not transfer heat to the environment, as long as the working medium after the expansion work is found, such as thrown into the environment or thrown into any temperature.
  • the heat engine can be cycled.
  • the low temperature working fluid after expansion work can be thrown into the high temperature heat source of the system (as shown by the dotted line in Qc-ML in Fig. 12).
  • the working fluid cooled and condensed after expansion work can be thrown into the combustion of the internal combustion engine.
  • the exhaust gas in the air motor is thrown into the environment (in some air engines, the environment is the high-temperature heat source of the air motor), and for example, it will be absorbed from the working fluid after the expansion work.
  • the hot liquid is thrown into the high temperature heat source.
  • the heat engine can work under a heat source, and the heat engine can be cycled as long as the working fluid after the expansion work is derived.
  • the derived working fluid after expansion can be thrown into a heat source lower than its own temperature, can be thrown into the same heat source as its own temperature, can be thrown into a heat source higher than its own temperature, can be thrown into In the high-temperature heat source, it can also be thrown into a heat source higher than the temperature of the high-temperature heat source; not only that, if the working medium after the expansion work is only transferred to the low-temperature heat source, the heated low-temperature heat source can still be thrown into the high-temperature heat source.
  • the cooling medium for cooling the working fluid after the expansion work can be thrown into the high temperature heat source. Therefore, the necessary conditions for the operation of the heat engine are not two heat sources, but at least one heat source, at least one residual flow outlet (the so-called residual flow outlet refers to the outlet of the working fluid after the expansion work and/or the work after the expansion work)
  • the outlet of the mass heat can be connected to any other heat source (including the high temperature heat source of the system), and in the structure in which the residual stream outlet is connected to the high temperature heat source, the heat machine only needs one heat source to circulate,
  • the heat engine needs at least two heat sources, and the residual flow outlet can only be when the residual flow outlet is in communication with a heat source having a temperature higher than the residual flow outlet.
  • the inventor's heat is: heat transfer and mass transfer during the operation of the heat engine may exist, coexist or replace each other. It is completely correct to say that it is impossible to transfer heat from a low temperature object to a high temperature object without any other influence, but we can throw a low temperature object (such as a low temperature working medium) into a high temperature object (such as a high temperature working medium) through mass transfer ( That is, the process of throwing a low-temperature object into a high-temperature object) realizes the unrealizable process of "transferring heat from a low-temperature object to a high-temperature object.”
  • the conclusion that the heat transfer and mass transfer during the operation of the heat engine can exist, coexist or replace each other is the conclusion that the work of manufacturing a high-efficiency heat engine or manufacturing output equals the calorific value of the fuel or the work output is greater than the heat value of the fuel.
  • FIG. 1 , FIG. 12 and FIG. 13 are three cycle diagrams of q>
  • the condition is not two heat sources, but at least one heat source, at least one residual stream outlet (the so-called residual stream outlet refers to the outlet of the working fluid after the expansion work and/or the heat outlet of the working medium after the expansion work)
  • the residual flow outlet may be in communication with any other heat source (including a high temperature heat source of the system), and in the structure in which the residual flow outlet is in communication with the high temperature heat source, the heat engine only needs one heat source to circulate, in the residual flow
  • the heat exchanger in the structure that is not connected to the high temperature heat source needs at least two heat sources.
  • the residual stream outlet When the residual stream outlet is in communication with a heat source having a temperature higher than the residual stream outlet, the residual stream outlet can only be expanded after work.
  • the export of working fluids In his 1824 paper "The Power of Fire", Carnot proposed that "the heat engine must work between two heat sources, extract heat from the high-temperature heat source, and pass a part of the heat absorbed to the low-temperature heat source. Only in this way The discussion of obtaining mechanical work is only a special case of the inventor's claim to the second law of thermodynamics. Kano is a great scientist, but in his time the internal combustion engine was not born, and it may be because of this reason that Karno's thought was limited.
  • the low temperature heat source of the actual heat engine also called The cold source
  • the temperature of the low temperature heat source which is self-made by the expansion process can be completely lower than the ambient temperature. In other words, the output work can be completely high. The heat extracted from the high temperature heat source.
  • thermodynamic properties of the working fluid are determined by the temperature of the low temperature heat source that is self-manufactured by the expansion process.
  • Chemical energy is the source of energy for modern heat engines.
  • the inventors believe that the use of chemical energy in conventional heat engines has considerable defects, and the root cause of these defects is that the understanding of an extremely important property of chemical energy is insufficient. Deep, that is, the understanding of the properties of chemical energy that can be input energy to the working fluid in any high-energy state (high temperature and high pressure) is not deep enough.
  • the chemical energy is an attribute that can input energy to a working medium in any high-energy state (high temperature and high pressure) as a super-existence of chemical energy, and if the super-characteristics of chemical energy are fully utilized That is, the efficiency of the heat engine can be substantially improved.
  • Figure 1 4, S, S 2 and S 3 are schematic diagrams of the heat machine with different compression strengths.
  • Q h is the chemical energy of the fuel, since the work required for the compression process can be recovered through the expansion process, assuming that both the compression process and the expansion process are reversible, regardless of the pressure How high the shrinking force does not affect the efficiency of the heat engine itself, but the higher the compression strength, the higher the chemical energy is to a higher grade.
  • These higher grade chemical energy can be more in the process of work. Most of them are output in the form of work. If the state parameters are reasonable, they are increased by a considerable compression force to a relatively high grade of chemical energy.
  • the temperature of the working medium can be lowered to a level significantly lower than the standard state.
  • the rationalization of the state parameters of the formed high-temperature and high-pressure working medium means that the relationship between the pressure and the temperature of the working fluid after combustion can be made to bring the temperature of the working medium to work close to, equal to, or lower than the temperature by the introduction of the expanding agent or other means. Or substantially lower than the standard state temperature, the so-called other way is to greatly increase the strength of the engine compression stroke without the expansion agent, so that the pressure and temperature at the end of the compression stroke are at a relatively high state It can heat and heat the working fluid, as shown in the high-end position in Figure 18.
  • the working fluid For external combustion engines, first, the working fluid must absorb heat at a relatively high pressure and temperature (using environment or other low-grade heat source to make the working medium at a relatively high temperature and pressure, then use chemical energy to heat the working medium. Second, the state parameters of the working fluid after the endotherm must be rationalized; Third, the reasonable selection of the working medium (the so-called reasonable choice of working medium refers to the selection of the phase change heat is small and the liquid is liquefied when the expansion work to the set level) quality).
  • Figure 18 is a detailed calculation data of heating and warming up the working fluid by fuel combustion under the premise of different compression strength of the working medium.
  • the vertical axis is pressure
  • the horizontal axis is temperature
  • 0-H is adiabatic compression.
  • the curves, A, - E, A 2 - E 2 , A 3 - E 3 , ..., A - E n represent the straight line of heating and heating of the working medium by fuel combustion under different compression forces, and with the value of n
  • the compression strength continues to increase, as can be seen from Figure 18, the slope of the combustion temperature rise line gradually increases with the increase of compression strength; it is not difficult to reason, from the state point E, E 2 in Figure 18 E 3 , ..., After starting the adiabatic expansion work, as the value of n increases, the temperature of the working medium is lower.
  • FIG. 18 also illustrates that: the temperature excess in the conventional internal combustion engine is very serious, that is, in the conventional internal combustion engine, the temperature is far after the combustion compared with the pressure. Exceeding the necessary values, it can be said that the pressure is much lower than the necessary value compared with the temperature.
  • the corpse is the gas working fluid pressure, the temperature of the gas working fluid, the relationship of the adiabatic compression index) is greatly improved, or if we can find a new heating method to make the pressure and temperature of the working fluid of the external combustion engine according to P -
  • the relationship between C and ⁇ is greatly improved, and a highly efficient external combustion engine can be manufactured.
  • the external combustion cycle is a cyclical way to create a higher efficiency than the internal combustion cycle.
  • the small temperature rise and low entropy co-firing engine disclosed by the invention utilizes the respective advantages of the external combustion cycle and the internal combustion cycle, so that the efficiency of the engine is substantially improved.
  • the highest energy state of the gas working fluid in the engine cylinder ie, the gas working state when the combustion is just finished, at this time the gas working fluid Temperature and pressure are at the highest state throughout the cycle
  • the process consists of: the first process is the adiabatic compression of the gas by the piston (actually approximately adiabatic compression).
  • the pressure, ⁇ is the gas working temperature, the adiabatic compression index, and the adiabatic compression index of the air is 1.
  • the second process is to inject fuel into the gas.
  • the heat generated by the combustion chemical reaction is in the state of near isovolumic heating.
  • the warming pressurization is carried out (see the line shown by A - E in Fig. 17), and Fig. 17 is the pressure-temperature relationship diagram in which the vertical axis is the pressure coordinate and the horizontal axis is the temperature coordinate.)
  • the two processes work together.
  • the quality is at the beginning of the work, and the power stroke is performed according to the adiabatic expansion process (actually approximately adiabatic expansion) (see the curve shown by EF in Fig. 17).
  • the highest energy state of the working medium is achieved by two different processes, and the highest energy state of the working medium reaches the work.
  • the state at the end of the stroke is achieved by an adiabatic expansion process.
  • Figure 15 is a schematic diagram showing the relationship between the pressure and temperature of the gas working fluid after combustion in accordance with the temperature and pressure of the adiabatic compression process.
  • the three points of point eight, point 8, and point C respectively indicate the state when the compression stroke is completed, and the point ⁇ indicates The state reached after the combustion of the chemical reaction is started from the point ,
  • the point BB represents the state reached after the combustion of the chemical reaction from the point B
  • the point CC represents the state reached after the combustion of the chemical reaction from the point C
  • the point 0 is the starting point of the compression stroke.
  • Figure 16 is a schematic diagram showing the pressure value of the gas working fluid after combustion is greater than the pressure value determined by the relationship between the pressure and temperature of the adiabatic compression process.
  • FIG. 1 7 is the intensity of different warming pressurization process and increasing the compression stroke when the compression stroke is completed, so that the temperature of the compressed gas reaches the environmental temperature limit or the material temperature limit and the temperature before or after combustion is constant or not obvious.
  • A-CC, A-BB, A-AA indicate different temperature rise and pressure rise process
  • point D indicates that the temperature of the compressed gas reaches the environmental protection temperature
  • D-DD indicates the process of constant or no significant change in pressure before and after combustion
  • point DDD, point CCG, point BBB, point AAA, and point 0 Represents the end points of the expansion work for different processes.
  • Fig. 15, Fig. 16, and Fig. 17, if we can find a way to make the pressure temperature state point of the burned working medium be at the pressure temperature curve 0-H of the adiabatic compression process or at adiabatic pressure.
  • the pressure temperature curve of the shrinking process is 0-H to the left, and the working temperature after the expansion work can reach a temperature equal to 0, a temperature lower than 0, or a temperature lower than 0, which will The efficiency of the engine is greatly improved, and an engine whose output work is close to the fuel heat value, equal to the fuel heat value, or greater than the fuel heat value can be manufactured. If the pressure temperature state point of the burned working fluid is on the right side of the pressure temperature curve 0-H of the adiabatic compression process, although the engine whose output work is equal to the fuel heat value or greater than the fuel heat value cannot be produced, by burning The pressure temperature state point of the working fluid is as close as possible to the 0-H curve to achieve an increase in efficiency.
  • the determined pressure value that is, the corpse value, thus ensuring the pressure temperature state of the working medium after combustion The point is on curve 0-H or on the left side of curve 0-H to achieve higher efficiency and better environmental friendliness.
  • the small temperature rise and low entropy co-firing engine disclosed in the present invention discloses the following technical solution: when the compression stroke/process is completed, a certain proportion or all of the heat released by the combustion chemical reaction is introduced into the combustion.
  • the expansion agent absorption of the chamber increases the number of moles of gas working medium to be started, for example, the combustion absorbed by the expansion agent introduced into the combustion chamber as shown by A-GC, A-BB, A-AA in Fig. 17.
  • the amount of heat released by the chemical reaction increases in order of A-AA, A-BB, and A-CC; in order to further improve efficiency and environmental protection, the small temperature rise and low entropy co-combustion engine disclosed by the present invention also discloses another type.
  • the heat released by the chemical reaction of the fuel combustion is absorbed by the expansion agent introduced into the combustion chamber to increase the number of moles of the gaseous working medium to be started to work.
  • the temperature and pressure in the combustion chamber will increase, but the pressure increase is composed of two factors: The first factor is that the working medium absorbs a part of the heat released by the combustion chemical reaction, causing the temperature of the working medium to rise.
  • the constant temperature rise is considered), and then the pressure rises in a linear relationship; the second factor is that the expansion agent absorbs a part of the heat released by the combustion chemical reaction, causing the gas phase number in the combustion chamber to increase, resulting in an increase in pressure, which is not an increase in pressure. Due to the temperature rise, even if the temperature drops, the temperature is constant, or the temperature increases, the pressure will increase significantly during this process.
  • the state created by the first factor is the state of over-temperature, and the state created by the second factor is the state of negative temperature excess.
  • the small temperature rising low entropy co-firing engine disclosed by the invention can not only absorb the total heat released by the fuel combustion, but also absorb a part of the compressed gas.
  • the heat of the working fluid in this case, the temperature of the working fluid to be started to work is lower than the working temperature at the end of the compression stroke/process.
  • Figure 19 is a comparison diagram of the cycle of the cycle of the small temperature rise and low entropy co-firing engine disclosed in the present invention and the cycle of the conventional internal combustion engine.
  • the curve shown by abcda is a diagram of the cycle of the conventional internal combustion engine, in which abmsa
  • the curve shown is that the pressure of the small temperature rise and low entropy co-firing engine disclosed in the present invention when the compression stroke is completed is slightly larger than the pressure at the end of the compression of the conventional internal combustion engine, but all or nearly all of the heat released by the combustion chemical reaction has been
  • the expansion agent introduced into the combustion chamber absorbs the number of moles of gas working medium that is about to start work, and forms a cycle diagram of a state in which the temperature before or after combustion is constant or does not change significantly, and the pressure is greatly increased, in the figure, a - the curve shown by znta is the total or near-heat of the temperature of the small temperature rise and low entropy co-firing engine disclosed in the present
  • FIG. 20 is a graph showing the relationship between the temperature T and the pressure P of the gas working medium, and the curve indicated by 0-A-H is a gas working adiabatic relationship curve passing through the zero point of the state parameter of 298 K and 0.1 MPa; Point B is the actual state point of the gas working fluid.
  • the curve shown by EBD is the adiabatic relationship curve passing through point B.
  • the pressures at point A and point B are the same;
  • the curve shown by F-G is through 2800K and 10MPa (that is, the current internal combustion engine is about to The adiabatic relationship curve of the working point of the gaseous working fluid that starts work.
  • the so-called adiabatic relationship includes the following three cases: 1.
  • the state parameter of the gaseous working fluid ie, the temperature and pressure of the working medium
  • the state parameter of the gaseous working fluid is on the adiabatic relationship curve of the working fluid, that is, the state parameter of the gaseous working fluid.
  • the point is on the curve shown by 0-AH in Figure 20; 2.
  • the state parameter of the gas working fluid ie the temperature and pressure of the working medium
  • the state parameter of the gas working fluid (ie, the temperature and pressure of the working fluid) is on the right side of the adiabatic relationship curve of the working fluid, that is, the state parameter of the gas working fluid.
  • the point is on the right side of the curve shown by 0-AH in Fig. 20, but the temperature of the gas working fluid is not higher than the temperature of the gas working fluid calculated by the adiabatic relationship plus the sum of 1000K, the sum of 950K, and 900K.
  • the temperature difference between point A and point B should be less than 1 000 ⁇ , 900 ⁇ , 850 ⁇ , 800 ⁇ , 750 ⁇ , 700 ⁇ , 650 ⁇ , 600 ⁇ , 550 ⁇ , 500 ⁇ , 450 ⁇ , 400 ⁇ , 350 ⁇ , 300 ⁇ , 250 ⁇ , 200 ⁇ , 1 90 ⁇ , 180 ⁇ , 1 70 ⁇ , 1 60 ⁇ , 150 ⁇ , 140 ⁇ , 130 ⁇ , 1 20 ⁇ , 1 10 ⁇ , 100 ⁇ , 90 ⁇ , 80 ⁇ , 70 ⁇ , 60 ⁇ , 50 ⁇ , 40 ⁇ , 30 ⁇ or small At 20 baht.
  • the so-called adiabatic relationship may be any one of the above three cases, that is, the state parameter of the gas working medium to be started working (ie, the temperature and pressure of the gas working medium) is as shown in FIG. 20 .
  • the adiabatic process curve shown through the defect is in the left region of the EB-D.
  • the so-called gaseous working fluid which is about to start work refers to a gaseous working fluid when both the combustion reaction and the expansion agent introduction process are completed.
  • an engine system i.e., a thermodynamic system
  • the state parameters of the gaseous working medium i.e., the temperature and pressure of the gaseous working medium
  • the state (i.e., temperature, pressure, and mass) of the gaseous working medium charged in the combustion chamber is adjusted, the amount of fuel introduced into the combustion chamber is adjusted, and the amount of the expanding agent introduced into the system is caused to start work.
  • the temperature and pressure of the gaseous working fluid are in a class of adiabatic relationships.
  • the gas working medium is greatly pressurized (for example, multi-stage compression).
  • a swelling agent into the combustion chamber, the temperature and pressure of the gaseous working fluid to be started to work are in an adiabatic relationship.
  • the present invention proposes the following scheme:
  • a small temperature rise low entropy co-firing engine includes a combustion chamber, a source of expansion agent and a fuel source, the fuel source being in communication with the combustion chamber via a fuel introduction control mechanism, and the source of the expansion agent is introduced into the control machine via an expansion agent Constructed in communication with the combustion chamber, the fuel introduction control mechanism and the expansion agent introduction control mechanism are controlled by a combustion control device; the combustion chamber is set as a piston engine combustion chamber, and a pressure of the piston engine combustion chamber is The capacity is greater than or equal to 4 MPa, or the combustion chamber is set to be a turbine combustion chamber, and the pressure capacity of the turbine combustion chamber is greater than or equal to 2 MPa.
  • An expansion agent heat absorption heat exchanger is disposed between the combustion chamber and the expansion agent source to cause the expansion agent in the expansion agent source to absorb heat in the expansion agent heat absorption heat exchanger.
  • the heat source of the expansion agent heat absorption heat exchanger is set as the residual heat of the small temperature rise low entropy co-firing engine.
  • the expansion agent in the expansion agent source enters the combustion chamber after the endothermic heat in the expansion agent heat absorption heat exchanger reaches a critical state, a supercritical state, or an ultra-supercritical state.
  • the small temperature rise low entropy co-firing engine further includes an oxidant source and a gas communication passage, the gas communication passage communicates with an intake passage and an exhaust passage of the combustion chamber, and an exhaust gas discharge port is disposed on the exhaust passage, Providing an exhaust gas discharge control valve at the exhaust gas discharge outlet, wherein the oxidant source is connected to the combustion chamber via the oxidant introduction control mechanism or directly through the oxidant introduction control mechanism and the combustion
  • the chamber is connected to communicate, and the oxidant introduction control means, the fuel introduction control means, and the expansion agent introduction control means are controlled by a combustion control means.
  • a gas-absorbing low-grade heat source heater is disposed on the gas communication passage.
  • a gas exothermic ambient cooler is provided on the gas communication passage and/or on the intake passage and/or on the exhaust passage.
  • a gas-liquid separator is provided at an exhaust passage of the combustion chamber, the expansion agent source is a liquid outlet of the gas-liquid separator, and a liquid in the gas-liquid separator is used as the expansion agent.
  • the expansion agent in the source of the expansion agent is set as a gas liquefied material.
  • the fuel in the fuel source is set to ethanol
  • the expansion agent in the expansion agent source is set to water
  • the fuel source and the expansion agent source are set to be the same aqueous ethanol storage tank.
  • the combustion chamber is configured as an adiabatic combustion chamber.
  • a method for improving the efficiency and environmental protection of the small temperature rise and low entropy co-firing engine adjusting a compression ratio of the engine in a structure in which the combustion chamber is set as the combustion chamber of the piston engine, so that the compression stroke is completed before combustion
  • the temperature of the compressed gas is in the range of plus or minus 200K of 1800K, and the flow rate of the compressor and the power turbine is adjusted in the structure in which the combustion chamber is set to the turbine combustion chamber to burn the turbine.
  • the temperature of the pre-combustion gas is in the range of plus or minus 200 K of 1800 K; adjusting the amount of the expansion agent introduced into the expansion agent source in the combustion chamber and the amount of fuel introduced into the combustion source in the combustion chamber so that All or nearly all of the heat generated by the combustion of the fuel introduced into the fuel source of the combustion chamber is absorbed in the combustion chamber by the expansion agent introduced into the expansion agent source in the combustion chamber; adjusting the fuel in the The maximum gas temperature in the combustion chamber after combustion in the combustion chamber is below the harmful compound NOx formation temperature to improve the environmental friendliness of the engine.
  • a method for improving the efficiency and environmental friendliness of the small temperature rise and low entropy co-firing engine adjusting an amount of expansion agent introduced into the expansion agent source in the combustion chamber and fuel introduced into the fuel source in the combustion chamber An amount such that all or nearly all of the heat generated by the combustion of the fuel in the fuel source introduced into the combustion chamber is absorbed in the combustion chamber by the expansion agent introduced into the expansion agent source in the combustion chamber;
  • the temperature in the combustion chamber is substantially maintained at a constant pressure increase before and after combustion of the combustion chamber to increase the efficiency of the engine.
  • a method for improving the efficiency and environmental protection of the small temperature rise and low entropy co-firing engine adjusting a compression ratio of the engine in a structure in which the combustion chamber is set as the combustion chamber of the piston engine, so that the compression stroke is completed before combustion
  • the temperature of the compressed gas is 1000 K or more
  • the volume flow ratio of the compressor and the power turbine is adjusted in the structure in which the combustion chamber is set to the turbine combustion chamber, so that the temperature of the gas before combustion in the combustion chamber of the turbine is 1000 K or more.
  • a method for improving the efficiency and environmental friendliness of the small temperature rise and low entropy co-firing engine adjusting an amount of expansion agent introduced into the expansion agent source in the combustion chamber and fuel introduced into the fuel source in the combustion chamber.
  • the amount of 5% or more of the heat generated by the combustion of the fuel in the fuel source introduced into the combustion chamber is absorbed in the combustion chamber by the expansion agent introduced into the expansion agent source in the combustion chamber.
  • a method for improving the efficiency and environmental protection of the small temperature rise and low entropy co-combustion engine adjusting the temperature of the gas working medium to be started to work below 2000K, adjusting the pressure of the gas working medium to be started to work to 15 Pa Above, the temperature and pressure of the gaseous working fluid that is about to start work are in accordance with the adiabatic relationship.
  • the pressure capacity of the piston engine combustion chamber is greater than or equal to 4 MPa, 4. 5 MPa, 5 MPa, 5. 5 MPa, 6 MPa, 6 5WPa, 7MPa, 7. 5MPa, 8MPa, 8. 5MPa, 9MPa, 9. 5MPa, 10MPa, 10.
  • the pressure capacity of the turbine combustion chamber is greater than or equal to 2 MPa, 2.5 MPa, 3 MPa, 3.5 MPa, 4 MPa, 4.5 MPa, 5 MPa, 5.5 MPa, 6 MPa, 6.5 Pa 7 MPa, 7.5 MPa, 8 MPa, 8.5 MPa, 9MPa, 9.5MPa, 10MPa, 10.5MPa, 11
  • the amount of the expansion agent introduced into the expansion agent source in the combustion chamber and the amount of fuel introduced into the combustion source in the combustion chamber are adjusted to cause fuel introduced into the fuel source of the combustion chamber 6% or more, 7% or more, 8% or more, 9% or more, 10% or more, 11% or more, 12% or more, 13% or more, 14% or more, 15% or more, 16% or more of the heat generated by combustion, 17% or more, 18% or more, 19% or more, 20% or more, 21% or more, 22% or more, 23% or more, 24% or more, 25% or more, 30% or more, 35% or more, 40% or more, 45% Above, 50% or more, 55% or more, 60% or more, 65% or more, 70% or more, 75% or more, 80% or more, 85% or more, 90% or more, 95% or more, or 100% in the burning
  • the cooking chamber is absorbed by the expanding agent introduced into the expansion agent source in the combustion chamber.
  • the compression ratio of the engine is adjusted so that the compression stroke is completed.
  • the temperature of the compressed gas before combustion is 1000 K or more, 1300 K or more, and 1500 K or more. 1800K or more, 2000K or more, 2300K or more, 2500K or more, 2800K or more, 3000K or more, 3200K or more, or 3500K or more, adjusting the volumetric flow ratio of the compressor and the power turbine in the structure in which the combustion chamber is set to the turbine combustion chamber
  • the temperature of the gas before combustion in the turbine combustion chamber is 1000 K or more, 1300 K or more, 1500 K or more, 1800 K or more, 2000 K or more, 2300 K or more, 2500 K or more, 2800 K or more, 3000 K or more, 3200 K or more, or 3500 K or more.
  • the principle of the present invention is to increase the amount of fuel and expansion agent entering the combustion chamber by increasing the compression ratio of the engine to increase the temperature and pressure of the gas in the combustion chamber when the compression stroke or compression process is completed.
  • a certain value of the calorific value of the combustion of the fuel in the combustion chamber is absorbed by the expansion agent to form an increase in the number of moles of the working medium, thereby increasing the working medium pressure and the temperature change amount is small or constant, and replacing the combustion chamber of the conventional internal combustion engine
  • the working cycle mode for increasing the pressure of the gas working fluid is specifically: For the piston engine, the gas pressure and temperature before combustion of the combustion chamber exceed the conventional piston internal combustion engine by increasing the compression ratio of the piston internal combustion engine.
  • Gas pressure and temperature controlling the amount of fuel and expansion agent entering the combustion chamber and the temperature at which the expansion agent enters the combustion chamber so that as much of the heat released by the combustion of the fuel is absorbed by the expansion agent, greatly increasing combustion Indoor pressure, while temperature changes are small or constant; for turbines, Adjusting the volumetric flow ratio of the compressor and the turbine such that the gas pressure and temperature before combustion of the turbine combustor exceeds the gas pressure and temperature of the conventional turbine combustion chamber, controlling the amount of fuel and expansion agent entering the combustion chamber, and the expansion agent entering the The temperature at the combustion chamber causes the heat released by the combustion of as much fuel as possible to be absorbed by the expansion agent, greatly increasing the pressure in the combustion chamber, and the amount of temperature change is small or constant; thereby greatly improving the efficiency and environmental protection of the engine. Sex.
  • the main purpose of the heat released by the combustion of the fuel is to be absorbed by the expansion agent, and is not used to heat the warming gas working medium (especially the gas working medium before combustion).
  • the so-called piston engine combustion chamber may be a four-stroke piston engine combustion chamber, or a two-stroke piston engine combustion chamber, a combustion chamber of the rotor piston engine, or may be inhaled.
  • the compression stroke and the work exhaust stroke are combustion chambers of a piston engine composed of two sets of mechanisms.
  • the so-called low temperature heat source can also be referred to as a cold source, and is equivalent to a so-called cold source in some literatures.
  • the expansion agent heat absorption heat exchanger may be set as a cooler of the compressed gas in the compression process (stroke), that is, the expansion agent is used to absorb the heat of the compressed gas during the compression process, The temperature of the compressed gas is lowered.
  • the state of the working medium (temperature and pressure) under the high-temperature heat source refers to the state of the working fluid after the endothermic heat source is completed, that is, the temperature and pressure of the working medium; the so-called high-temperature heat source
  • the state may be consistent with the state of the high temperature heat source or with the state of the high temperature heat source.
  • the term "heat is absorbed by the expansion agent” means that the heat is used to heat the temperature expansion agent, the gasification expansion agent, the critical expansion agent and/or the superheat expansion agent;
  • the critically-expanded expansion agent refers to a state in which the expansion agent is in a critical state, a supercritical state, an ultra-supercritical state, or a higher temperature and pressure state.
  • the so-called "small or constant temperature change” means that all or nearly all of the heat of the fuel is absorbed by the expansion agent, and the temperature of the gas in the combustion chamber is small or constant before and after combustion, and There is almost no excess temperature (the so-called excess temperature refers to the relationship of adiabatic expansion in order to reach a certain end state, the actual temperature of the working medium is higher than the theoretically required temperature in the starting state); according to this working mode, in the present invention
  • any two of the fuel, the oxidant (for example, compressed air or compressed oxygen-containing gas) and the expansion agent may be mixed beforehand and the third Mixed
  • the combustion reaction may first occur between the oxidant and the fuel and then mixed with the expansion agent, or may occur when the three are mixed or after the three are mixed; a core combustion zone may be established in the combustion chamber, and the oxidant in the core combustion zone
  • the fuel is directly combusted and then mixed with the expansion agent between the combustion core zone and the combustion chamber wall, so that the excessive temperature flame formed by direct combustion of the fuel and the oxidant can be separated from the combustion chamber wall by the expansion agent, thereby reducing the combustion chamber wall.
  • the heat load may be directly combusted and then mixed with the expansion agent between the combustion core zone and the combustion chamber wall, so that the excessive temperature flame formed by direct combustion of the fuel and the oxidant can be separated from the combustion chamber wall by the expansion agent, thereby reducing the combustion chamber wall.
  • the so-called expansion agent of the present invention refers to a working medium which does not participate in the combustion chemical reaction and absorbs heat and adjusts the number of moles of working medium and expands work. It may be a gas, a liquid, a critical substance, a gas liquefaction, such as water vapor, Carbon dioxide, helium, nitrogen, liquid carbon dioxide, liquid helium, liquid nitrogen or liquefied air.
  • the gas liquefied matter in the present invention means a gas to be liquefied, such as liquid nitrogen, liquid carbon dioxide, liquid helium or liquefied air.
  • oxidant means an oxygen-containing gas such as liquefied air, hydrogen peroxide or an aqueous hydrogen peroxide solution in which pure oxygen or other components do not generate harmful compounds during thermal power conversion.
  • oxidant source is meant any device, system or vessel that can provide an oxidant, such as a commercial oxygen source (ie a high pressure oxygen storage tank or a liquefied oxygen tank) and oxygen supplied by an on-site oxygen system in a thermodynamic system (eg membrane separation) Oxygen system) and so on.
  • the so-called gas-absorbing low-grade heat source heater of the present invention refers to a device for heating a gas working medium by using a low-grade heat source (such as exhaust heat, exhaust heat of a cooling system, etc.) as a heat source;
  • the so-called gas heat-dissipating environment cooler means A device for cooling a gaseous working fluid by discharging heat of a gaseous working fluid into the environment;
  • a so-called combustion control device means controlling the amount of fuel, the amount of expanding agent, and/or the amount of oxidizing agent, and the fuel, the expanding agent, and the oxidizing agent.
  • the introduced phase controls the device for combustion;
  • the so-called gas-liquid separator refers to a device that separates gas and liquid.
  • the so-called introduction control mechanism of the present invention refers to a system for supplying the original working medium (fuel, expansion agent and/or oxidant) to the combustion chamber according to the requirements of the combustion conditions of the combustion chamber of the thermodynamic system, the system including the valve, the pump and/or Or sensor, etc.
  • the so-called expander heat absorbing heat exchanger in the present invention refers to an expansion agent capable of absorbing heat by using ambient heat or the small temperature rise and low entropy co-firing engine residual heat (such as exhaust heat and residual heat of the cooling system) as a heat source. Heat exchanger.
  • the so-called environmentally friendly temperature limit in the present invention refers to the highest temperature that does not produce harmful pollutants, such as not producing
  • the environmental temperature limit for raw nitrogen oxides is 1800K, etc.
  • the so-called material temperature limit refers to the maximum temperature that the material can withstand.
  • the expansion agent of the present invention can be recycled in the small temperature rise low entropy co-firing engine.
  • the so-called fuel in the present invention refers to a substance which can undergo a vigorous redox reaction with oxygen in the sense of chemical combustion, and may be a gas, a liquid or a solid, and mainly includes gasoline, diesel, natural gas, hydrogen and gas, and fluidized fuel, Liquefied fuel or powdered solid fuel, etc.
  • the so-called liquefied fuel refers to a fuel that is liquefied and is in a gaseous state at a normal temperature and a normal pressure state.
  • the small temperature rising low entropy co-firing engine disclosed by the invention can use hydrocarbon or carbon oxyhydroxide as fuel, for example, ethanol or ethanol aqueous solution, and use ethanol aqueous solution instead of original fuel and expansion agent, not only can prevent freezing, but also It is possible to replace the original fuel storage tank and the expansion agent storage tank with only one aqueous ethanol storage tank, and to change the ratio of the fuel and the expansion agent by adjusting the concentration of the aqueous ethanol solution.
  • a mixed solution of ethanol, water and hydrocarbon may be used in place of the fuel and expansion agent of the present invention, and the concentration thereof may be adjusted to meet the requirements of the small temperature rise and low entropy co-firing engine disclosed in the present invention.
  • an aqueous hydrogen peroxide solution can be used instead of the oxidizing agent and the expanding agent, and the ratio of the oxidizing agent and the expanding agent can be adjusted by adjusting the concentration of the aqueous hydrogen peroxide solution, and a peroxidation can be used.
  • the aqueous hydrogen storage tank replaces the oxidant storage tank and the expansion agent storage tank.
  • the working fluid temperature can reach several thousand degrees or even higher, and the working fluid pressure can reach several hundred atmospheres or even higher.
  • the temperature and pressure of the working fluid after the expansion work can be adjusted to expand the work to the set expansion pressure.
  • the working temperature drops to a relatively low level, such as near ambient temperature, below ambient temperature, or substantially below ambient temperature.
  • engine refers to a mechanism that uses gas to drive a turbine to work, such as a gas turbine or a jet engine; the piston engine includes a piston type internal combustion engine, a rotor piston type internal combustion engine, and the like.
  • liquid nitrogen can be introduced into the combustion chamber in liquid form, or can be introduced into the combustion chamber in a critical state, or can be introduced into the combustion chamber in the form of an ultra-high pressure gas.
  • ultra-high pressure means that the pressure of the gas is not only high.
  • the pressure of nitrogen gas is higher than the gas pressure in the combustion chamber by 2 MPa, 3 MPa, 4 MPa, 5 MPa, 6 MPa, 7 MPa, 8 MPa, 9 MPa, 10 MPa 1 1 MPa, 1 2 MPa, 13 MPa, 14 MPa, 1 5MPa, 16 6MPa, 17 7MPa, 1 8 Pa 1 9MPa or 20MPa high.
  • the small temperature rising low entropy co-combustion engine disclosed by the invention has high efficiency and good environmental protection.
  • Embodiment 1 is a schematic structural view of Embodiment 1 of the present invention.
  • Embodiment 2 is a schematic structural view of Embodiment 2 of the present invention.
  • Embodiment 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 a tenth embodiment of the present invention.
  • Figure 1 is a schematic diagram of the q>0 cycle of the present invention
  • Figure 13 is a schematic diagram of the q ⁇ 0 cycle of the present invention.
  • Figure 14 shows a schematic diagram of the operation of a heat engine with different compression forces
  • Figure 15 is a schematic view showing the relationship between the pressure and temperature of the gaseous working fluid after combustion in accordance with the temperature and pressure of the adiabatic compression process;
  • Figure 16 is a schematic view showing the pressure value of the gas working fluid after combustion is greater than the pressure value determined by the relationship between the pressure and temperature of the adiabatic compression process;
  • Figure 17 shows the pressure-temperature relationship of the vertical axis as the pressure-slope horizontal axis as the temperature coordinate;
  • Figure 18 is a schematic diagram showing the temperature-pressure relationship of the adiabatic expansion work at different points E;
  • Figure 19 is a comparison diagram of the cycle of the cycle of the small temperature rise and low entropy co-firing engine disclosed in the present invention and the cycle of the conventional internal combustion engine;
  • Figure 20 is a graph showing the relationship between the temperature T of the gas working fluid and the pressure P.
  • FIG. 1 a small temperature rise and low entropy co-firing engine as shown in FIG. 1 , comprising a combustion chamber, an expansion agent source 2 and a fuel source 3, the combustion chamber being set as a piston engine combustion chamber 101, and the piston engine combustion chamber 101
  • the pressure bearing capacity is greater than or equal to 4 MPa
  • the fuel source 3 is in communication with the combustion chamber via a fuel introduction control mechanism 30, and the expansion agent source 2 is communicated with the combustion chamber via an expansion agent introduction control mechanism 20, the fuel introduction control
  • the mechanism 30 and the expansion agent introduction control mechanism 20 are controlled by the combustion control device 3020 to realize that more than 5% of the heat generated by the combustion of the fuel in the fuel source 3 entering the combustion chamber has been introduced into the combustion chamber.
  • Absorbing agent in the expansion agent source 2 in the combustion chamber adjusting the compression ratio of the engine in the structure in which the combustion chamber is set to the piston engine combustion chamber 101 to be compressed when the compression stroke is completed
  • the pressure of the gas is greater than the gas pressure at the end of the compression stroke of the conventional piston engine, and the temperature of the gas working fluid that is about to start work is adjusted to below 2000K, and the gas working fluid that is about to start work is adjusted. 1 5MPa or more to force the gas will begin work as working fluid temperature and pressure in line with the adiabatic relation classes.
  • a compression ratio of the engine in a configuration in which the combustion chamber is configured as the piston engine combustion chamber 101 such that a pressure of a compressed gas when the compression stroke is completed is greater than or equal to 4 MPa;
  • the compression ratio of the engine is adjusted such that the compression stroke is completed, and the temperature of the compressed gas before combustion is in the range of plus or minus 200K of 1 800 K, the fuel introduction control mechanism 30 and the The expansion agent introduction control mechanism 20 is subjected to the combustion control device 3020 Controlling all or nearly all of the heat generated by combustion of the fuel within the fuel source 3 entering the combustion chamber is absorbed by the expansion agent in the expansion agent source 2 that has been introduced into the combustion chamber After the combustion of the combustion chamber, the highest temperature in the combustion chamber is below the harmful compound NOx generation temperature to improve the environmental protection of the engine;
  • the compression ratio of the engine is adjusted so that the temperature of the compressed gas before the combustion is completed is 1000 K or more.
  • the fuel introduction control mechanism 30 and the expansion agent introduction control mechanism 20 are controlled by the combustion control device 3020 to control 6% or more and 7% or more of the heat generated by combustion of the fuel in the fuel source 3 entering the combustion chamber. 8% or more, 9% or more, 10% or more, 11% or more, 12% or more, 13% or more, 14% or more, 15% or more, 16% or more, more than 1%, 18% or more, and 9% Above, 20% or more, 21% or more, 22% or more, 23% or more, 24% or more, 25% or more, 30% or more, 35% or more, 40% or more, 45% or more, 50% or more, 55% or more, 60% or more, 65% or more, 70% or more, 75% or more, 80% or more, 85% or more, 90% or more, 95% or more, or 100%, which are introduced into the combustion chamber in the combustion chamber Absorbing agent in the expander source 2 is absorbed;
  • the temperature of the compressed gas before combustion is 1300K or more, 1500K or more, 1800K or more, 2000K or more, 2300K or more, 2500K or more, 2800K or more, 3000K or more, 3200K or more, or 3500K or more. .
  • FIG. 2 a small temperature rise and low entropy co-firing engine as shown in FIG. 2, which differs from Embodiment 1 in that: an expander heat absorption heat exchanger 1 020 is provided between the combustion chamber and the expansion agent source 2, The expansion agent in the expansion agent source 2 absorbs heat in the expansion agent heat absorption heat exchanger 1020, and the combustion chamber is set as an adiabatic combustion chamber.
  • Example 3
  • the small temperature rise and low entropy co-firing engine shown in FIG. 3 is different from the embodiment 1 in that: the heat source of the expander heat absorption heat exchanger 1020 is set as the waste heat of the small temperature rise and low entropy co-firing engine. .
  • the expansion agent in the expansion agent source 2 enters the combustion chamber after the endothermic state in the expansion agent heat absorption heat exchanger 1020 reaches a critical state, a supercritical state, or an ultra-supercritical state.
  • the fuel in the fuel source 3 is set as ethanol
  • the expansion agent in the expansion agent source 2 is set as water
  • the fuel source 3 and the expansion agent source 2 are set to be the same ethanol aqueous solution tank. .
  • the small temperature rise and low entropy co-firing engine shown in FIG. 4 is different from the embodiment 1 in that: the small temperature rise and low entropy co-firing engine further includes an oxidant source 5 and a gas communication passage 9, the gas communication passage 9 an intake passage 10 and an exhaust passage 1 connected to the combustion chamber, an exhaust gas discharge port 12 is disposed on the exhaust passage 1 1 , and an exhaust gas discharge control valve 13 is disposed at the exhaust gas discharge port 12
  • the oxidant source 5 is communicated with the combustion chamber via the oxidant introduction control mechanism 16 and directly communicated with the combustion chamber via the oxidant introduction control mechanism 16.
  • the fuel introduction control mechanism 30 and the expansion agent introduction control mechanism 20 are controlled by a combustion control device 3020.
  • the small temperature rise and low entropy co-firing engine shown in Fig. 5 differs from the embodiment 4 in that a gas-absorbing low-grade heat source heater 17 is provided on the gas communication passage 9.
  • FIG. 6 a small temperature rise and low entropy co-firing engine as shown in FIG. 6, which differs from Embodiment 4 in that: on the gas communication passage and/or on the intake passage and/or on the exhaust passage Gas exothermic environment cooler.
  • a small temperature rise and low entropy co-firing engine as shown in FIG. 7 , comprising a combustion chamber, a swelling agent source 2 and a fuel source 3, which is different from Embodiment 1 in that: the combustion chamber is set as a turbine combustion chamber 102, The pressure capacity of the turbine combustion chamber 102 is greater than or equal to 2 MPa, and the flow rate of the compressor 6 and the power turbine 7 of the turbine is adjusted such that the pressure in the turbine combustion chamber 102 is greater than or equal to 2 MPa; Adjusting the volumetric flow ratio of the compressor 6 and the power turbine 7 of the turbine in the structure of the combustion chamber 102 The temperature of the gas before combustion in the turbine combustion chamber 102 is 1000 K or more.
  • 5MPa 1 1 MPa, 1 1 . 5Pa, 12MPa, 12. 5MPa, 13MPa, 13 5MPa, 14MPa, 14. 5MPa, 1 5MPa, 15.5MPa, 16 6MPa, 16. 5MPa 1 7MPa, 1 7. 5 Pa 18MPa, 18. 5MPa, 1 9MPa, 1 9.
  • the small temperature rise and low entropy co-firing engine shown in Fig. 8 differs from the embodiment 7 in that: the expander source 2 is replaced by an oxidant source 5, and the oxidant source 5 is introduced into the control unit 16 via the oxidant.
  • the turbine combustion chamber 102 is in communication.
  • the small temperature rise and low entropy co-firing engine shown in FIG. 9 is different from the embodiment 5 in that: the small temperature rise and low entropy co-firing engine further includes an oxidant source 5, a gas communication passage 9, and a gas absorption low grade.
  • a heat source heater 17 that communicates with the turbine combustion chamber 102 via an oxidant introduction control mechanism 16 that communicates with the intake passage 10 of the compressor 6 and the power turbine 7
  • the exhaust passage 1 1 is provided with an exhaust gas outlet 12, and an exhaust gas discharge valve 13 is provided at the exhaust gas discharge port 12, and the oxidant introduction control mechanism 16 and the fuel introduction
  • the control mechanism 30, the expansion agent introduction control mechanism 20, and the exhaust gas release valve 13 are controlled by the combustion control device 3020.
  • the small temperature rise and low entropy co-firing engine shown in FIG. 10 is different from the embodiment 1 in that: a gas-liquid separator 1 100 is disposed at the exhaust passage 11 of the combustion chamber, and the expander source 2 The liquid outlet of the gas-liquid separator 1 100 is used, and the liquid in the gas-liquid separator 1 100 is used as the expansion agent.

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Abstract

A small temperature rise low-entropy mixed-fuel engine includes a combustion chamber, an expansive agent source (2) and a fuel source (3). The fuel source (3) is in communication with the combustion chamber through a fuel input control mechanism (30). The expansive agent source (2) is in communication with the combustion chamber through an expansive agent input control mechanism (20). The fuel input control mechanism (30) and the expansive agent input control mechanism (20) are controlled by a combustion control device (3020). The combustion chamber is designed to be a piston engine combustion chamber (101), and the pressure bearing capability of the piston engine combustion chamber (101) is greater than or equal to 4 MPa. Alternatively, the combustion chamber is designed to be a turbine combustion chamber (102), and the pressure bearing capability of the turbine combustion chamber (102) is greater than or equal to 2 MPa. The small temperature rise low-entropy mixed-fuel engine is efficient and environmentally friendly. Also provided is a method for improving the efficiency and environmental friendliness of the small temperature rise low-entropy mixed-fuel engine.

Description

小温升低熵混燃发动机  Small temperature rise and low entropy co-firing engine
技术领域 Technical field
本发明涉及热能与动力领域, 尤其是一种发动机。  This invention relates to the field of thermal energy and power, and more particularly to an engine.
背景技术 Background technique
为提高传统内燃机 (包括活塞式内燃机和内燃式轮机) 的效率, 已有不少 方案提出向燃烧室喷射膨胀剂。但是没有任何方案明确向燃烧室内喷射膨胀剂 的量以及喷射前燃烧室内的压力状态, 然而向燃烧室喷射膨胀剂的量和燃烧前 燃烧室内的压力和温度状态是影响向内燃机燃烧室喷射膨胀剂方案中内燃机 的效率的最重要的因素之一。 因此, 需要明确向燃烧室喷射膨胀剂的量和内燃 机压縮过程完了时气体的状态参数, 以使向燃烧室喷射膨胀剂并发生燃烧后的 工质状态参数更加合理, 以提高发动机的效率。  In order to improve the efficiency of conventional internal combustion engines (including piston internal combustion engines and internal combustion engines), many proposals have been made to inject expansion agents into the combustion chamber. However, there is no solution to explicitly inject the amount of expansion agent into the combustion chamber and the pressure state in the combustion chamber before injection. However, the amount of expansion agent injected into the combustion chamber and the pressure and temperature state in the combustion chamber before combustion affect the injection of the expansion agent into the combustion chamber of the internal combustion engine. One of the most important factors in the efficiency of an internal combustion engine in a solution. Therefore, it is necessary to clarify the amount of the expansion agent to be injected into the combustion chamber and the state parameter of the gas when the internal combustion engine is compressed, so that the combustion medium is injected into the combustion chamber and the combustion state parameter is more reasonable to improve the efficiency of the engine.
发明内容 Summary of the invention
热力学第二定律具有代表性的两种阐述方式是: 一、开尔文的阐述方式是 "不可能从单一热源吸取热量,使之完全变为有用功而不引起其他变化。";二、 克劳修斯的阐述方式是"不可能把热量从低温物体传到高温物体而不产生其他 影响"。 卡诺在其 1824年发表的 《论火的动力》论文中提出: 热机必须工作在 两个热源之间, 从高温热源吸取热量, 又把所吸取热量的一部分传递给低温热 源,只有这样才能获得机械功。而且卡诺根据这一结论提出了著名的卡诺定理, 即 ;7 = 1 - Γ2 /7, (其中, //为循环效率, 7;为高温热源的温度, Γ2为低温热源的 温度), 卡诺定理是目前热机理论中具有指导性意义的定理。 目前人们对卡诺 定理的理解是:将工质在高温热源温度下等温膨胀过程中从高温热源中吸取的 热量视为卡诺定理中的 "从高温热源吸取热量"的热量; 把工质向环境排出的 热量视为卡诺定理中的 "把所吸取热量的一部分传递给低温热源"的那一部分 热量。 然而, 在实际热机循环中, 高温热源都是人为制造的, 而低温热源都是 根据高温热源下工质的状态(温度和压力) 以及工质的热力学性质, 膨胀过程 自行制造的。 例如, 在外燃机中, 如果向高温热源温度下的工质内注入膨胀剂 并使膨胀剂在高温热源温度下吸收热量升压或发生气化(含临界化过程和过热 过程)升压, 而且使新形成的工质(所谓新形成的工质包括原来的工质和膨胀 剂)的压力参数达到这样一种状态: 即膨胀作功终了时工质的温度低于甚至大 幅度低于环境温度。 这样一个循环过程所输出的功一定会接近、 等于或超过从 高温热源中吸收的热量, 换句话说, 其效率一定会接近、 等于或超过 100%, 如 果膨胀作功的工质的温度低于环境温度, 就不可能向低温热源排热但是可以从 低温热源吸热或被导出, 被导出的工质可以被抛入任何温度的其他热源(包括 高温热源)。 再例如在内燃机中, 内燃机的高温热源是燃料燃烧后的工质, 低 温热源(也可称为冷源)是膨胀作功后的工质, 而膨胀作功后的工质的状态是 由燃料燃烧后的工质的状态所决定的。 在这种情况下, 如果控制燃烧过程使燃 料燃烧后的工质的状态参数达到一定的值,就可以使膨胀作功后的工质的温度 低于甚至大幅度低于环境温度, 这样一个循环过程所输出的功一定会接近、 等 于或超过从高温热源中吸收的热量, 换句话说, 其效率一定会接近、 等于或超 过 100%,如果膨胀作功的工质的温度低于环境温度,就不可能向低温热源排热 但是可以从低温热源吸热或被导出,被导出的工质可以被抛入任何温度的其他 热源 (包括高温热源)。 这两个例子从表面上看, 都造成了用现有的热力学理 论和定理无法解释的状况。 因此, 目前人们对卡诺定理的理解是存在误区的, 那么所谓的 "从高温热源吸取热量"的热量究竟是指哪一部分热量, 以及所谓 的 "把所吸取热量的一部分传递给低温热源"的那一部分热量究竟是指哪一部 分热量。 本发明人认为 "从高温热源吸取热量"的热量是由将工质从低温热源 的温度被高温热源加热到高温热源的温度的过程中工质从高温热源中吸取的 热量(含在高温热源温度下工质从高温热源吸取的热量)(如图 1 1 中的 Q所示) 和工质的底热(所谓工质的底热是指工质处于低温热源温度下本身所包含的从 绝对零度算起的热量) (如图 1 1 中的 Qc所示) 两部分构成的, 而所谓的 "把 所吸取热量的一部分传递给低温热源"的那一部分热量是由工质向环境排出的 热量 (如图 1 1 中的 q所示) 和工质的底热 (如图 1 1 中的 Qc所示) 两部分构 成的。 换句话说, 即便是膨胀作功后的工质温度低于环境温度, 工质不能向环 境传热, 只要将膨胀作功后的工质找到去向, 如抛入环境中或抛入任何温度的 其他热源 (包括高温热源) 中, 热机就可循环工作。 不仅如此, 在某些特定条 件下,可以将膨胀作功后的低温工质抛入系统的高温热源中(如图 12中 Qc-M-L 所示虚线方向), 例如膨胀作功后降温冷凝的工质可以抛入内燃机的燃烧后的 内或锅炉蒸气发生器内, 例如将气动发动机中的乏气抛入环境中 (在某些气动 发动机中环境就是气动发动机的高温热源), 再例如将从膨胀作功后的工质吸 收热量的液体抛入高温热源中。 由此可以得出这样的结论: 热机可以工作在一 个热源之下, 只要将膨胀作功后的工质导出, 热机就可以循环工作。 被导出的 膨胀作功后的工质可以被抛入比自身温度低的热源中, 可以被抛入与自身温度 相同的热源中, 可以被抛入比自身温度高的热源中, 可以被抛入高温热源中, 也可以被抛入比高温热源温度更高的热源中; 不仅如此, 膨胀作功后的工质如 果只对外传热传给低温热源, 受热的低温热源仍可以被抛入高温热源中, 例如 可以将用于冷却膨胀作功后的工质的冷却介质抛入高温热源中。 因此, 热机工 作的必要条件并不是两个热源, 而是至少一个热源, 至少一个残留流出口 (所 谓的残留流出口是指膨胀作功后的工质的出口和 /或膨胀作功后的工质的热量 的出口), 所述残留流出口可以与任何其他热源连通 (包括系统的高温热源), 在所述残留流出口与高温热源连通的结构中热机就只需要一个热源即可循环 工作,在所述残留流出口不与高温热源连通的结构中热机就需要至少有两个热 源, 当所述残留流出口与温度高于所述残留流出口的热源连通时所述残留流出 口只能是膨胀作功后的工质的出口。 本发明人热为: 热机工作过程中的热量传 递和质量传递可以单一存在、 共同存在或相互取代。 不可能把热量从低温物体 传到高温物体而不产生其他影响的说法是完全正确的,但是我们可以把低温物 体 (例如低温工质) 抛入高温物体 (例如高温工质), 通过质量传递 (即把低 温物体抛入高温物体的过程) 实现 "把热量从低温物体传到高温物体"的这一 不可实现过程。 热机工作过程中的热量传递和质量传递可以单一存在、 共同存 在或相互取代的这一结论为制造高效热机或制造输出的功等于燃料的热值或 制造输出的功大于燃料的热值的热机指明了方向。图 1 1、图 12和图 13所示分 别为 q〉0、 q=0、 q<0的三种循环示意图。 Two representative ways of the second law of thermodynamics are: 1. Kelvin's way of saying is "it is impossible to extract heat from a single heat source, so that it becomes completely useful without causing other changes." Sri Lanka's way of saying is "it is impossible to transfer heat from a low temperature object to a high temperature object without any other influence." In his 1824 paper entitled "The Power of Fire", Carnot proposed that the heat engine must work between two heat sources, extract heat from the high-temperature heat source, and transfer a part of the heat absorbed to the low-temperature heat source. Mechanical work. According to this conclusion, Kano proposed the famous Kano theorem, namely, 7 = 1 - Γ 2 /7, (where, // is the cycle efficiency, 7; is the temperature of the high temperature heat source, and Γ 2 is the temperature of the low temperature heat source. ), Carnot's theorem is a theorem with guiding significance in current heat engine theory. At present, the understanding of Carnot's theorem is: the heat extracted from the high-temperature heat source during the isothermal expansion of the working medium at the high-temperature heat source temperature is regarded as the heat of "absorbing heat from the high-temperature heat source" in the Carnot's theorem; The amount of heat emitted by the environment is considered to be the part of the heat in the Carnot's theorem "transmitting a part of the absorbed heat to the low-temperature heat source". However, in the actual heat engine cycle, the high-temperature heat source is artificially manufactured, and the low-temperature heat source is self-manufactured according to the state of the working medium (temperature and pressure) under the high-temperature heat source and the thermodynamic properties of the working medium. For example, in an external combustion engine, if a swelling agent is injected into a working fluid at a high temperature heat source temperature and the expansion agent absorbs heat at a high temperature heat source temperature to increase or vaporize (including a criticalization process and overheating). Process) boosting, and the pressure parameter of the newly formed working medium (the so-called newly formed working medium including the original working medium and the expanding agent) reaches a state in which the temperature of the working medium is lower than even when the expansion is completed Substantially lower than the ambient temperature. The work output by such a cyclic process must be close to, equal to or exceed the heat absorbed from the high temperature heat source. In other words, the efficiency must be close to, equal to or exceed 100%, if the temperature of the working fluid of the expansion work is lower than At ambient temperature, it is impossible to dissipate heat from a low temperature heat source but can absorb heat from a low temperature heat source or be exported. The derived working fluid can be thrown into other heat sources at any temperature (including high temperature heat sources). For example, in an internal combustion engine, the high-temperature heat source of the internal combustion engine is the working fluid after the combustion of the fuel, and the low-temperature heat source (also referred to as the cold source) is the working medium after the expansion work, and the state of the working fluid after the expansion work is the fuel. Determined by the state of the working fluid after combustion. In this case, if the combustion process is controlled so that the state parameter of the working fluid after the combustion of the fuel reaches a certain value, the temperature of the working fluid after the expansion work can be made lower or even lower than the ambient temperature, such a cycle. The work output by the process must be close to, equal to or exceed the heat absorbed from the high temperature heat source. In other words, the efficiency must be close to, equal to or exceed 100%. If the temperature of the working fluid for expansion is lower than the ambient temperature, It is impossible to dissipate heat from a low temperature heat source but can absorb heat from a low temperature heat source or be derived, and the derived working fluid can be thrown into other heat sources at any temperature (including high temperature heat sources). On the surface, these two examples all create conditions that cannot be explained by existing thermodynamic theories and theorems. Therefore, the current understanding of the Carnot's theorem is misunderstood, so what is the so-called "heat from the high-temperature heat source" refers to which part of the heat, and the so-called "transfer a part of the absorbed heat to the low-temperature heat source" Which part of the heat is the part of the heat? The inventors believe that the heat of "absorbing heat from a high-temperature heat source" is the heat absorbed by the working medium from the high-temperature heat source during the process of heating the working medium from the temperature of the low-temperature heat source to the temperature of the high-temperature heat source (including the temperature of the high-temperature heat source) The heat absorbed by the lower working medium from the high temperature heat source) (shown as Q in Figure 11) and the bottom heat of the working medium (the so-called bottom heat of the working medium refers to the absolute zero degree contained in the working medium at the low temperature heat source temperature itself). The calculated heat (shown as Qc in Figure 1) consists of two parts, and the so-called "transfer a part of the heat absorbed to the low-temperature heat source" is the heat that is discharged from the working medium to the environment ( As shown by q in Figure 1) and the bottom heat of the working fluid (shown as Qc in Figure 11), it consists of two parts. In other words, even if the working temperature after the expansion work is lower than the ambient temperature, the working fluid can not transfer heat to the environment, as long as the working medium after the expansion work is found, such as thrown into the environment or thrown into any temperature. In other heat sources (including high temperature heat sources), the heat engine can be cycled. Not only that, but in certain specific Under the condition, the low temperature working fluid after expansion work can be thrown into the high temperature heat source of the system (as shown by the dotted line in Qc-ML in Fig. 12). For example, the working fluid cooled and condensed after expansion work can be thrown into the combustion of the internal combustion engine. In the inner or boiler steam generator, for example, the exhaust gas in the air motor is thrown into the environment (in some air engines, the environment is the high-temperature heat source of the air motor), and for example, it will be absorbed from the working fluid after the expansion work. The hot liquid is thrown into the high temperature heat source. From this, it can be concluded that the heat engine can work under a heat source, and the heat engine can be cycled as long as the working fluid after the expansion work is derived. The derived working fluid after expansion can be thrown into a heat source lower than its own temperature, can be thrown into the same heat source as its own temperature, can be thrown into a heat source higher than its own temperature, can be thrown into In the high-temperature heat source, it can also be thrown into a heat source higher than the temperature of the high-temperature heat source; not only that, if the working medium after the expansion work is only transferred to the low-temperature heat source, the heated low-temperature heat source can still be thrown into the high-temperature heat source. For example, the cooling medium for cooling the working fluid after the expansion work can be thrown into the high temperature heat source. Therefore, the necessary conditions for the operation of the heat engine are not two heat sources, but at least one heat source, at least one residual flow outlet (the so-called residual flow outlet refers to the outlet of the working fluid after the expansion work and/or the work after the expansion work) The outlet of the mass heat can be connected to any other heat source (including the high temperature heat source of the system), and in the structure in which the residual stream outlet is connected to the high temperature heat source, the heat machine only needs one heat source to circulate, In the structure in which the residual flow outlet is not in communication with the high temperature heat source, the heat engine needs at least two heat sources, and the residual flow outlet can only be when the residual flow outlet is in communication with a heat source having a temperature higher than the residual flow outlet. The outlet of the working fluid after the expansion work. The inventor's heat is: heat transfer and mass transfer during the operation of the heat engine may exist, coexist or replace each other. It is completely correct to say that it is impossible to transfer heat from a low temperature object to a high temperature object without any other influence, but we can throw a low temperature object (such as a low temperature working medium) into a high temperature object (such as a high temperature working medium) through mass transfer ( That is, the process of throwing a low-temperature object into a high-temperature object) realizes the unrealizable process of "transferring heat from a low-temperature object to a high-temperature object." The conclusion that the heat transfer and mass transfer during the operation of the heat engine can exist, coexist or replace each other is the conclusion that the work of manufacturing a high-efficiency heat engine or manufacturing output equals the calorific value of the fuel or the work output is greater than the heat value of the fuel. The direction. FIG. 1 , FIG. 12 and FIG. 13 are three cycle diagrams of q>0, q=0, and q<0, respectively.
本发明人认为, 热力学第二定律可以用下述说法加以诠释: 热机工作的必 要条件并不是两个热源, 而是至少一个热源, 至少一个残留流出口 (所谓的残 留流出口是指膨胀作功后的工质的出口和 /或膨胀作功后的工质的热量的出 口), 所述残留流出口可以与任何其他热源连通(包括系统的高温热源), 在所 述残留流出口与高温热源连通的结构中热机就只需要一个热源即可循环工作, 在所述残留流出口不与高温热源连通的结构中热机就需要至少有两个热源, 当 所述残留流出口与温度高于所述残留流出口的热源连通时所述残留流出口只 能是膨胀作功后的工质的出口。 卡诺在其 1824年发表的 《论火的动力》 论文 中提出的 "热机必须工作在两个热源之间, 从高温热源吸取热量, 又把所吸取 热量的一部分传递给低温热源, 只有这样才能获得机械功"的论述只是本发明 人对热力学第二定律的这一说法中的一个特例。 卡诺是一位伟大的科学家, 但 是在他的那个年代里内燃机还没有诞生, 可能正是因为这个原因局限了卡诺的 思想。 不仅如此, 在卡诺定理中只体现了温度, 而没有涉及到压力, 这一点说 明很有可能卡诺在构思卡诺定理的过程中是首先设定了两个温度不同的热源, 然后让热机(很可能是仅局限于外燃机)在这两个热源之间按照卡诺循环的方 式进行工作, 而这种模式恰恰与现实中的热机相反。 现实中的热机的低温热源The inventor believes that the second law of thermodynamics can be explained by the following statement: The condition is not two heat sources, but at least one heat source, at least one residual stream outlet (the so-called residual stream outlet refers to the outlet of the working fluid after the expansion work and/or the heat outlet of the working medium after the expansion work) The residual flow outlet may be in communication with any other heat source (including a high temperature heat source of the system), and in the structure in which the residual flow outlet is in communication with the high temperature heat source, the heat engine only needs one heat source to circulate, in the residual flow The heat exchanger in the structure that is not connected to the high temperature heat source needs at least two heat sources. When the residual stream outlet is in communication with a heat source having a temperature higher than the residual stream outlet, the residual stream outlet can only be expanded after work. The export of working fluids. In his 1824 paper "The Power of Fire", Carnot proposed that "the heat engine must work between two heat sources, extract heat from the high-temperature heat source, and pass a part of the heat absorbed to the low-temperature heat source. Only in this way The discussion of obtaining mechanical work is only a special case of the inventor's claim to the second law of thermodynamics. Kano is a great scientist, but in his time the internal combustion engine was not born, and it may be because of this reason that Karno's thought was limited. Not only that, but only the temperature is reflected in the Carnot's theorem, and there is no pressure involved. This shows that it is very likely that Carnot first set two heat sources with different temperatures in the process of conceiving the Carnots theorem, and then let the heat engine (Most likely to be limited to external combustion engines) work between the two heat sources in a Carnot cycle, which is exactly the opposite of a real heat engine. Low temperature heat source for real heat engines
(也叫冷源) 不是事先存在的, 而是由高温热源下工质的状态 (温度和压力) 以及工质的热力学性质所决定的, 换句话说, 现实中的热机的低温热源(也叫 冷源) 不是事先存在的, 而是根据高温热源下工质的状态 (温度和压力) 以及 工质的热力学性质, 膨胀过程自行制造的。 根据高温热源下工质的状态(温度 和压力)以及工质的热力学性质, 被膨胀过程自行制造的低温热源的温度是完 全可以低于环境温度的, 换句话说, 所输出的功完全可以高于从高温热源所吸 取的热量。 由此可以得出这样的结论: 在将高温热源的温度设置到环保温度限 值或材料温度限值的前提下, 要尽量提高高温热源下工质的压力, 以使膨胀作 功后工质的温度尽可能的低, 以提高发动机的效率。 在现实中, 热机的效率并 不是由高温热源的温度和环境温度所决定, 而是由高温热源状态下温度和压力 的值所决定的, 换句话说, 是由高温热源的温度和根据高温热源下工质的状态(also called cold source) is not pre-existing, but is determined by the state of the working fluid (temperature and pressure) under high temperature heat source and the thermodynamic properties of the working medium. In other words, the low temperature heat source of the actual heat engine (also called The cold source is not pre-existing, but is based on the state of the working fluid (temperature and pressure) under the high temperature heat source and the thermodynamic properties of the working medium. According to the state of the working fluid (temperature and pressure) under the high temperature heat source and the thermodynamic properties of the working medium, the temperature of the low temperature heat source which is self-made by the expansion process can be completely lower than the ambient temperature. In other words, the output work can be completely high. The heat extracted from the high temperature heat source. From this, it can be concluded that: under the premise of setting the temperature of the high-temperature heat source to the environmental temperature limit or the material temperature limit, it is necessary to increase the pressure of the working medium under the high-temperature heat source so as to make the working medium after the expansion work. The temperature is as low as possible to improve the efficiency of the engine. In reality, the efficiency of the heat engine is not determined by the temperature of the high temperature heat source and the ambient temperature, but by the value of the temperature and pressure in the high temperature heat source state. In other words, it is the temperature of the high temperature heat source and the heat source according to the high temperature. Lower working condition
(温度和压力)以及工质的热力学性质, 被膨胀过程自行制造的低温热源的温 度所决定的。 化学能是现代热机的能量的来源,然而本发明人认为在传统热机中对化学 能的利用存在着相当的缺陷, 导致这些缺陷的根本原因是, 对化学能的一个极 其重要的属性的理解不够深刻, 即对化学能是可以近乎向任何高能状态(高温 高压) 下的工质输入能量的属性的理解不够深刻。 本发明中, 为了说明方便, 将化学能是可以近乎向任何高能状态(高温高压)下的工质输入能量的属性定 义为化学能的超品性, 如果对化学能的超品性进行充分利用, 即可以使热机的 效率得到本质性的提高。 现以有压縮冲程(过程)且燃烧产物参与作功的热机 为例加以说明: 图 1 4中 S,、 S2和 S3是压縮力度不同的热机工作示意图, 压縮 力度按 S,、 S2和 S3顺序依次增加, Qh是燃料的化学能, 由于压縮过程所需要的 功是可以通过膨胀过程加以回收的, 假设压縮过程和膨胀过程都是可逆的, 则 不论压縮力度多高, 其本身并不影响热机的效率, 但是压縮力度越高, 相当于 将化学能提高到了更高的品位,这些处于更高品位的化学能在作功过程中可以 将其更大部分以功的形式输出, 如果状态参数合理, 被相当大的压縮力度提高 到相当高品位的化学能在膨胀作功过程中可以使工质的温度下降到大幅度低 于标准状态的程度, 进而使热机输出的功大于燃料的热值; 图 1 4中 S31是在有 膨胀剂存在的条件下燃料燃烧放出化学能后温度不变的过程,在此过程中, P2= Pi表示燃烧前后工质压力不变体积增大,输出的功 W接近化学能 Qh的过程, P2>P, 表示燃烧前后工质压力增大, 输出的功 W大于化学能 Qh的过程。 由此可见, 要 想制造出高效或超高效 (超高效表示热机输出的功等于或大于燃料的化学能) 的有压縮冲程 (过程) 且燃烧产物参与作功的热机, 就必须: 一、 大幅度增加 热机的压縮力度使化学能在相当高的能量级别上传递给工质; 二、 将化学能释 放后所形成的高温高压工质的状态参数合理化(所谓的 "将化学能释放后所形 成的高温高压工质的状态参数合理化"是指通过导入膨胀剂或其他方式使燃烧 后工质的压力和温度之间的关系能够使工质膨胀作功后的温度接近、 等于、 低 于或大幅度低于标准状态温度, 所谓的其他方式是在没有膨胀剂的条件下大幅 度提高发动机压縮冲程的力度,使压縮冲程完了时的压力和温度处于相当高的 状态后在利用化学能对工质进行加热升温, 见图 1 8中的高端位置所示的状态, 这种方式虽然制造不出超高效发动机, 但是可以制造出高效发动机, 然而所 S 要的压縮后的工质温度和压力相当高, 将对发动机的材料提出非常苛刻的要 求); 三、 合理选择工质和 /或膨胀剂 (所谓合理选择工质是指选择相变热小而 且在膨胀作功到设定程度时才液化的工质, 所谓合理选择膨胀剂是指选择相变 热小而且在膨胀作功到设定程度时才液化的膨胀剂)。 对于外燃机来说, 一、 必须使工质在相当高的压力和温度下吸热(用环境或其他低品位热源使工质处 于相当高的温度和压力下再利用化学能对工质加热); 二、 必须使吸热后的工 质的状态参数合理化; 三、 合理选择工质(所谓合理选择工质是指选择相变热 小而且在膨胀作功到设定程度时才液化的工质)。图 18是在对工质进行不同压 縮力度的前提下利用燃料燃烧对工质进行加热升温升压的详细计算数据图, 纵 轴为压力, 横轴为温度, 0-H为绝热压縮曲线, A,- E,、 A2-E2、 A3-E3、 ……、 A -En 表示不同压缩力度下由燃料燃烧对工质加热升温升压的直线, 而且随着 n值的 增加, 压縮力度不断加大, 由图 18可见, 燃烧升温升压直线的斜率随压縮力 度的提高而逐渐变大; 不难推理, 由图 18中的状态点 E,、 E2、 E3、 ……、 出 发绝热膨胀作功后, 随着 n值的增加, 工质的温度越低。 (Temperature and pressure) and the thermodynamic properties of the working fluid are determined by the temperature of the low temperature heat source that is self-manufactured by the expansion process. Chemical energy is the source of energy for modern heat engines. However, the inventors believe that the use of chemical energy in conventional heat engines has considerable defects, and the root cause of these defects is that the understanding of an extremely important property of chemical energy is insufficient. Deep, that is, the understanding of the properties of chemical energy that can be input energy to the working fluid in any high-energy state (high temperature and high pressure) is not deep enough. In the present invention, for the convenience of explanation, the chemical energy is an attribute that can input energy to a working medium in any high-energy state (high temperature and high pressure) as a super-existence of chemical energy, and if the super-characteristics of chemical energy are fully utilized That is, the efficiency of the heat engine can be substantially improved. Now take the heat engine with compression stroke (process) and combustion products involved in work as an example: Figure 1 4, S, S 2 and S 3 are schematic diagrams of the heat machine with different compression strengths. , S 2 and S 3 sequentially increase, Q h is the chemical energy of the fuel, since the work required for the compression process can be recovered through the expansion process, assuming that both the compression process and the expansion process are reversible, regardless of the pressure How high the shrinking force does not affect the efficiency of the heat engine itself, but the higher the compression strength, the higher the chemical energy is to a higher grade. These higher grade chemical energy can be more in the process of work. Most of them are output in the form of work. If the state parameters are reasonable, they are increased by a considerable compression force to a relatively high grade of chemical energy. During the expansion work, the temperature of the working medium can be lowered to a level significantly lower than the standard state. , in turn, the work output by the heat engine is greater than the heat value of the fuel; S 31 in Figure 14 is a process in which the temperature of the fuel is constant after the fuel burns out in the presence of a swelling agent, in the process, P 2 = Pi represents the process of increasing the volume of the working fluid before and after combustion, and the output work W is close to the chemical energy Q h , P 2 >P, indicating that the working pressure before and after combustion increases, and the output work W is greater than the chemical energy Q h . It can be seen that in order to produce a heat engine with a compression stroke (process) and combustion products involved in work, which is efficient or ultra-efficient (super efficient means that the output of the heat engine is equal to or greater than the chemical energy of the fuel), it must be: Significantly increase the compression force of the heat engine to transfer the chemical energy to the working medium at a relatively high energy level; 2. Rationalize the state parameters of the high temperature and high pressure working medium formed by the release of chemical energy (so-called "after chemical energy release" The rationalization of the state parameters of the formed high-temperature and high-pressure working medium means that the relationship between the pressure and the temperature of the working fluid after combustion can be made to bring the temperature of the working medium to work close to, equal to, or lower than the temperature by the introduction of the expanding agent or other means. Or substantially lower than the standard state temperature, the so-called other way is to greatly increase the strength of the engine compression stroke without the expansion agent, so that the pressure and temperature at the end of the compression stroke are at a relatively high state It can heat and heat the working fluid, as shown in the high-end position in Figure 18. Although this method does not produce an ultra-efficient engine, It is possible to manufacture a highly efficient engine, however, S The required temperature and pressure of the compressed working fluid are quite high, which will impose very demanding requirements on the material of the engine.) 3. Reasonable selection of working medium and/or expansion agent (so-called reasonable choice of working medium means selection of phase change heat is small) Moreover, the working fluid which is liquefied when the expansion work is set to a certain degree, the so-called rational selection of the expansion agent refers to a swelling agent which is selected to be liquefied when the expansion heat is small to a set degree. For external combustion engines, first, the working fluid must absorb heat at a relatively high pressure and temperature (using environment or other low-grade heat source to make the working medium at a relatively high temperature and pressure, then use chemical energy to heat the working medium. Second, the state parameters of the working fluid after the endotherm must be rationalized; Third, the reasonable selection of the working medium (the so-called reasonable choice of working medium refers to the selection of the phase change heat is small and the liquid is liquefied when the expansion work to the set level) quality). Figure 18 is a detailed calculation data of heating and warming up the working fluid by fuel combustion under the premise of different compression strength of the working medium. The vertical axis is pressure, the horizontal axis is temperature, and 0-H is adiabatic compression. The curves, A, - E, A 2 - E 2 , A 3 - E 3 , ..., A - E n represent the straight line of heating and heating of the working medium by fuel combustion under different compression forces, and with the value of n The increase of compression, the compression strength continues to increase, as can be seen from Figure 18, the slope of the combustion temperature rise line gradually increases with the increase of compression strength; it is not difficult to reason, from the state point E, E 2 in Figure 18 E 3 , ..., After starting the adiabatic expansion work, as the value of n increases, the temperature of the working medium is lower.
本发明所公开的小温升低熵混燃发动机中, 图 18还说明了: 传统内燃机 中温度过剩的情况是十分严重的, 也就是说在传统内燃机中燃烧后与压力相 比, 温度远远超于必要的值, 也可以说, 与温度相比,压力远远低于必要的值。 从这一点我们不难得出这样的结论: 如果我们能够找到能够承受更高的温度和 更高压力的优质材料, 使外燃机的工质的压力和温度按照 P = C (其中, 是常数, 尸是气体工质压力, Γ是气体工质温度, 为绝热压縮指数) 的关系 大幅度提高,或者如果我们能够找到一种新型加热方式使外燃机的工质的压力 和温度按照 P - C ^的关系大幅度提高, 就可以制造出高效外燃机。 从这个方 面上讲, 外燃循环是具有制造出效率高于内燃循环的潜力的一种循环方式。 本 发明所公开的小温升低熵混燃发动机就是利用了外燃循环和内燃循环的各自 优势, 使发动机的效率实现本质性提高。  In the small temperature rise and low entropy co-firing engine disclosed by the present invention, FIG. 18 also illustrates that: the temperature excess in the conventional internal combustion engine is very serious, that is, in the conventional internal combustion engine, the temperature is far after the combustion compared with the pressure. Exceeding the necessary values, it can be said that the pressure is much lower than the necessary value compared with the temperature. From this point we can easily conclude that if we can find high-quality materials that can withstand higher temperatures and higher pressures, the pressure and temperature of the external combustion engine's working fluid should be P = C (where is constant) The corpse is the gas working fluid pressure, the temperature of the gas working fluid, the relationship of the adiabatic compression index) is greatly improved, or if we can find a new heating method to make the pressure and temperature of the working fluid of the external combustion engine according to P - The relationship between C and ^ is greatly improved, and a highly efficient external combustion engine can be manufactured. In this respect, the external combustion cycle is a cyclical way to create a higher efficiency than the internal combustion cycle. The small temperature rise and low entropy co-firing engine disclosed by the invention utilizes the respective advantages of the external combustion cycle and the internal combustion cycle, so that the efficiency of the engine is substantially improved.
经更加深入地对传统内燃机的工作过程的详细分析,我们可以得出如下结 论: 发动机气缸内的气体工质的最高能量状态(即燃烧刚刚完了时的气体工质 状态, 此时气体工质的温度和压力都是处于整个循环中的最高状态)是由两个 过程组成的:第一个过程是活塞对气体进行绝热压縮(实际上是近似绝热压縮) 将气体的温度和压力按照 ρ = ςΓ^ (其中, ^是常数, Ρ是气体工质压力, Γ是 气体工质温度, 为绝热压縮指数, 空气的绝热压縮指数为 1 . 4) 的关系进行 增压增温(见图 1 7中的 0-Α所示的曲线); 第二个过程是向气体内喷入燃料由 燃烧化学反应产生的热量在近乎等容加热的状态下将气体的温度和压力按照 P = C2T (其中, (:2是常数) 的关系进行增温增压 (见图 1 7中的 A - E所示的直 线, 图 1 7是纵轴为压力坐标横轴为温度坐标的压力温度关系图)。 由这两个过 程共同作用使工质处于作功即将开始状态, 作功冲程是按照绝热膨胀过程(实 际上是近似绝热膨胀)进行的(见图 1 7中的 E-F所示的曲线), 在这个绝热膨 胀过程中, 在对外输出功的同时, 工质按照 = C3r^ (其中, 3是常数) 的关 系降压降温直至作功冲程完了 (点 F所示的状态)。 换句话说, 达到工质最高 能量状态是通过两个不同过程实现的, 而由工质最高能量状态达到作功冲程完 了时的状态是由一个绝热膨胀过程实现的。 由于达到能量最高状态的过程中包 括了一个燃烧化学反应放热升温的过程, 此过程的温度和压力关系式为 P = C2T , 不难看出工质最高能量状态下(见图 1 7中的点 E所示的状态), 温度 处于 "过剩"状态 (所谓的 "过剩"温度是指按照绝热膨胀的关系为了达到某 一终点状态, 在起点状态下工质的实际温度高于理论上所需要的温度, 在本发 明中所谓的某一终点状态是指接近 0点的状态), "过剩"的温度导致膨胀过程 的曲线处于高温位置 (在图 1 7中向右移动, 即点 F的状态, 也就是说, 点 F 处于点 0的右侧), 形成作功冲程完了时, 温度仍然相当高的状态(如图 1 7中 曲线 E-F所示的曲线上的点 F所示的状态), 由图 1 7中点 F所示的状态不难看 出, Γ2 (即作功冲程完了时的工质温度, 也就是低温热源的温度) 仍然处于较 高状态, 也就是说仍然有相当的热量在工质内而没有变成功, 这部分热量全部 白白排放至环境, 因此, 效率会处于较低状态。 图 15是描述燃烧后气体工质 的压力和温度关系符合绝热压縮过程温度和压力关系的示意图, 点八、 点 8、 点 C三点分别表示压縮冲程完了时的状态, 点 ΑΑ表示由点 Α开始燃烧化学反 应后达到的状态, 点 BB表示由点 B开始燃烧化学反应后达到的状态, 点 CC表 示由点 C开始燃烧化学反应后达到的状态, 点 0是压縮冲程的起点也是膨胀作 功冲程的终点。 图 1 6是描述燃烧后气体工质的压力大于由绝热压縮过程的压 力和温度的关系所确定的压力值的示意图, 点 、 点 B、 点 C三点分别表示压 縮冲程完了时的状态; 点 AA表示由点 A开始燃烧化学反应后达到的状态, 点 AAA表示由点 AA膨胀作功达到的终点; 点 BB表示由点 B开始燃烧化学反应后 达到的状态, 点 BBB表示由点 BB膨胀作功达到的终点; 点 CC表示由点 C开始 燃烧化学反应后达到的状态,点 CGC表示由点 CC膨胀作功达到的终点。图 1 7 是 压縮冲程完了时不同增温增压过程和加大压縮冲程的力度,使被压縮气体的温 度达到环保温度限值或材料温度限值且燃烧前后温度不变或者没有明显变化, 而压力大幅增加的过程示意图 (包括与传统内燃机循环的比较曲线); A-CC、 A-BB、 A- AA表示不同升温升压过程,点 D表示被压縮气体的温度达到环保温度 限值或材料温度限值的压縮冲程完了时的状态, D-DD表示燃烧前后温度不变或 者没有明显变化而压力大幅增加的过程, 点 DDD、 点 CCG、 点 BBB、 点 AAA和点 0分别表示不同过程的膨胀作功终点。 如图 15、 图 16和图 1 7所示, 如果我们 能够找到一种方法使燃烧后的工质的压力温度状态点处于绝热压縮过程的压 力温度曲线 0-H上或处于绝热压縮过程的压力温度曲线 0-H左方, 则膨胀作功 后的工质温度将可达到等于 0点的温度、低于 0点的温度或大幅度低于 0点的 温度的状态, 这样将使发动机的效率大幅度提高, 而且可以制造出输出的功接 近燃料热值、 等于燃料热值或大于燃料热值的发动机。 如果燃烧后的工质的压 力温度状态点处于绝热压縮过程的压力温度曲线 0- H右侧, 虽然不能制造出输 出的功等于燃料热值或大于燃料热值的发动机,但通过使燃烧后的工质的压力 温度状态点尽可能靠近 0-H曲线, 以达到效率的提高。 而要想使燃烧后的工质 的压力温度状态点处于曲线 0- H上或处于曲线 0- H左方, 可行的办法是使燃烧 化学反应放出的热量的全部或部分被所述膨胀剂吸收增加即将开始作功的气 体工质的摩尔数, 形成燃烧后的工质压力不低于由公式/ > = (尸。 + PJ(77r。)^ (其 中, 尸是燃烧后的工质压力, P。是绝热压縮后未燃烧未导入膨胀剂的工质压力, 是燃烧后膨胀剂所形成的分压, Γ是燃烧后的工质温度, 7是绝热压縮后未 燃烧未导入膨胀剂的工质温度, ^为绝热压縮指数, 空气的绝热压縮指数为 1 . 4) 所确定的压力值, 即尸值, 这样就能保证燃烧后的工质的压力温度状态 点处于曲线 0-H上或处于曲线 0-H左方, 这样才能实现更高的效率和更好的环 保性。 本发明所公开的小温升低熵混燃发动机依据上述理论, 公开了如下技术 方案: 在压縮冲程 /过程完了时, 使燃烧化学反应放出的热量的一定比例或全 部被已导入所述燃烧室的膨胀剂吸收增加即将开始作功的气体工质的摩尔数, 例如图 1 7中 A-GC、 A-BB、 A-AA所示被已导入所述燃烧室的膨胀剂所吸收的燃 烧化学反应所放出的热量的量按 A-AA、 A-BB、 A-CC依次增加; 为了进一步提 高效率和环保性,本发明所公开的小温升低熵混燃发动机还公开了另外一种技 术方案: 大幅度提高对气体的压縮力度, 使被压縮气体的温度达到环保温度限 值或材料温度限值,并且使燃烧化学反应放出的热量全部被已导入所述燃烧室 的膨胀剂吸收增加即将开始作功的气体工质的摩尔数, 形成燃烧前后温度不变 或者没有明显变化, 而压力大幅增加的状态 (例如图 1 7中 D-DD所示)。 After a more detailed analysis of the working process of a conventional internal combustion engine, we can draw the following conclusions: The highest energy state of the gas working fluid in the engine cylinder (ie, the gas working state when the combustion is just finished, at this time the gas working fluid Temperature and pressure are at the highest state throughout the cycle) are made up of two The process consists of: the first process is the adiabatic compression of the gas by the piston (actually approximately adiabatic compression). The temperature and pressure of the gas are in accordance with ρ = ςΓ^ (where ^ is a constant, Ρ is a gaseous working fluid) The pressure, Γ is the gas working temperature, the adiabatic compression index, and the adiabatic compression index of the air is 1. 4) for the boosting and warming (see the curve shown by 0-Α in Figure 17.) The second process is to inject fuel into the gas. The heat generated by the combustion chemical reaction is in the state of near isovolumic heating. The temperature and pressure of the gas are in accordance with P = C 2 T (where (: 2 is a constant) relationship. The warming pressurization is carried out (see the line shown by A - E in Fig. 17), and Fig. 17 is the pressure-temperature relationship diagram in which the vertical axis is the pressure coordinate and the horizontal axis is the temperature coordinate.) The two processes work together. The quality is at the beginning of the work, and the power stroke is performed according to the adiabatic expansion process (actually approximately adiabatic expansion) (see the curve shown by EF in Fig. 17). During this adiabatic expansion, the external output is At the same time, the working fluid is in accordance with = C 3 r^ (where 3 is The relationship of the constants is lowered by the temperature until the power stroke is completed (the state shown by point F). In other words, the highest energy state of the working medium is achieved by two different processes, and the highest energy state of the working medium reaches the work. The state at the end of the stroke is achieved by an adiabatic expansion process. Since the process of reaching the highest energy state includes a process of exothermic heating of the combustion chemical reaction, the relationship between temperature and pressure of this process is P = C 2 T , It is difficult to see that the working medium has the highest energy state (see the state shown by point E in Fig. 17), and the temperature is in the "excess" state (the so-called "excess" temperature means that in order to reach a certain end state according to the relationship of adiabatic expansion, In the starting state, the actual temperature of the working medium is higher than the theoretically required temperature. In the present invention, the so-called end point state refers to a state close to zero point), and the "excess" temperature causes the curve of the expansion process to be in a high temperature position. (moving to the right in Figure 17. That is, the state of point F, that is, point F is on the right side of point 0), when the power stroke is completed, the temperature is still quite high. State (as shown by the point F on the curve shown by the curve EF in Fig. 17), it is easy to see from the state shown by the point F in Fig. 17. Γ 2 (that is, the working fluid when the power stroke is completed) The temperature, that is, the temperature of the low-temperature heat source, is still in a high state, that is, there is still considerable heat in the working medium without success, and this part of the heat is completely discharged to the environment, so the efficiency will be in a low state. Figure 15 is a schematic diagram showing the relationship between the pressure and temperature of the gas working fluid after combustion in accordance with the temperature and pressure of the adiabatic compression process. The three points of point eight, point 8, and point C respectively indicate the state when the compression stroke is completed, and the point ΑΑ indicates The state reached after the combustion of the chemical reaction is started from the point ,, the point BB represents the state reached after the combustion of the chemical reaction from the point B, the point CC represents the state reached after the combustion of the chemical reaction from the point C, and the point 0 is the starting point of the compression stroke. Also inflated The end of the power stroke. Figure 16 is a schematic diagram showing the pressure value of the gas working fluid after combustion is greater than the pressure value determined by the relationship between the pressure and temperature of the adiabatic compression process. The three points of point, point B and point C respectively indicate when the compression stroke is completed. State; point AA indicates the state reached after burning chemical reaction from point A, point AAA indicates the end point reached by expansion of point AA; point BB indicates the state reached after burning chemical reaction from point B, point BBB indicates point by point The end point at which the BB expansion work is reached; the point CC indicates the state reached after the combustion of the chemical reaction from the point C, and the point CGC indicates the end point reached by the expansion of the point CC. Figure 1 7 is the intensity of different warming pressurization process and increasing the compression stroke when the compression stroke is completed, so that the temperature of the compressed gas reaches the environmental temperature limit or the material temperature limit and the temperature before or after combustion is constant or not obvious. Change, and the process diagram of the pressure increase greatly (including the comparison curve with the traditional internal combustion engine cycle); A-CC, A-BB, A-AA indicate different temperature rise and pressure rise process, point D indicates that the temperature of the compressed gas reaches the environmental protection temperature The state of the limit or material temperature limit at the end of the compression stroke, D-DD indicates the process of constant or no significant change in pressure before and after combustion, point DDD, point CCG, point BBB, point AAA, and point 0 Represents the end points of the expansion work for different processes. As shown in Fig. 15, Fig. 16, and Fig. 17, if we can find a way to make the pressure temperature state point of the burned working medium be at the pressure temperature curve 0-H of the adiabatic compression process or at adiabatic pressure. The pressure temperature curve of the shrinking process is 0-H to the left, and the working temperature after the expansion work can reach a temperature equal to 0, a temperature lower than 0, or a temperature lower than 0, which will The efficiency of the engine is greatly improved, and an engine whose output work is close to the fuel heat value, equal to the fuel heat value, or greater than the fuel heat value can be manufactured. If the pressure temperature state point of the burned working fluid is on the right side of the pressure temperature curve 0-H of the adiabatic compression process, although the engine whose output work is equal to the fuel heat value or greater than the fuel heat value cannot be produced, by burning The pressure temperature state point of the working fluid is as close as possible to the 0-H curve to achieve an increase in efficiency. However, if the pressure temperature state point of the burned working fluid is on the curve 0-H or on the left side of the curve 0-H, it is feasible to absorb all or part of the heat released by the combustion chemical reaction by the expansion agent. Increase the number of moles of gas working fluid that is about to start work, and the pressure of the working fluid after combustion is not lower than the formula / > = (corpse. + PJ (77r.) ^ (where the corpse is the working pressure of the burning, P. is the working pressure of unburned and not introduced into the expansion agent after adiabatic compression, is the partial pressure formed by the expansion agent after combustion, Γ is the working temperature after combustion, 7 is not burned after adiabatic compression, not introduced The working temperature of the expanding agent, ^ is the adiabatic compression index, and the adiabatic compression index of the air is 1. 4) The determined pressure value, that is, the corpse value, thus ensuring the pressure temperature state of the working medium after combustion The point is on curve 0-H or on the left side of curve 0-H to achieve higher efficiency and better environmental friendliness. According to the above theory, the small temperature rise and low entropy co-firing engine disclosed in the present invention discloses the following technical solution: when the compression stroke/process is completed, a certain proportion or all of the heat released by the combustion chemical reaction is introduced into the combustion. The expansion agent absorption of the chamber increases the number of moles of gas working medium to be started, for example, the combustion absorbed by the expansion agent introduced into the combustion chamber as shown by A-GC, A-BB, A-AA in Fig. 17. The amount of heat released by the chemical reaction increases in order of A-AA, A-BB, and A-CC; in order to further improve efficiency and environmental protection, the small temperature rise and low entropy co-combustion engine disclosed by the present invention also discloses another type. Technical solution: The compression of the gas is greatly increased, the temperature of the compressed gas reaches the environmental temperature limit or the material temperature limit, and the heat released by the combustion chemical reaction is completely introduced into the expansion agent of the combustion chamber. Absorption increases the number of moles of gaseous working fluid that is about to start work, forming a state in which the temperature before or after combustion is constant or does not change significantly, and the pressure is greatly increased (for example, as shown by D-DD in Fig. 17).
本发明所公开的小温升低熵混燃发动机中,在燃料燃烧化学反应放出的热 量的一定比例被已导入所述燃烧室的膨胀剂吸收增加即将开始作功的气体工 质的摩尔数的结构中, 燃烧室内的温度和压力均会提高, 但是压力的提高是由 两个因素构成的: 第一个因素是由于工质吸收燃烧化学反应所放出热量的一部 分导致工质温度升高 (按定容升温考虑), 进而按直线关系导致压力升高; 第 二个因素是由于膨胀剂吸收燃烧化学反应所放出热量的一部分导致燃烧室内 气相摩尔数增加, 而导致压力增加, 这种压力增加不是由于升温所致, 即便温 度下降、 温度恒定或温度有所增加, 在这个过程中, 压力都会明显增加, 所谓 的压力明显增加是指压力增加的值不仅大于由 > = C2r所确定的压力值,而且大 于由 P = Cir 所确定的压力值。 第一个因素所营造的状态是温度过剩状态, 第 二个因素所营造的状态是温度负过剩状态,科学控制被膨胀剂吸收的燃料燃烧 化学反应所放出热量的量, 可以实现控制这两种因素的影响力, 进而实现燃烧 后温度升高、压力升高,但所形成的工质的状态点(由温度和压力所决定的点) 在图 1 7所示 0-H曲线的左侧或在 0- H曲线上或在 0-H曲线的右侧但尽可能靠 近 0- H曲线。 In the small temperature rise and low entropy co-firing engine disclosed in the present invention, a certain proportion of the heat released by the chemical reaction of the fuel combustion is absorbed by the expansion agent introduced into the combustion chamber to increase the number of moles of the gaseous working medium to be started to work. In the structure, the temperature and pressure in the combustion chamber will increase, but the pressure increase is composed of two factors: The first factor is that the working medium absorbs a part of the heat released by the combustion chemical reaction, causing the temperature of the working medium to rise. The constant temperature rise is considered), and then the pressure rises in a linear relationship; the second factor is that the expansion agent absorbs a part of the heat released by the combustion chemical reaction, causing the gas phase number in the combustion chamber to increase, resulting in an increase in pressure, which is not an increase in pressure. Due to the temperature rise, even if the temperature drops, the temperature is constant, or the temperature increases, the pressure will increase significantly during this process. The so-called pressure increase means that the pressure increase is not only greater than the pressure determined by >= C 2 r Value, and greater than the pressure value determined by P = Cir . The state created by the first factor is the state of over-temperature, and the state created by the second factor is the state of negative temperature excess. Scientifically controlling the amount of heat released by the chemical reaction of the fuel absorbed by the expansion agent can achieve control. The influence of the factor, and then the temperature rise and pressure rise after combustion, but the state point of the formed working fluid (the point determined by temperature and pressure) is on the left side of the 0-H curve shown in Figure 17. On the 0-H curve or on the right side of the 0-H curve but as close as possible to the 0-H curve.
本发明所公开的小温升低熵混燃发动机,被导入燃烧室的膨胀剂不仅可以 吸收燃料燃烧所放出的全部的热量, 而且还可以吸收一部分已经被压縮的气 工质的热量, 在这种情况下, 即将开始作功的工质的温度比压縮冲程 /过程终 了时的工质温度低。 The small temperature rising low entropy co-firing engine disclosed by the invention can not only absorb the total heat released by the fuel combustion, but also absorb a part of the compressed gas. The heat of the working fluid, in this case, the temperature of the working fluid to be started to work is lower than the working temperature at the end of the compression stroke/process.
图 1 9是本发明所公开的小温升低熵混燃发动机的循环和传统内燃机的循 环的示功对比图, 图中 a-b-c-d-a所示的曲线是传统内燃机循环的示功图, 图 中 a-b-m-s-a所示的曲线是本发明所公开的小温升低熵混燃发动机在压縮冲程 完了时的压力略大于传统内燃机压縮终了时的压力时但是燃烧化学反应放出 的热量的全部或近乎全部被已导入所述燃烧室的膨胀剂吸收增加即将开始作 功的气体工质的摩尔数, 形成燃烧前后温度不变或者没有明显变化, 而压力大 幅增加的状态所构成的循环示功图, 图中 a- z-n-t-a所示的曲线是本发明所公 开的小温升低熵混燃发动机在压縮冲程完了时的温度达到环保温度限值或材 料温度限值并且使燃烧化学反应放出的热量的全部或近乎全部被已导入所述 燃烧室的膨胀剂吸收增加即将开始作功的气体工质的摩尔数, 形成燃烧前后温 度不变或者没有明显变化, 而压力大幅增加的状态所构成的循环示功图。 不难 看出, 本发明所公开的小温升低熵混燃发动机与传统内燃机相比, 具有更高的 效率和更好的环保性。  Figure 19 is a comparison diagram of the cycle of the cycle of the small temperature rise and low entropy co-firing engine disclosed in the present invention and the cycle of the conventional internal combustion engine. The curve shown by abcda is a diagram of the cycle of the conventional internal combustion engine, in which abmsa The curve shown is that the pressure of the small temperature rise and low entropy co-firing engine disclosed in the present invention when the compression stroke is completed is slightly larger than the pressure at the end of the compression of the conventional internal combustion engine, but all or nearly all of the heat released by the combustion chemical reaction has been The expansion agent introduced into the combustion chamber absorbs the number of moles of gas working medium that is about to start work, and forms a cycle diagram of a state in which the temperature before or after combustion is constant or does not change significantly, and the pressure is greatly increased, in the figure, a - the curve shown by znta is the total or near-heat of the temperature of the small temperature rise and low entropy co-firing engine disclosed in the present invention when the compression stroke is completed, the temperature reaches the environmental temperature limit or the material temperature limit, and the combustion chemical reaction is released. All of the expansion agent introduced into the combustion chamber absorbs the number of moles of gaseous working fluid that is about to start work, forming before and after combustion. Of the same or did not change significantly, and the cycle indicator diagram of a substantial increase in the pressure state thereof. It is not difficult to see that the small temperature rise and low entropy co-firing engine disclosed by the present invention has higher efficiency and better environmental protection than conventional internal combustion engines.
本发明中, 图 20是气体工质的温度 T和压力 P的关系图, 0-A- H所示曲线 是通过状态参数为 298K和 0. 1 MPa的 0点的气体工质绝热关系曲线; B点为气 体工质的实际状态点, E-B-D所示曲线是通过 B点的绝热关系曲线, A点和 B 点的压力相同; F- G所示曲线是通过 2800K和 10MPa (即目前内燃机中即将开 始作功的气体工质的状态点) 的工质绝热关系曲线。  In the present invention, FIG. 20 is a graph showing the relationship between the temperature T and the pressure P of the gas working medium, and the curve indicated by 0-A-H is a gas working adiabatic relationship curve passing through the zero point of the state parameter of 298 K and 0.1 MPa; Point B is the actual state point of the gas working fluid. The curve shown by EBD is the adiabatic relationship curve passing through point B. The pressures at point A and point B are the same; the curve shown by F-G is through 2800K and 10MPa (that is, the current internal combustion engine is about to The adiabatic relationship curve of the working point of the gaseous working fluid that starts work.
本发明中, 所谓的类绝热关系包括下列三种情况: 1 .气体工质的状态参数 (即工质的温度和压力)点在所述工质绝热关系曲线上, 即气体工质的状态参 数点在图 20中 0-A-H所示曲线上; 2.气体工质的状态参数 (即工质的温度和 压力) 点在所述工质绝热关系曲线左侧, 即气体工质的状态参数点在图 20 中 0-A-H所示曲线的左侧; 3.气体工质的状态参数 (即工质的温度和压力) 点在 所述工质绝热关系曲线右侧, 即气体工质的状态参数点在图 20中 0-A-H所示 曲线的右侧,但是气体工质的温度不高于由此气体工质的压力按绝热关系计算 所得温度加 1000K的和、 加 950K的和、 加 900K的和、 加 850K的和、 加 800K 的和、 加 750K的和、 加 700K的和、 加 650K的和、 加 600K的和、 加 550K的 和、 加 500K的和、 加 450K的和、 加 400K的和、 加 350K的和、 加 300K的和、 加 250K的和、 加 200K的和、 力 Π 1 90K的和、 力 H 180K的和、 力 [] 1 70K的和、 加 1 60K的和、力 Π 1 50K的和、力卩 140K的和、力 B 130K的和、加 1 20K的和、加 1 10K 的和、 加 100K的和、 加 90K的和、 加 80K的和、 加 70K的和、 加 60K的和、 加 50K的和、 加 40K的和、 加 30K的和或不高于加 20K的和, 即如图 20所示, 所述气体工质的实际状态点为 B点, A点是压力与 B点相同的绝热关系曲线上 的点, A点和 B点之间的温差应小于 1 000Κ、 900Κ、 850Κ、 800Κ、 750Κ、 700Κ、 650Κ、 600Κ、 550Κ、 500Κ、 450Κ、 400Κ、 350Κ、 300Κ、 250Κ、 200Κ、 1 90Κ、 180Κ、 1 70Κ、 1 60Κ、 150Κ、 140Κ、 130Κ、 1 20Κ、 1 10Κ、 100Κ、 90Κ、 80Κ、 70Κ、 60Κ、 50Κ、 40Κ、 30Κ或小于 20Κ。 In the present invention, the so-called adiabatic relationship includes the following three cases: 1. The state parameter of the gaseous working fluid (ie, the temperature and pressure of the working medium) is on the adiabatic relationship curve of the working fluid, that is, the state parameter of the gaseous working fluid. The point is on the curve shown by 0-AH in Figure 20; 2. The state parameter of the gas working fluid (ie the temperature and pressure of the working medium) is on the left side of the adiabatic relationship curve of the working fluid, that is, the state parameter point of the gas working fluid. On the left side of the curve shown by 0-AH in Figure 20; 3. The state parameter of the gas working fluid (ie, the temperature and pressure of the working fluid) is on the right side of the adiabatic relationship curve of the working fluid, that is, the state parameter of the gas working fluid. The point is on the right side of the curve shown by 0-AH in Fig. 20, but the temperature of the gas working fluid is not higher than the temperature of the gas working fluid calculated by the adiabatic relationship plus the sum of 1000K, the sum of 950K, and 900K. And, add 850K and add 800K And, add 750K and, add 700K and, add 650K and add 600K and add 550K and add 500K and add 450K and add 400K and add 350K and add 300K And, add 250K and, add 200K and, force 1 90K and force H 180K, force [] 1 70K sum, add 1 60K sum, force Π 1 50K sum, force 卩 140K And sum of force B 130K, add 1 20K sum, add 1 10K sum, add 100K sum, add 90K sum, add 80K sum, add 70K sum, add 60K sum, plus 50K sum Add 40K sum, add 30K and or not to add 20K, that is, as shown in Figure 20, the actual working point of the gas working medium is point B, and point A is the same adiabatic relationship of pressure and point B. The point on the curve, the temperature difference between point A and point B should be less than 1 000Κ, 900Κ, 850Κ, 800Κ, 750Κ, 700Κ, 650Κ, 600Κ, 550Κ, 500Κ, 450Κ, 400Κ, 350Κ, 300Κ, 250Κ, 200Κ, 1 90Κ, 180Κ, 1 70Κ, 1 60Κ, 150Κ, 140Κ, 130Κ, 1 20Κ, 1 10Κ, 100Κ, 90Κ, 80Κ, 70Κ, 60Κ, 50Κ, 40Κ, 30Κ or small At 20 baht.
本发明中,所谓类绝热关系可以是上述三种情况中的任何一种,也就是指: 即将开始作功的气体工质的状态参数(即气体工质的温度和压力)点在如图 20 所示的通过 Β点的绝热过程曲线 E-B- D的左侧区域内。  In the present invention, the so-called adiabatic relationship may be any one of the above three cases, that is, the state parameter of the gas working medium to be started working (ie, the temperature and pressure of the gas working medium) is as shown in FIG. 20 . The adiabatic process curve shown through the defect is in the left region of the EB-D.
本发明中, 所谓的即将开始作功的气体工质是指燃烧反应和膨胀剂导入过 程均完成时的气体工质。  In the present invention, the so-called gaseous working fluid which is about to start work refers to a gaseous working fluid when both the combustion reaction and the expansion agent introduction process are completed.
本发明中, 将即将开始作功的气体工质的状态参数(即气体工质的温度和 压力) 符合类绝热关系的发动机系统 (即热动力系统) 定义为低熵发动机。  In the present invention, an engine system (i.e., a thermodynamic system) in which the state parameters of the gaseous working medium (i.e., the temperature and pressure of the gaseous working medium) to be started to work is classified as a low-entropy engine is defined.
本发明中, 调整充入所述燃烧室内的气体工质的状态 (即温度、 压力和质 量), 调整向所述燃烧室导入燃料的量以及向系统内导入膨胀剂的量使即将开 始作功的气体工质的温度和压力符合类绝热关系。  In the present invention, the state (i.e., temperature, pressure, and mass) of the gaseous working medium charged in the combustion chamber is adjusted, the amount of fuel introduced into the combustion chamber is adjusted, and the amount of the expanding agent introduced into the system is caused to start work. The temperature and pressure of the gaseous working fluid are in a class of adiabatic relationships.
本发明中,通过对气体工质在压縮过程中进行冷却或将压縮后的气体工质 进行冷却的方式, 通过对气体工质进行大幅度增压的方式 (如多级压縮), 通 过向所述燃烧室导入膨胀剂的方式,使即将开始作功的气体工质的温度和压力 符合类绝热关系。  In the present invention, by cooling the gas working medium during the compression process or cooling the compressed gas working medium, the gas working medium is greatly pressurized (for example, multi-stage compression). By introducing a swelling agent into the combustion chamber, the temperature and pressure of the gaseous working fluid to be started to work are in an adiabatic relationship.
为了制造出高效和超高效发动机, 本发明提出了下述方案:  In order to produce an efficient and ultra efficient engine, the present invention proposes the following scheme:
一种小温升低熵混燃发动机, 包括燃烧室, 膨胀剂源和燃料源, 所述燃料 源经燃料导入控制机构与所述燃烧室连通, 所述膨胀剂源经膨胀剂导入控制机 构与所述燃烧室连通,所述燃料导入控制机构和所述膨胀剂导入控制机构受燃 烧控制装置控制; 所述燃烧室设为活塞式发动机燃烧室, 所述活塞式发动机燃 烧室的承压能力大于等于 4MPa,或所述燃烧室设为轮机燃烧室,所述轮机燃烧 室的承压能力大于等于 2MPa。 A small temperature rise low entropy co-firing engine includes a combustion chamber, a source of expansion agent and a fuel source, the fuel source being in communication with the combustion chamber via a fuel introduction control mechanism, and the source of the expansion agent is introduced into the control machine via an expansion agent Constructed in communication with the combustion chamber, the fuel introduction control mechanism and the expansion agent introduction control mechanism are controlled by a combustion control device; the combustion chamber is set as a piston engine combustion chamber, and a pressure of the piston engine combustion chamber is The capacity is greater than or equal to 4 MPa, or the combustion chamber is set to be a turbine combustion chamber, and the pressure capacity of the turbine combustion chamber is greater than or equal to 2 MPa.
在所述燃烧室和所述膨胀剂源之间设膨胀剂吸热热交换器,使所述膨胀剂 源内的膨胀剂在所述膨胀剂吸热热交换器中吸热。  An expansion agent heat absorption heat exchanger is disposed between the combustion chamber and the expansion agent source to cause the expansion agent in the expansion agent source to absorb heat in the expansion agent heat absorption heat exchanger.
所述膨胀剂吸热热交换器的热源设为所述小温升低熵混燃发动机的余热。 所述膨胀剂源内的膨胀剂在所述膨胀剂吸热热交换器中吸热达到临界状 态、 超临界状态或超超临界状态后再进入所述燃烧室。  The heat source of the expansion agent heat absorption heat exchanger is set as the residual heat of the small temperature rise low entropy co-firing engine. The expansion agent in the expansion agent source enters the combustion chamber after the endothermic heat in the expansion agent heat absorption heat exchanger reaches a critical state, a supercritical state, or an ultra-supercritical state.
所述小温升低熵混燃发动机还包括氧化剂源和气体连通通道,所述气体连 通通道连通所述燃烧室的进气道和排气道, 在所述排气道上设排气放出口, 在 所述排气放出口处设排气放出控制阀, 所述氧化剂源经氧化剂导入控制机构再 经所述进气道与所述燃烧室连通或直接经所述氧化剂导入控制机构与所述燃 烧室连通, 所述氧化剂导入控制机构、 所述燃料导入控制机构和所述膨胀剂导 入控制机构受燃烧控制装置控制。  The small temperature rise low entropy co-firing engine further includes an oxidant source and a gas communication passage, the gas communication passage communicates with an intake passage and an exhaust passage of the combustion chamber, and an exhaust gas discharge port is disposed on the exhaust passage, Providing an exhaust gas discharge control valve at the exhaust gas discharge outlet, wherein the oxidant source is connected to the combustion chamber via the oxidant introduction control mechanism or directly through the oxidant introduction control mechanism and the combustion The chamber is connected to communicate, and the oxidant introduction control means, the fuel introduction control means, and the expansion agent introduction control means are controlled by a combustion control means.
在所述气体连通通道上设气体吸热低品位热源加热器。  A gas-absorbing low-grade heat source heater is disposed on the gas communication passage.
在所述气体连通通道上和 /或在所述进气道上和 /或在所述排气道上设气 体放热环境冷却器。  A gas exothermic ambient cooler is provided on the gas communication passage and/or on the intake passage and/or on the exhaust passage.
在所述燃烧室的排气道处设气液分离器,所述膨胀剂源设为所述气液分离 器的液体出口, 所述气液分离器内的液体作为所述膨胀剂使用。  A gas-liquid separator is provided at an exhaust passage of the combustion chamber, the expansion agent source is a liquid outlet of the gas-liquid separator, and a liquid in the gas-liquid separator is used as the expansion agent.
所述膨胀剂源内的膨胀剂设为气体液化物。  The expansion agent in the source of the expansion agent is set as a gas liquefied material.
所述燃料源内的燃料设为乙醇, 所述膨胀剂源内的膨胀剂设为水, 所述燃 料源和所述膨胀剂源设为同一个乙醇水溶液储罐。  The fuel in the fuel source is set to ethanol, the expansion agent in the expansion agent source is set to water, and the fuel source and the expansion agent source are set to be the same aqueous ethanol storage tank.
所述燃烧室设为绝热燃烧室。  The combustion chamber is configured as an adiabatic combustion chamber.
一种提高所述小温升低熵混燃发动机效率和环保性的方法, 在所述燃烧室 设为所述活塞式发动机燃烧室的结构中调整发动机的压縮比使压縮冲程完了 燃烧前的被压縮气体的温度在 1800K的正负 200K的范围内, 在所述燃烧室设 为所述轮机燃烧室的结构中调整压气机和动力涡轮的流量使所述轮机燃烧 ^ 内燃烧前气体的温度在 1800K的正负 200K的范围内; 调整导入所述燃烧室内 的所述膨胀剂源内的膨胀剂的量和导入所述燃烧室内的所述燃料源内的燃料 的量,使导入所述燃烧室的所述燃料源内的燃料燃烧所产生的热量的全部或近 乎全部在所述燃烧室内被已导入所述燃烧室内的所述膨胀剂源内的膨胀剂吸 收; 调整燃料在所述燃烧室内燃烧后所述燃烧室内的气体温度最高值在有害化 合物 NOx生成温度以下以提高发动机的环保性。 A method for improving the efficiency and environmental protection of the small temperature rise and low entropy co-firing engine, adjusting a compression ratio of the engine in a structure in which the combustion chamber is set as the combustion chamber of the piston engine, so that the compression stroke is completed before combustion The temperature of the compressed gas is in the range of plus or minus 200K of 1800K, and the flow rate of the compressor and the power turbine is adjusted in the structure in which the combustion chamber is set to the turbine combustion chamber to burn the turbine. The temperature of the pre-combustion gas is in the range of plus or minus 200 K of 1800 K; adjusting the amount of the expansion agent introduced into the expansion agent source in the combustion chamber and the amount of fuel introduced into the combustion source in the combustion chamber so that All or nearly all of the heat generated by the combustion of the fuel introduced into the fuel source of the combustion chamber is absorbed in the combustion chamber by the expansion agent introduced into the expansion agent source in the combustion chamber; adjusting the fuel in the The maximum gas temperature in the combustion chamber after combustion in the combustion chamber is below the harmful compound NOx formation temperature to improve the environmental friendliness of the engine.
一种提高所述小温升低熵混燃发动机效率和环保性的方法, 调整导入所述 燃烧室内的所述膨胀剂源内的膨胀剂的量和导入所述燃烧室内的所述燃料源 内的燃料的量,使导入所述燃烧室的所述燃料源内的燃料燃烧所产生的热量的 全部或近乎全部在所述燃烧室内被已导入所述燃烧室内的所述膨胀剂源内的 膨胀剂吸收; 燃料在所述燃烧室燃烧前后所述燃烧室内的温度基本维持不变压 力增加, 以提高发动机的效率。  A method for improving the efficiency and environmental friendliness of the small temperature rise and low entropy co-firing engine, adjusting an amount of expansion agent introduced into the expansion agent source in the combustion chamber and fuel introduced into the fuel source in the combustion chamber An amount such that all or nearly all of the heat generated by the combustion of the fuel in the fuel source introduced into the combustion chamber is absorbed in the combustion chamber by the expansion agent introduced into the expansion agent source in the combustion chamber; The temperature in the combustion chamber is substantially maintained at a constant pressure increase before and after combustion of the combustion chamber to increase the efficiency of the engine.
一种提高所述小温升低熵混燃发动机效率和环保性的方法,在所述燃烧室 设为所述活塞式发动机燃烧室的结构中调整发动机的压縮比使压縮冲程完了 燃烧前的被压縮气体的温度在 1000K以上,在所述燃烧室设为所述轮机燃烧室 的结构中调整压气机和动力涡轮的体积流量比使所述轮机燃烧室内燃烧前气 体的温度在 1000K以上。  A method for improving the efficiency and environmental protection of the small temperature rise and low entropy co-firing engine, adjusting a compression ratio of the engine in a structure in which the combustion chamber is set as the combustion chamber of the piston engine, so that the compression stroke is completed before combustion The temperature of the compressed gas is 1000 K or more, and the volume flow ratio of the compressor and the power turbine is adjusted in the structure in which the combustion chamber is set to the turbine combustion chamber, so that the temperature of the gas before combustion in the combustion chamber of the turbine is 1000 K or more. .
一种提高所述小温升低熵混燃发动机效率和环保性的方法, 调整导入所述 燃烧室内的所述膨胀剂源内的膨胀剂的量和导入所述燃烧室内的所述燃料源 内的燃料的量,使导入所述燃烧室的所述燃料源内的燃料燃烧所产生的热量的 5%以上在所述燃烧室内被已导入所述燃烧室内的所述膨胀剂源内的膨胀剂吸 收。  A method for improving the efficiency and environmental friendliness of the small temperature rise and low entropy co-firing engine, adjusting an amount of expansion agent introduced into the expansion agent source in the combustion chamber and fuel introduced into the fuel source in the combustion chamber The amount of 5% or more of the heat generated by the combustion of the fuel in the fuel source introduced into the combustion chamber is absorbed in the combustion chamber by the expansion agent introduced into the expansion agent source in the combustion chamber.
一种提高所述小温升低熵混燃发动机效率和环保性的方法, 调整即将开始 作功的气体工质的温度到 2000K以下, 调整即将开始作功的气体工质的压力到 1 5 Pa以上, 使即将开始作功的气体工质的温度和压力符合类绝热关系。  A method for improving the efficiency and environmental protection of the small temperature rise and low entropy co-combustion engine, adjusting the temperature of the gas working medium to be started to work below 2000K, adjusting the pressure of the gas working medium to be started to work to 15 Pa Above, the temperature and pressure of the gaseous working fluid that is about to start work are in accordance with the adiabatic relationship.
本发明中, 在所述燃烧室设为所述活塞式发动机燃烧室的结构中, 所述活 塞式发动机燃烧室的承压能力大于等于 4MPa、 4. 5MPa、 5MPa、 5. 5MPa、 6MPa、 6. 5WPa、 7MPa、 7. 5MPa、 8MPa、 8. 5MPa、 9MPa、 9. 5MPa、 10MPa、 10. 5MPa、 1 1 MPa、 11.5Pa、 12MPa、 12.5MPa、 13MPa、 13.5 Pa 14MPa、 14.5MPa、 15MPa、 15.5MPa、 16MPa、 16.5MPa、 17MPa、 17.5 Pa> 18MPa、 18.5MPa、 19MPa、 19.5 Pa 20MPa、 22MPa、 24MPa、 26MPa、 28MPa、 30MPa、 32MPa、 34MPa、 36MPa、 38MPa或大于 等于 40MPa, 即调整发动机的压縮比使压縮冲程完了时的被压縮气体的压力大 于等于 4MPa、 4.5MPa、 5MPa、 5.5MPa、 6MPa、 6.5MPa、 7MPa、 7.5MPa、 8MPa、 8.5MPa、 9MPa 9.5MPa、 10MPa、 10.5MPa、 11MPa、 11.5Pa、 12MPa、 12.5 Pa 13MPa、 13.5MPa、 14MPa、 14.5MPa、 15MPa、 15.5MPa、 16MPa、 16.5MPa、 17MPa、 17.5MPa 18MPa、 18.5MPa、 19MPa、 19.5MPa、 20MPa、 22MPa、 24MPa、 26MPa、 28 Pa 30MPa、 32MPa、 34MPa、 36MPa、 38MPa或大于等于 40MPa; 在所述燃烧 室设为所述轮机燃烧室的结构中, 所述轮机燃烧室的承压能力大于等于 2MPa、 2.5MPa、 3MPa、 3.5MPa、 4MPa、 4.5MPa、 5MPa、 5.5MPa、 6MPa、 6.5 Pa 7MPa、 7.5MPa、 8MPa、 8.5MPa、 9MPa、 9.5MPa、 10MPa、 10.5MPa、 11MPa、 11.5Pa、 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、 22MPa、 24MPa、 26MPa、 28MPa、 30MPa、 32MPa、 34MPa、 36MPa、 38MPa或大于等于 40MPa, 即调整压气机和动力涡轮的流量使所述轮机燃烧室内的压力大于等于 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、 11MPa、 11.5Pa、 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、 22MPa、 24MPa、 26MPa、 28MPa、 30MPa、 32MPa 34MPa、 36MPa、 38MPa或大于等于 40MPa。 In the present invention, in the structure in which the combustion chamber is configured as the piston engine combustion chamber, the pressure capacity of the piston engine combustion chamber is greater than or equal to 4 MPa, 4. 5 MPa, 5 MPa, 5. 5 MPa, 6 MPa, 6 5WPa, 7MPa, 7. 5MPa, 8MPa, 8. 5MPa, 9MPa, 9. 5MPa, 10MPa, 10. 5MPa, 1 1 MPa, 11.5Pa, 12MPa, 12.5MPa, 13MPa, 13.5 Pa 14MPa, 14.5MPa, 15MPa, 15.5MPa, 16MPa, 16.5MPa, 17MPa, 17.5 Pa> 18MPa, 18.5MPa, 19MPa, 19.5 Pa 20MPa, 22MPa, 24MPa, 26MPa, 28MPa 30MPa, 32MPa, 34MPa, 36MPa, 38MPa or 40MPa or more, that is, the compression ratio of the engine is adjusted so that the pressure of the compressed gas when the compression stroke is completed is 4 MPa, 4.5 MPa, 5 MPa, 5.5 MPa, 6 MPa, 6.5. MPa, 7MPa, 7.5MPa, 8MPa, 8.5MPa, 9MPa 9.5MPa, 10MPa, 10.5MPa, 11MPa, 11.5Pa, 12MPa, 12.5 Pa 13MPa, 13.5MPa, 14MPa, 14.5MPa, 15MPa, 15.5MPa, 16MPa, 16.5MPa, 17MPa, 17.5MPa 18MPa, 18.5MPa, 19MPa, 19.5MPa, 20MPa, 22MPa, 24MPa, 26MPa, 28 Pa 30MPa, 32MPa, 34MPa, 36MPa, 38MPa or 40MPa or more; In the structure, the pressure capacity of the turbine combustion chamber is greater than or equal to 2 MPa, 2.5 MPa, 3 MPa, 3.5 MPa, 4 MPa, 4.5 MPa, 5 MPa, 5.5 MPa, 6 MPa, 6.5 Pa 7 MPa, 7.5 MPa, 8 MPa, 8.5 MPa, 9MPa, 9.5MPa, 10MPa, 10.5MPa, 11MPa, 11.5Pa, 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, 22MPa, 24MPa, 26MPa, 28MPa, 30MPa, 32MPa, 34MPa, 36MPa, 38MPa or 40MPa or more, that is, adjusting the flow rate of the compressor and the power turbine to make the pressure in the combustion chamber of the turbine greater than or equal to 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, 11MPa, 11.5Pa, 12MPa, 12.5 MPa, 13MPa, 13.5MPa, 14MPa, 14.5MPa, 15MPa, 15.5MPa, 16MPa, 16.5MPa, 17MPa, 17.5MPa, 18MPa, 18.5MPa, 19MPa, 19.5MPa, 20MPa, 22MPa, 24MPa, 26MPa, 28MPa, 30MPa, 32MPa 34 MPa, 36 MPa, 38 MPa or 40 MPa or more.
本发明中, 调整导入所述燃烧室内的所述膨胀剂源内的膨胀剂的量和导入 所述燃烧室内的所述燃料源内的燃料的量,使导入所述燃烧室的所述燃料源内 的燃料燃烧所产生的热量的 6%以上、 7%以上、 8%以上、 9%以上、 10%以上、 11% 以上、 12%以上、 13%以上、 14%以上、 15%以上、 16%以上、 17%以上、 18%以上、 19%以上、 20%以上、 21%以上、 22%以上、 23%以上、 24%以上、 25%以上、 30%以 上、 35%以上、 40%以上、 45%以上、 50%以上、 55%以上、 60%以上、 65%以上、 70%以上、 75%以上、 80%以上、 85%以上、 90%以上、 95%以上、 或 100%在所述燃 烧室内被已导入所述燃烧室内的所述膨胀剂源内的膨胀剂吸收。 In the present invention, the amount of the expansion agent introduced into the expansion agent source in the combustion chamber and the amount of fuel introduced into the combustion source in the combustion chamber are adjusted to cause fuel introduced into the fuel source of the combustion chamber 6% or more, 7% or more, 8% or more, 9% or more, 10% or more, 11% or more, 12% or more, 13% or more, 14% or more, 15% or more, 16% or more of the heat generated by combustion, 17% or more, 18% or more, 19% or more, 20% or more, 21% or more, 22% or more, 23% or more, 24% or more, 25% or more, 30% or more, 35% or more, 40% or more, 45% Above, 50% or more, 55% or more, 60% or more, 65% or more, 70% or more, 75% or more, 80% or more, 85% or more, 90% or more, 95% or more, or 100% in the burning The cooking chamber is absorbed by the expanding agent introduced into the expansion agent source in the combustion chamber.
本发明中, 在所述燃烧室设为所述活塞式发动机燃烧室的结构中调整发动 机的压縮比使压縮冲程完了燃烧前的被压縮气体的温度在 1000K以上、 1300K 以上、 1500K以上、 1800K以上、 2000K以上、 2300K以上、 2500K以上、 2800K 以上、 3000K以上、 3200K以上或 3500K以上, 在所述燃烧室设为所述轮机燃 烧室的结构中调整压气机和动力涡轮的体积流量比使所述轮机燃烧室内燃烧 前气体的温度在 1000K以上、 1300K以上、 1500K以上、 1800K以上、 2000K以 上、 2300K以上、 2500K以上、 2800K以上、 3000K以上、 3200K以上或 3500K 以上。  In the present invention, in the configuration in which the combustion chamber is a piston engine combustion chamber, the compression ratio of the engine is adjusted so that the compression stroke is completed. The temperature of the compressed gas before combustion is 1000 K or more, 1300 K or more, and 1500 K or more. 1800K or more, 2000K or more, 2300K or more, 2500K or more, 2800K or more, 3000K or more, 3200K or more, or 3500K or more, adjusting the volumetric flow ratio of the compressor and the power turbine in the structure in which the combustion chamber is set to the turbine combustion chamber The temperature of the gas before combustion in the turbine combustion chamber is 1000 K or more, 1300 K or more, 1500 K or more, 1800 K or more, 2000 K or more, 2300 K or more, 2500 K or more, 2800 K or more, 3000 K or more, 3200 K or more, or 3500 K or more.
本发明的原理是, 通过提高发动机的压縮比, 达到提高压縮冲程或压縮过 程完了时的燃烧室内的气体的温度和压力, 调整进入所述燃烧室的燃料和膨胀 剂的量,通过使燃料燃烧放出热量的一定值在所述燃烧室室内被所述膨胀剂吸 收形成工质摩尔数增加进而增加工质压力而温度变化量小或保持不变的工作 循环模式代替传统内燃机燃烧室内靠对气体工质升温获得压力增加的工作循 环模式, 具体说来是: 对活塞式发动机来说, 通过提高活塞式内燃机的压縮比 使燃烧室燃烧前的气体压力和温度均超过传统活塞式内燃机的气体压力和温 度,控制燃料和膨胀剂进入所述燃烧室的量以及膨胀剂进入所述燃烧室时的温 度使尽可能多的燃料燃烧放出的热量被所述膨胀剂吸收, 大幅度提高燃烧室内 的压力, 而温度的变化量小或保持不变; 对轮机来说, 通过调整压气机和涡轮 的体积流量比使轮机燃烧室燃烧前的气体压力和温度均超过传统轮机燃烧室 的气体压力和温度,控制燃料和膨胀剂进入所述燃烧室的量以及膨胀剂进入所 述燃烧室时的温度使尽可能多的燃料燃烧放出的热量被所述膨胀剂吸收, 大幅 度提高燃烧室内的压力, 而温度的变化量小或保持不变; 进而大幅度提高发动 机的效率和环保性。  The principle of the present invention is to increase the amount of fuel and expansion agent entering the combustion chamber by increasing the compression ratio of the engine to increase the temperature and pressure of the gas in the combustion chamber when the compression stroke or compression process is completed. A certain value of the calorific value of the combustion of the fuel in the combustion chamber is absorbed by the expansion agent to form an increase in the number of moles of the working medium, thereby increasing the working medium pressure and the temperature change amount is small or constant, and replacing the combustion chamber of the conventional internal combustion engine The working cycle mode for increasing the pressure of the gas working fluid is specifically: For the piston engine, the gas pressure and temperature before combustion of the combustion chamber exceed the conventional piston internal combustion engine by increasing the compression ratio of the piston internal combustion engine. Gas pressure and temperature, controlling the amount of fuel and expansion agent entering the combustion chamber and the temperature at which the expansion agent enters the combustion chamber so that as much of the heat released by the combustion of the fuel is absorbed by the expansion agent, greatly increasing combustion Indoor pressure, while temperature changes are small or constant; for turbines, Adjusting the volumetric flow ratio of the compressor and the turbine such that the gas pressure and temperature before combustion of the turbine combustor exceeds the gas pressure and temperature of the conventional turbine combustion chamber, controlling the amount of fuel and expansion agent entering the combustion chamber, and the expansion agent entering the The temperature at the combustion chamber causes the heat released by the combustion of as much fuel as possible to be absorbed by the expansion agent, greatly increasing the pressure in the combustion chamber, and the amount of temperature change is small or constant; thereby greatly improving the efficiency and environmental protection of the engine. Sex.
本发明中, 燃料燃烧所放出的热量的主要目的是被所述膨胀剂吸收, 而不 被用于加热升温气体工质 (特别是燃烧前的气体工质)。  In the present invention, the main purpose of the heat released by the combustion of the fuel is to be absorbed by the expansion agent, and is not used to heat the warming gas working medium (especially the gas working medium before combustion).
本发明中, 所谓的活塞式发动机燃烧室可以是四冲程活塞发动机燃烧室, 也可以是二冲程活塞发动机燃烧室, 转子活塞发动机的燃烧室, 还可以是吸气 压縮冲程和作功排气冲程由两套机构构成的活塞发动机的燃烧室。 In the present invention, the so-called piston engine combustion chamber may be a four-stroke piston engine combustion chamber, or a two-stroke piston engine combustion chamber, a combustion chamber of the rotor piston engine, or may be inhaled. The compression stroke and the work exhaust stroke are combustion chambers of a piston engine composed of two sets of mechanisms.
本发明中, 所谓的低温热源也可称之为冷源, 与有些文献中的所谓冷源等 价。  In the present invention, the so-called low temperature heat source can also be referred to as a cold source, and is equivalent to a so-called cold source in some literatures.
本发明中, 所述膨胀剂吸热热交换器可以设为压縮过程(冲程) 中的被压 縮气体的冷却器, 也就是利用膨胀剂吸收压縮过程中被压縮气体的热量, 以使 被压縮气体温度降低。  In the present invention, the expansion agent heat absorption heat exchanger may be set as a cooler of the compressed gas in the compression process (stroke), that is, the expansion agent is used to absorb the heat of the compressed gas during the compression process, The temperature of the compressed gas is lowered.
本发明中, 所谓 "高温热源下工质的状态 (温度和压力)"是指从高温热 源吸热完毕后的工质的状态, 即工质的温度和压力; 所谓的高温热源下工质的 状态可能与高温热源的状态一致, 也可能与高温热源的状态不一致。  In the present invention, the state of the working medium (temperature and pressure) under the high-temperature heat source refers to the state of the working fluid after the endothermic heat source is completed, that is, the temperature and pressure of the working medium; the so-called high-temperature heat source The state may be consistent with the state of the high temperature heat source or with the state of the high temperature heat source.
本发明所公开的小温升低熵混燃发动机中, 所谓 "热量被膨胀剂吸收"是 指热量被用于加热升温膨胀剂、 气化膨胀剂、 临界化膨胀剂和 /或过热膨胀剂; 所谓临界化膨胀剂是指使膨胀剂处于临界状态、 超临界状态、 超超临界状态或 更高的温度压力状态。  In the small temperature rise and low entropy co-firing engine disclosed in the present invention, the term "heat is absorbed by the expansion agent" means that the heat is used to heat the temperature expansion agent, the gasification expansion agent, the critical expansion agent and/or the superheat expansion agent; The critically-expanded expansion agent refers to a state in which the expansion agent is in a critical state, a supercritical state, an ultra-supercritical state, or a higher temperature and pressure state.
本发明中, 所谓的 "温度变化量小或保持不变"是指燃料燃烧后热量全部 或近乎全部被所述膨胀剂吸收, 燃烧室内的气体温度在燃烧前后变化量小或保 持不变, 而且近乎没有过剩温度(所谓过剩温度是指按照绝热膨胀的关系为了 达到某一终点状态, 在起点状态下工质的实际温度高于理论上所需要的温度); 依据这一工作模式, 在本发明所公开的小温升低熵混燃发动机中, 在向经压縮 冲程 (过程) 被压縮的气体工质内导入燃料和膨胀剂并发生燃烧化学反应后, 所述燃烧室内的气体压力接近、 等于或大于由公式 p = cr^所确定的压力值 In the present invention, the so-called "small or constant temperature change" means that all or nearly all of the heat of the fuel is absorbed by the expansion agent, and the temperature of the gas in the combustion chamber is small or constant before and after combustion, and There is almost no excess temperature (the so-called excess temperature refers to the relationship of adiabatic expansion in order to reach a certain end state, the actual temperature of the working medium is higher than the theoretically required temperature in the starting state); according to this working mode, in the present invention In the disclosed small temperature rise and low entropy co-firing engine, after introducing fuel and expansion agent into a gas working medium compressed by a compression stroke (process) and generating a combustion chemical reaction, the gas pressure in the combustion chamber is close to , equal to or greater than the pressure value determined by the formula p = cr^
(其中, C是常量和工质的起始状态以及热力学物性有关, P是燃烧后的工质 压力, Γ是燃烧后的工质温度, 为绝热压縮指数, 空气的绝热压縮指数为 1 . 4), 换句话说, 所述燃烧室内的气体的温度和压力的关系基本遵循以压縮冲 程开始时的状态为起点, 以公式 P = C7^i所确定的温度和压力的关系, 或者压 力大于由公式 p = cr^所确定的压力值; 这就使得膨胀作功后的工质温度要大 幅度低于传统内燃机的排气温度, 显而易见, 效率的提高程度是相当大的。 (where C is constant and the initial state of the working fluid and thermodynamic properties, P is the working fluid pressure after combustion, Γ is the working temperature after combustion, is the adiabatic compression index, and the adiabatic compression index of air In the case of 1.4), in other words, the relationship between the temperature and the pressure of the gas in the combustion chamber basically follows the relationship between the temperature and the pressure determined by the formula P = C7^i starting from the state at the beginning of the compression stroke. , or the pressure is greater than the pressure value determined by the formula p = cr^; this makes the temperature of the working fluid after the expansion work much lower than the exhaust temperature of the conventional internal combustion engine. Obviously, the degree of improvement of the efficiency is considerable.
本发明所公开的小温升低熵混燃发动机中, 燃料、 氧化剂 (例如被压縮的 空气或被压縮的含氧气体)和膨胀剂中的任何两个可以事先混合后与第三个混 合, 燃烧反应可以先发生在氧化剂和燃料之间再与膨胀剂混合, 也可以发生在 三者混合时或三者混合后; 可以在燃烧室内建立核心燃烧区, 在该核心燃烧区 内氧化剂和燃料直接燃烧后再与处于燃烧核心区与燃烧室壁之间的膨胀剂混 合,这样可以利用膨胀剂将燃料和氧化剂直接燃烧形成的过高温度的火焰与燃 烧室壁隔离, 从而减少燃烧室壁的热负荷。 In the small temperature rise and low entropy co-firing engine disclosed in the present invention, any two of the fuel, the oxidant (for example, compressed air or compressed oxygen-containing gas) and the expansion agent may be mixed beforehand and the third Mixed The combustion reaction may first occur between the oxidant and the fuel and then mixed with the expansion agent, or may occur when the three are mixed or after the three are mixed; a core combustion zone may be established in the combustion chamber, and the oxidant in the core combustion zone The fuel is directly combusted and then mixed with the expansion agent between the combustion core zone and the combustion chamber wall, so that the excessive temperature flame formed by direct combustion of the fuel and the oxidant can be separated from the combustion chamber wall by the expansion agent, thereby reducing the combustion chamber wall. The heat load.
本发明所谓的膨胀剂是指不参与燃烧化学反应起吸热和调整作功工质摩 尔数并膨胀作功的工质, 可以是气体、 液体、 临界态物质、 气体液化物, 例如 水蒸汽、 二氧化碳、 氦气、 氮气、 液态二氧化碳、 液氦、 液氮或液化空气等。  The so-called expansion agent of the present invention refers to a working medium which does not participate in the combustion chemical reaction and absorbs heat and adjusts the number of moles of working medium and expands work. It may be a gas, a liquid, a critical substance, a gas liquefaction, such as water vapor, Carbon dioxide, helium, nitrogen, liquid carbon dioxide, liquid helium, liquid nitrogen or liquefied air.
本发明中所谓的气体液化物是指被液化的气体, 如液氮、 液体二氧化碳、 液氦或液化空气等。  The gas liquefied matter in the present invention means a gas to be liquefied, such as liquid nitrogen, liquid carbon dioxide, liquid helium or liquefied air.
本发明所谓的氧化剂是指纯氧或其他成分在热功转换过程中不产生有害 化合物的含氧气体, 如液化空气、 过氧化氢或过氧化氢水溶液等。 所谓氧化剂 源是指一切可以提供氧化剂的装置、 系统或容器, 如商用氧源(即高压储氧罐 或液化氧罐)和在热动力系统内由现场制氧系统提供的氧(如膜分离制氧系统) 等。  The term "oxidant" as used in the present invention means an oxygen-containing gas such as liquefied air, hydrogen peroxide or an aqueous hydrogen peroxide solution in which pure oxygen or other components do not generate harmful compounds during thermal power conversion. By oxidant source is meant any device, system or vessel that can provide an oxidant, such as a commercial oxygen source (ie a high pressure oxygen storage tank or a liquefied oxygen tank) and oxygen supplied by an on-site oxygen system in a thermodynamic system (eg membrane separation) Oxygen system) and so on.
本发明所谓的气体吸热低品位热源加热器是指以低品位热源 (如排气余 热、 冷却系统的余热等)为热源对气体工质进行加热的装置; 所谓气体放热环 境冷却器是指通过将气体工质的热量排放到环境中而对气体工质进行冷却的 装置; 所谓燃烧控制装置是指通过控制燃料的量、 膨胀剂的量和 /或氧化剂的 量以及燃料、膨胀剂和氧化剂导入的相位来控制燃烧的装置; 所谓气液分离器 是指将气体和液体进行分离的装置。  The so-called gas-absorbing low-grade heat source heater of the present invention refers to a device for heating a gas working medium by using a low-grade heat source (such as exhaust heat, exhaust heat of a cooling system, etc.) as a heat source; the so-called gas heat-dissipating environment cooler means A device for cooling a gaseous working fluid by discharging heat of a gaseous working fluid into the environment; a so-called combustion control device means controlling the amount of fuel, the amount of expanding agent, and/or the amount of oxidizing agent, and the fuel, the expanding agent, and the oxidizing agent. The introduced phase controls the device for combustion; the so-called gas-liquid separator refers to a device that separates gas and liquid.
本发明所谓的导入控制机构是指按照热动力系统燃烧室燃烧条件的要求 将原工质 (燃料、 膨胀剂和 /或氧化剂) 供送给燃烧室的系统, 这一系统包括 阀、 泵和 /或传感器等。  The so-called introduction control mechanism of the present invention refers to a system for supplying the original working medium (fuel, expansion agent and/or oxidant) to the combustion chamber according to the requirements of the combustion conditions of the combustion chamber of the thermodynamic system, the system including the valve, the pump and/or Or sensor, etc.
本发明中所谓的膨胀剂吸热热交换器是指以环境的热量或所述小温升低 熵混燃发动机的余热(如排气余热、 冷却系统的余热) 为热源的膨胀剂可以吸 热的热交换器。  The so-called expander heat absorbing heat exchanger in the present invention refers to an expansion agent capable of absorbing heat by using ambient heat or the small temperature rise and low entropy co-firing engine residual heat (such as exhaust heat and residual heat of the cooling system) as a heat source. Heat exchanger.
本发明中所谓的环保温度限值是指不产生有害污染物的最高温度,如不产 生氮氧化物的环保温度限值为 1800K等; 所谓材料温度限值是指材料所能承受 白勺最 1¾温度。 The so-called environmentally friendly temperature limit in the present invention refers to the highest temperature that does not produce harmful pollutants, such as not producing The environmental temperature limit for raw nitrogen oxides is 1800K, etc.; the so-called material temperature limit refers to the maximum temperature that the material can withstand.
本发明中的所述膨胀剂可以在所述小温升低熵混燃发动机中循环使用。 本发明所谓的燃料是指一切化学燃烧意义上能和氧发生剧烈的氧化还原 反应的物质, 可以是气体、液体或固体, 在这里主要包括汽油、柴油、 天然气、 氢气和煤气及流化燃料、 液化燃料或粉末状的固体燃料等。所谓的液化燃料是 指被液化的在常温常压状态下为气态的燃料。  The expansion agent of the present invention can be recycled in the small temperature rise low entropy co-firing engine. The so-called fuel in the present invention refers to a substance which can undergo a vigorous redox reaction with oxygen in the sense of chemical combustion, and may be a gas, a liquid or a solid, and mainly includes gasoline, diesel, natural gas, hydrogen and gas, and fluidized fuel, Liquefied fuel or powdered solid fuel, etc. The so-called liquefied fuel refers to a fuel that is liquefied and is in a gaseous state at a normal temperature and a normal pressure state.
本发明所公开的小温升低熵混燃发动机, 可使用碳氢化合物或碳氢氧化合 物作燃料, 例如乙醇或乙醇水溶液, 使用乙醇水溶液来代替原来的燃料和膨胀 剂, 不但可以防冻, 还可以只用一个乙醇水溶液储罐来代替原来的燃料储罐和 膨胀剂储罐,并且通过调整乙醇水溶液的浓度来改变燃料和膨胀剂所需要的比 例。 在必要的时候, 可以用乙醇、 水和碳氢化合物的混合溶液来代替本发明中 的燃料和膨胀剂,调节其浓度以满足本发明所公开的小温升低熵混燃发动机的 要求。 本发明所公开的小温升低熵混燃发动机中, 可以用过氧化氢水溶液代替 氧化剂和膨胀剂,通过调整过氧化氢水溶液的浓度实现调整氧化剂和膨胀剂的 比例, 而且可以用一个过氧化氢水溶液储罐代替氧化剂储罐和膨胀剂储罐。  The small temperature rising low entropy co-firing engine disclosed by the invention can use hydrocarbon or carbon oxyhydroxide as fuel, for example, ethanol or ethanol aqueous solution, and use ethanol aqueous solution instead of original fuel and expansion agent, not only can prevent freezing, but also It is possible to replace the original fuel storage tank and the expansion agent storage tank with only one aqueous ethanol storage tank, and to change the ratio of the fuel and the expansion agent by adjusting the concentration of the aqueous ethanol solution. When necessary, a mixed solution of ethanol, water and hydrocarbon may be used in place of the fuel and expansion agent of the present invention, and the concentration thereof may be adjusted to meet the requirements of the small temperature rise and low entropy co-firing engine disclosed in the present invention. In the small temperature rising low entropy co-firing engine disclosed in the present invention, an aqueous hydrogen peroxide solution can be used instead of the oxidizing agent and the expanding agent, and the ratio of the oxidizing agent and the expanding agent can be adjusted by adjusting the concentration of the aqueous hydrogen peroxide solution, and a peroxidation can be used. The aqueous hydrogen storage tank replaces the oxidant storage tank and the expansion agent storage tank.
本发明中, 在某些技术方案中, 作功工质温度可以达到数千度甚至更高, 作功工质的压力可以达到数百个大气压甚至更高。  In the present invention, in some technical solutions, the working fluid temperature can reach several thousand degrees or even higher, and the working fluid pressure can reach several hundred atmospheres or even higher.
本发明所公开的小温升低熵混燃发动机中, 通过调整燃烧室的气体温度和 压力, 可以调整膨胀作功后的工质的温度和压力可使当作功膨胀到所设定膨胀 压力时, 其工质温度降至相当低的水平, 例如接近环境温度、 低于环境温度或 大幅度低于环境温度。  In the small temperature rise and low entropy co-firing engine disclosed in the present invention, by adjusting the gas temperature and pressure of the combustion chamber, the temperature and pressure of the working fluid after the expansion work can be adjusted to expand the work to the set expansion pressure. At the time, the working temperature drops to a relatively low level, such as near ambient temperature, below ambient temperature, or substantially below ambient temperature.
本发明中所谓的轮机是指燃气轮机、喷气式发动机等利用燃气推动涡轮作 功的机构; 所谓活塞式发动机包括活塞式内燃机、 转子活塞式内燃机等。  The term "engine" as used in the present invention refers to a mechanism that uses gas to drive a turbine to work, such as a gas turbine or a jet engine; the piston engine includes a piston type internal combustion engine, a rotor piston type internal combustion engine, and the like.
本发明所公开的小温升低熵混燃发动机中, 由于燃烧室内的温度可以设置 到氮氧化物生成温度以下, 所以即便使用液氮作为所述膨胀剂, 也不会产生氮 氧化物 (N0J; 液氮可以以液态形式导入燃烧室, 也可以以临界状态导入燃烧 室, 还可以以超高压气体形式导入燃烧室。 所谓超高压是指气体的压力不仅高 于导入液氮时的所述燃烧室内的气体压力, 还要高于由公式 P = C7^i所确定的 压力值; 本发明所公开的小温升低熵混燃发动机中, 液氮以气体的形式导入所 述燃烧室时,氮气的压力比所述燃烧室内的气体压力高 2MPa、3MPa、4MPa、5MPa、 6MPa、 7MPa、 8MPa、 9MPa、 10MPa 1 1 MPa、 1 2MPa、 1 3MPa、 14MPa、 1 5MPa、 1 6MPa、 1 7MPa、 1 8 Pa 1 9MPa或高 20MPa。 In the small temperature rise and low entropy co-firing engine disclosed in the present invention, since the temperature in the combustion chamber can be set below the nitrogen oxide formation temperature, even if liquid nitrogen is used as the expansion agent, nitrogen oxides are not generated (N0J). Liquid nitrogen can be introduced into the combustion chamber in liquid form, or can be introduced into the combustion chamber in a critical state, or can be introduced into the combustion chamber in the form of an ultra-high pressure gas. The so-called ultra-high pressure means that the pressure of the gas is not only high. The gas pressure in the combustion chamber when liquid nitrogen is introduced is higher than the pressure value determined by the formula P = C7^i; in the small temperature rise and low entropy co-firing engine disclosed in the present invention, liquid nitrogen is gas When the form is introduced into the combustion chamber, the pressure of nitrogen gas is higher than the gas pressure in the combustion chamber by 2 MPa, 3 MPa, 4 MPa, 5 MPa, 6 MPa, 7 MPa, 8 MPa, 9 MPa, 10 MPa 1 1 MPa, 1 2 MPa, 13 MPa, 14 MPa, 1 5MPa, 16 6MPa, 17 7MPa, 1 8 Pa 1 9MPa or 20MPa high.
本发明的有益效果如下: The beneficial effects of the present invention are as follows:
本发明所公开的小温升低熵混燃发动机效率高, 环保性好。  The small temperature rising low entropy co-combustion engine disclosed by the invention has high efficiency and good environmental protection.
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;  2 is a schematic structural view of Embodiment 2 of the present invention;
图 3所示的是本发明实施例 3的结构示意图;  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 10的结构示意图。  Figure 10 is a schematic view showing the structure of a tenth embodiment of the present invention.
图 1 1所示的是本发明的 q>0循环示意图;  Figure 1 is a schematic diagram of the q>0 cycle of the present invention;
图 1 2所示的是本发明的 q=0循环示意图;  Figure 12 is a schematic diagram of the q=0 cycle of the present invention;
图 1 3所示的是本发明的 q<0循环示意图;  Figure 13 is a schematic diagram of the q<0 cycle of the present invention;
图 14所示的是压縮力度不同的热机工作示意图;  Figure 14 shows a schematic diagram of the operation of a heat engine with different compression forces;
图 1 5所示的是本发明描述燃烧后气体工质的压力和温度关系符合绝热压 縮过程温度和压力关系的示意图;  Figure 15 is a schematic view showing the relationship between the pressure and temperature of the gaseous working fluid after combustion in accordance with the temperature and pressure of the adiabatic compression process;
图 1 6所示的是本发明描述燃烧后气体工质的压力大于由绝热压縮过程的 压力和温度的关系所确定的压力值的示意图;  Figure 16 is a schematic view showing the pressure value of the gas working fluid after combustion is greater than the pressure value determined by the relationship between the pressure and temperature of the adiabatic compression process;
图 1 7所示的是纵轴为压力坐'标橫轴为温度坐标的压力温度关系图; 图 18所示的是不同 E点出发绝热膨胀作功的温度和压力关系的示意图; 图 1 9所示的是本发明所公开的小温升低熵混燃发动机的循环和传统内燃 机的循环的示功对比图; Figure 17 shows the pressure-temperature relationship of the vertical axis as the pressure-slope horizontal axis as the temperature coordinate; Figure 18 is a schematic diagram showing the temperature-pressure relationship of the adiabatic expansion work at different points E; Figure 19 is a comparison diagram of the cycle of the cycle of the small temperature rise and low entropy co-firing engine disclosed in the present invention and the cycle of the conventional internal combustion engine;
图 20为气体工质的温度 T和压力 P的关系图。  Figure 20 is a graph showing the relationship between the temperature T of the gas working fluid and the pressure P.
图中:  In the picture:
1燃烧室、 2膨胀剂源、 3燃料源、 5氧化剂源、 6压气机、 7动力涡轮、 9 气体连通通道、 10进气道、 1 1排气道、 1 2排气放出口、 13排气放出控制阀、 16氧化剂导入控制机构、 18气体放热环境冷却器、 1 7气体吸热低品位热源加 热器、 20膨胀剂导入控制机构、 30燃料导入控制机构、 101活塞式发动机燃烧 室、 102轮机燃烧室、 1020膨胀剂吸热热交换器、 3020燃烧控制装置、 1 100 气液分离器。  1 combustion chamber, 2 expansion agent source, 3 fuel source, 5 oxidant source, 6 compressor, 7 power turbine, 9 gas communication passage, 10 inlet, 1 1 exhaust, 1 2 exhaust discharge, 13 rows Air release control valve, 16 oxidant introduction control mechanism, 18 gas exothermic environment cooler, 17 7 gas absorption low grade heat source heater, 20 expansion agent introduction control mechanism, 30 fuel introduction control mechanism, 101 piston engine combustion chamber, 102 turbine combustion chamber, 1020 expansion agent heat absorption heat exchanger, 3020 combustion control device, 1 100 gas liquid separator.
具体实施方式 detailed description
实施例 1  Example 1
如图 1所示的小温升低熵混燃发动机, 包括燃烧室, 膨胀剂源 2和燃料源 3, 所述燃烧室设为活塞式发动机燃烧室 101, 所述活塞式发动机燃烧室 101 的承压能力大于等于 4MPa, 所述燃料源 3经燃料导入控制机构 30与所述燃烧 室连通, 所述膨胀剂源 2经膨胀剂导入控制机构 20与所述燃烧室连通, 所述 燃料导入控制机构 30和所述膨胀剂导入控制机构 20受燃烧控制装置 3020控 制实现进入所述燃烧室的所述燃料源 3 内的燃料燃烧所产生的热量的 5%以上 在所述燃烧室内被已导入所述燃烧室内的所述膨胀剂源 2内的膨胀剂吸收; 在 所述燃烧室设为所述活塞式发动机燃烧室 101的结构中调整发动机的压縮比使 压縮冲程完了时的被压縮气体的压力大于传统活塞式发动机压縮冲程完了时 的气体压力, 调整即将开始作功的气体工质的温度到 2000K以下, 调整即将开 始作功的气体工质的压力到 1 5MPa以上,使即将开始作功的气体工质的温度和 压力符合类绝热关系。在所述燃烧室设为所述活塞式发动机燃烧室 101的结构 中调整发动机的压縮比使压縮冲程完了时的被压縮气体的压力大于等于 4MPa ; 在所述燃烧室设为所述活塞式发动机燃烧室 101的结构中调整发动机的压縮比 使压縮冲程完了燃烧前的被压縮气体的温度在 1 800K的正负 200K的范围内, 所述燃料导入控制机构 30和所述膨胀剂导入控制机构 20受燃烧控制装置 3020 控制实现进入所述燃烧室的所述燃料源 3内的燃料燃烧所产生的热量的全部或 近乎全部在所述燃烧室被已导入所述燃烧室内的所述膨胀剂源 2内的膨胀剂吸 收; 燃料在所述燃烧室燃烧后所述燃烧室内的温度最高值在有害化合物 NOx生 成温度以下以提高发动机的环保性; a small temperature rise and low entropy co-firing engine as shown in FIG. 1 , comprising a combustion chamber, an expansion agent source 2 and a fuel source 3, the combustion chamber being set as a piston engine combustion chamber 101, and the piston engine combustion chamber 101 The pressure bearing capacity is greater than or equal to 4 MPa, the fuel source 3 is in communication with the combustion chamber via a fuel introduction control mechanism 30, and the expansion agent source 2 is communicated with the combustion chamber via an expansion agent introduction control mechanism 20, the fuel introduction control The mechanism 30 and the expansion agent introduction control mechanism 20 are controlled by the combustion control device 3020 to realize that more than 5% of the heat generated by the combustion of the fuel in the fuel source 3 entering the combustion chamber has been introduced into the combustion chamber. Absorbing agent in the expansion agent source 2 in the combustion chamber; adjusting the compression ratio of the engine in the structure in which the combustion chamber is set to the piston engine combustion chamber 101 to be compressed when the compression stroke is completed The pressure of the gas is greater than the gas pressure at the end of the compression stroke of the conventional piston engine, and the temperature of the gas working fluid that is about to start work is adjusted to below 2000K, and the gas working fluid that is about to start work is adjusted. 1 5MPa or more to force the gas will begin work as working fluid temperature and pressure in line with the adiabatic relation classes. Adjusting a compression ratio of the engine in a configuration in which the combustion chamber is configured as the piston engine combustion chamber 101 such that a pressure of a compressed gas when the compression stroke is completed is greater than or equal to 4 MPa; In the structure of the piston engine combustion chamber 101, the compression ratio of the engine is adjusted such that the compression stroke is completed, and the temperature of the compressed gas before combustion is in the range of plus or minus 200K of 1 800 K, the fuel introduction control mechanism 30 and the The expansion agent introduction control mechanism 20 is subjected to the combustion control device 3020 Controlling all or nearly all of the heat generated by combustion of the fuel within the fuel source 3 entering the combustion chamber is absorbed by the expansion agent in the expansion agent source 2 that has been introduced into the combustion chamber After the combustion of the combustion chamber, the highest temperature in the combustion chamber is below the harmful compound NOx generation temperature to improve the environmental protection of the engine;
在所述燃烧室设为所述活塞式发动机燃烧室 101的结构中调整发动机的压 縮比使压縮冲程完了燃烧前的被压縮气体的温度在 1000K以上。  In the configuration in which the combustion chamber is set to the piston engine combustion chamber 101, the compression ratio of the engine is adjusted so that the temperature of the compressed gas before the combustion is completed is 1000 K or more.
具体实施时, 可选择地, 调整发动机的压縮比使压縮冲程完了时的被压縮 气体的压力大于等于 4. 5MPa、 5MPa、 5. 5MPa 6MPa、 6. 5 Pa 7MPa、 7. 5MPa、 8MPa、 8. 5MPa、 9MPa、 9, 5MPa、 10 Pa 10. 5MPa、 1 1 MPa、 1 1 · 5Pa、 12 Pa 12. 5MPa、 13MPa、 1 3. 5MPa、 14MPa、 14. 5MPa、 15MPa、 15. 5MPa、 1 6MPa、 1 6. 5MPa、 1 7MPa、 1 7. 5MPa、 18MPa、 18. 5MPa、 1 9MPa、 19. 5MPa、 20MPa、 22MPa、 24MPa、 26MPa、 28MPa、 30MPa、 32MPa、 34MPa、 36MPa、 38MPa或大于等于 40MPa;  5 MPa, 6.5 MPa, 7.5 MPa, 7.5 MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa, MPa 8MPa, 8. 5MPa, 9MPa, 9, 5MPa, 10 Pa 10. 5MPa, 1 1 MPa, 1 1 · 5Pa, 12 Pa 12. 5MPa, 13MPa, 1 3. 5MPa, 14MPa, 14. 5MPa, 15MPa, 15. 5MPa, 16 MPa, 6.5 MPa, 17 MPa, 1.7 MPa, 18 MPa, 18. 5 MPa, 1 9 MPa, 19. 5 MPa, 20 MPa, 22 MPa, 24 MPa, 26 MPa, 28 MPa, 30 MPa, 32 MPa, 34 MPa, 36 MPa, 38 MPa Or greater than or equal to 40 MPa;
所述燃料导入控制机构 30和所述膨胀剂导入控制机构 20受燃烧控制装置 3020控制实现进入所述燃烧室的所述燃料源 3 内的燃料燃烧所产生的热量的 6%以上、 7%以上、 8%以上、 9%以上、 10%以上、 1 1 %以上、 12%以上、 13%以上、 14%以上、 15%以上、 16%以上、 1 7%以上、 18%以上、 1 9%以上、 20%以上、 21 %以 上、 22%以上、 23%以上、 24%以上、 25%以上、 30%以上、 35%以上、 40%以上、 45%以上、 50%以上、 55%以上、 60%以上、 65%以上、 70%以上、 75%以上、 80%以 上、 85%以上、 90%以上、 95%以上、 或 100%在所述燃烧室内被已导入所述燃烧 室内的所述膨胀剂源 2内的膨胀剂吸收;  The fuel introduction control mechanism 30 and the expansion agent introduction control mechanism 20 are controlled by the combustion control device 3020 to control 6% or more and 7% or more of the heat generated by combustion of the fuel in the fuel source 3 entering the combustion chamber. 8% or more, 9% or more, 10% or more, 11% or more, 12% or more, 13% or more, 14% or more, 15% or more, 16% or more, more than 1%, 18% or more, and 9% Above, 20% or more, 21% or more, 22% or more, 23% or more, 24% or more, 25% or more, 30% or more, 35% or more, 40% or more, 45% or more, 50% or more, 55% or more, 60% or more, 65% or more, 70% or more, 75% or more, 80% or more, 85% or more, 90% or more, 95% or more, or 100%, which are introduced into the combustion chamber in the combustion chamber Absorbing agent in the expander source 2 is absorbed;
调整发动机的压縮比使压縮冲程完了燃烧前的被压縮气体的温度在 1300K 以上、 1500K以上、 1800K以上、 2000K以上、 2300K以上、 2500K以上、 2800K 以上、 3000K以上、 3200K以上或 3500K以上。  Adjusting the compression ratio of the engine to complete the compression stroke. The temperature of the compressed gas before combustion is 1300K or more, 1500K or more, 1800K or more, 2000K or more, 2300K or more, 2500K or more, 2800K or more, 3000K or more, 3200K or more, or 3500K or more. .
实施例 2  Example 2
如图 2所示的小温升低熵混燃发动机, 其与实施例 1的区别是: 在所述燃 烧室和所述膨胀剂源 2之间设膨胀剂吸热热交换器 1 020, 使所述膨胀剂源 2 内的膨胀剂在所述膨胀剂吸热热交换器 1020中吸热, 所述燃烧室设为绝热燃 烧室。 实施例 3 a small temperature rise and low entropy co-firing engine as shown in FIG. 2, which differs from Embodiment 1 in that: an expander heat absorption heat exchanger 1 020 is provided between the combustion chamber and the expansion agent source 2, The expansion agent in the expansion agent source 2 absorbs heat in the expansion agent heat absorption heat exchanger 1020, and the combustion chamber is set as an adiabatic combustion chamber. Example 3
如图 3所示的小温升低熵混燃发动机, 其与实施例 1的区别是: 所述膨胀 剂吸热热交换器 1020的热源设为所述小温升低熵混燃发动机的余热。 所述膨 胀剂源 2内的膨胀剂在所述膨胀剂吸热热交换器 1020中吸热达到临界状态、 超临界状态或超超临界状态后再进入所述燃烧室。  The small temperature rise and low entropy co-firing engine shown in FIG. 3 is different from the embodiment 1 in that: the heat source of the expander heat absorption heat exchanger 1020 is set as the waste heat of the small temperature rise and low entropy co-firing engine. . The expansion agent in the expansion agent source 2 enters the combustion chamber after the endothermic state in the expansion agent heat absorption heat exchanger 1020 reaches a critical state, a supercritical state, or an ultra-supercritical state.
具体实施时, 所述燃料源 3内的燃料设为乙醇, 所述膨胀剂源 2内的膨胀 剂设为水, 所述燃料源 3和所述膨胀剂源 2设为同一个乙醇水溶液储罐。  In a specific implementation, the fuel in the fuel source 3 is set as ethanol, the expansion agent in the expansion agent source 2 is set as water, and the fuel source 3 and the expansion agent source 2 are set to be the same ethanol aqueous solution tank. .
实施例 4  Example 4
如图 4所示的小温升低熵混燃发动机, 其与实施例 1的区别是: 所述小温 升低熵混燃发动机还包括氧化剂源 5和气体连通通道 9, 所述气体连通通道 9 连通所述燃烧室的进气道 10和排气道 1 1, 在所述排气道 1 1 上设排气放出口 12, 在所述排气放出口 12处设排气放出控制阀 13, 所述氧化剂源 5经氧化剂 导入控制机构 16再经所述进气道 10与所述燃烧室连通或直接经所述氧化剂导 入控制机构 1 6与所述燃烧室连通, 所述氧化剂导入控制机构 1 6、 所述燃料导 入控制机构 30和所述膨胀剂导入控制机构 20受燃烧控制装置 3020控制。  The small temperature rise and low entropy co-firing engine shown in FIG. 4 is different from the embodiment 1 in that: the small temperature rise and low entropy co-firing engine further includes an oxidant source 5 and a gas communication passage 9, the gas communication passage 9 an intake passage 10 and an exhaust passage 1 connected to the combustion chamber, an exhaust gas discharge port 12 is disposed on the exhaust passage 1 1 , and an exhaust gas discharge control valve 13 is disposed at the exhaust gas discharge port 12 The oxidant source 5 is communicated with the combustion chamber via the oxidant introduction control mechanism 16 and directly communicated with the combustion chamber via the oxidant introduction control mechanism 16. The oxidant introduction control mechanism 16. The fuel introduction control mechanism 30 and the expansion agent introduction control mechanism 20 are controlled by a combustion control device 3020.
实施例 5  Example 5
如图 5所示的小温升低熵混燃发动机, 其与实施例 4的区别是: 在所述气 体连通通道 9上设气体吸热低品位热源加热器 1 7。  The small temperature rise and low entropy co-firing engine shown in Fig. 5 differs from the embodiment 4 in that a gas-absorbing low-grade heat source heater 17 is provided on the gas communication passage 9.
实施例 6  Example 6
如图 6所示的小温升低熵混燃发动机, 其与实施例 4的区别是: 在所述气 体连通通道上和 /或在所述进气道上和 /或在所述排气道上设气体放热环境冷 却器。  a small temperature rise and low entropy co-firing engine as shown in FIG. 6, which differs from Embodiment 4 in that: on the gas communication passage and/or on the intake passage and/or on the exhaust passage Gas exothermic environment cooler.
实施例 7  Example 7
如图 7所示的小温升低熵混燃发动机, 包括燃烧室, 膨胀剂源 2和燃料源 3, 其与实施例 1的区别是: 所述燃烧室设为轮机燃烧室 102, 所述轮机燃烧室 102的承压能力大于等于 2MPa, 调整所述轮机的压气机 6和动力涡轮 7的流量 使所述轮机燃烧室 102内的压力大于等于 2MPa;在所述燃烧室设为所述轮机燃 烧室 102的结构中调整所述轮机的压气机 6和动力涡轮 7的体积流量比使所述 轮机燃烧室 102内燃烧前气体的温度在 1000K以上。 a small temperature rise and low entropy co-firing engine as shown in FIG. 7 , comprising a combustion chamber, a swelling agent source 2 and a fuel source 3, which is different from Embodiment 1 in that: the combustion chamber is set as a turbine combustion chamber 102, The pressure capacity of the turbine combustion chamber 102 is greater than or equal to 2 MPa, and the flow rate of the compressor 6 and the power turbine 7 of the turbine is adjusted such that the pressure in the turbine combustion chamber 102 is greater than or equal to 2 MPa; Adjusting the volumetric flow ratio of the compressor 6 and the power turbine 7 of the turbine in the structure of the combustion chamber 102 The temperature of the gas before combustion in the turbine combustion chamber 102 is 1000 K or more.
具体实施时, 调整所述轮机的压气机 6和动力涡轮 7的流量使所述轮机燃 烧室 102内的压力大于等于 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、 1 1 MPa、 1 1 . 5Pa、 12MPa、 12. 5MPa、 13MPa、 13. 5MPa、 14MPa、 14. 5MPa、 1 5MPa、 1 5. 5MPa、 1 6MPa、 16. 5MPa 1 7MPa、 1 7. 5 Pa 18MPa、 18. 5MPa、 1 9MPa、 1 9. 5MPa、 20MPa、 22MPa、 24MPa、 26MPa、 28MPa、 30MPa、 32MPa、 34MPa、 36MPa、 38MPa 或大于等于 40MPa; 调整所述轮机的压气机 6和动力涡轮 7的体积流量比使所 述轮机燃烧室 102内燃烧前气体的温度在 1300K以上、 1500K以上、 1800K以 上、 2000K以上、 2300K以上、 2500K以上、 2800K以上、 3000K以上、 3200K 以上或 3500K以上。  5MPa,5MPa,5MPa,5. 5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa,5MPa 5MPa, 6MPa, 6. 5MPa, 7MPa, 7. 5MPa, 8MPa, 8. 5MPa, 9MPa, 9. 5MPa, 10MPa, 10. 5MPa, 1 1 MPa, 1 1 . 5Pa, 12MPa, 12. 5MPa, 13MPa, 13 5MPa, 14MPa, 14. 5MPa, 1 5MPa, 15.5MPa, 16 6MPa, 16. 5MPa 1 7MPa, 1 7. 5 Pa 18MPa, 18. 5MPa, 1 9MPa, 1 9. 5MPa, 20MPa, 22MPa, 24MPa 26MPa, 28MPa, 30MPa, 32MPa, 34MPa, 36MPa, 38MPa or 40MPa or more; adjusting the volumetric flow ratio of the compressor 6 and the power turbine 7 of the turbine to make the temperature of the gas before combustion in the turbine combustion chamber 102 at 1300K Above, 1500K or more, 1800K or more, 2000K or more, 2300K or more, 2500K or more, 2800K or more, 3000K or more, 3200K or more, or 3500K or more.
实施例 8  Example 8
如图 8所示的小温升低熵混燃发动机, 其与实施例 7的区别是: 用氧化剂 源 5取代了所述膨胀剂源 2,所述氧化剂源 5经氧化剂导入控制机构 16与所述 轮机燃烧室 102连通。  The small temperature rise and low entropy co-firing engine shown in Fig. 8 differs from the embodiment 7 in that: the expander source 2 is replaced by an oxidant source 5, and the oxidant source 5 is introduced into the control unit 16 via the oxidant. The turbine combustion chamber 102 is in communication.
实施例 9  Example 9
如图 9所示的小温升低熵混燃发动机, 其与实施例 5的区别是: 所述小温 升低熵混燃发动机还包括氧化剂源 5、 气体连通通道 9和气体吸热低品位热源 加热器 17 , 所述氧化剂源 5经氧化剂导入控制机构 1 6与所述轮机燃烧室 102 连通, 所述气体连通通道 9连通所述压气机 6的进气道 10和所述动力涡轮 7 的排气道 1 1, 爱所述排气道 1 1上设排气方出口 12, 在所述排气放出口 12处 设排气放出阀 13, 所述氧化剂导入控制机构 16、 所述燃料导入控制机构 30、 所述膨胀剂导入控制机构 20和所述排气放出阀 13受燃烧控制装置 3020控制。  The small temperature rise and low entropy co-firing engine shown in FIG. 9 is different from the embodiment 5 in that: the small temperature rise and low entropy co-firing engine further includes an oxidant source 5, a gas communication passage 9, and a gas absorption low grade. a heat source heater 17 that communicates with the turbine combustion chamber 102 via an oxidant introduction control mechanism 16 that communicates with the intake passage 10 of the compressor 6 and the power turbine 7 The exhaust passage 1 1 is provided with an exhaust gas outlet 12, and an exhaust gas discharge valve 13 is provided at the exhaust gas discharge port 12, and the oxidant introduction control mechanism 16 and the fuel introduction The control mechanism 30, the expansion agent introduction control mechanism 20, and the exhaust gas release valve 13 are controlled by the combustion control device 3020.
实施例 10  Example 10
如图 10所示的小温升低熵混燃发动机, 其与实施例 1 的区别是: 在所述 燃烧室的排气道 1 1处设气液分离器 1 100, 所述膨胀剂源 2设为所述气液分离 器 1 100的液体出口, 所述气液分离器 1 1 00内的液体作为所述膨胀剂使用。  The small temperature rise and low entropy co-firing engine shown in FIG. 10 is different from the embodiment 1 in that: a gas-liquid separator 1 100 is disposed at the exhaust passage 11 of the combustion chamber, and the expander source 2 The liquid outlet of the gas-liquid separator 1 100 is used, and the liquid in the gas-liquid separator 1 100 is used as the expansion agent.
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 is disclosed according to the well-known technology and the present invention in the art. The technical solutions can be deduced or associated with many variants, all of which are also considered to be the scope of protection of the present invention.

Claims

权利要求 Rights request
1、一种小温升低熵混燃发动机,包括燃烧室,膨胀剂源(2 )和燃料源(3), 其特征在于: 所述燃料源 (3) 经燃料导入控制机构 (30) 与所述燃烧室连通, 所述膨胀剂源 (2 ) 经膨胀剂导入控制机构 (20) 与所述燃烧室连通, 所述燃 料导入控制机构(30)和所述膨胀剂导入控制机构(20)受燃烧控制装置(3020) 控制; 所述燃烧室设为活塞式发动机燃烧室(101 ), 所述活塞式发动机燃烧室 ( 101 ) 的承压能力大于等于 4MPa, 或所述燃烧室设为轮机燃烧室 (102), 所 述轮机燃烧室 (102) 的承压能力大于等于 2MPa。  A small temperature rising low entropy co-firing engine comprising a combustion chamber, a swelling agent source (2) and a fuel source (3), characterized in that: the fuel source (3) is controlled by a fuel introduction control mechanism (30) The combustion chamber is in communication, the expansion agent source (2) is in communication with the combustion chamber via a expansion agent introduction control mechanism (20), the fuel introduction control mechanism (30) and the expansion agent introduction control mechanism (20) Controlled by a combustion control device (3020); the combustion chamber is set as a piston engine combustion chamber (101), the piston engine combustion chamber (101) has a pressure bearing capacity of 4 MPa or more, or the combustion chamber is set to be a turbine The combustion chamber (102), the turbine combustion chamber (102) has a pressure bearing capacity of 2 MPa or more.
2、 如权利要求 1 所述小温升低熵混燃发动机, 其特征在于: 在所述燃烧 室和所述膨胀剂源(2 )之间设膨胀剂吸热热交换器 (1020), 使所述膨胀剂源 2. The small temperature rising low entropy co-firing engine according to claim 1, wherein: an expansion agent heat absorption heat exchanger (1020) is disposed between the combustion chamber and the expansion agent source (2), Expansion agent source
(2 ) 内的膨胀剂在所述膨胀剂吸热热交换器 (1020) 中吸热。 The expansion agent in (2) absorbs heat in the expansion agent heat absorption heat exchanger (1020).
3、 如权利要求 2所述小温升低熵混燃发动机, 其特征在于: 所述膨胀剂 吸热热交换器 (1020) 的热源设为所述小温升低熵混燃发动机的余热。  3. The low temperature rise and low entropy co-firing engine according to claim 2, wherein: the heat source of said expander heat absorbing heat exchanger (1020) is set to a residual heat of said small temperature rise and low entropy co-firing engine.
4、 如权利要求 2所述小温升低熵混燃发动机, 其特征在于: 所述膨胀剂 源(2 ) 内的膨胀剂在所述膨胀剂吸热热交换器(1020) 中吸热达到临界状态、 超临界状态或超超临界状态后再进入所述燃烧室。  4. The low temperature rise and low entropy co-firing engine according to claim 2, wherein: the expansion agent in the expansion agent source (2) absorbs heat in the expansion agent heat absorption heat exchanger (1020) The critical state, supercritical state or ultra-supercritical state is then entered into the combustion chamber.
5、 如权利要求 1 所述小温升低熵混燃发动机, 其特征在于: 所述小温升 低熵混燃发动机还包括氧化剂源 (5) 和气体连通通道 (9), 所述气体连通通 道 (9) 连通所述燃烧室的进气道 (10) 和排气道 (1 1 ), 在所述排气道 (1 1 ) 上设排气放出口 (12), 在所述排气放出口 (12) 处设排气放出控制阀 (13), 所述氧化剂源 (5 ) 经氧化剂导入控制机构 (16 ) 再经所述进气道 (10) 与所 述燃烧室连通或直接经所述氧化剂导入控制机构(16 ) 与所述燃烧室连通, 所 述氧化剂导入控制机构 (16)、 所述燃料导入控制机构 (30) 和所述膨胀剂导 入控制机构 (20) 受燃烧控制装置 (3020) 控制。  5. The low temperature rise and low entropy co-firing engine according to claim 1, wherein: said small temperature rise and low entropy co-firing engine further comprises an oxidant source (5) and a gas communication passage (9), said gas communication a passage (9) connecting the intake passage (10) and the exhaust passage (1 1 ) of the combustion chamber, and an exhaust gas discharge port (12) is disposed on the exhaust passage (1 1 ) at the exhaust An exhaust gas discharge control valve (13) is disposed at the discharge port (12), and the oxidant source (5) is connected to the combustion chamber via the oxidant introduction control mechanism (16) via the oxidant inlet (10) or directly The oxidant introduction control mechanism (16) is in communication with the combustion chamber, and the oxidant introduction control mechanism (16), the fuel introduction control mechanism (30), and the expansion agent introduction control mechanism (20) are subjected to a combustion control device. (3020) Control.
6、 如权利要求 5所述小温升低熵混燃发动机, 其特征在于: 在所述气体 连通通道 (9) 上设气体吸热低品位热源加热器 (17 )。  6. The small temperature rise and low entropy co-firing engine according to claim 5, characterized in that: a gas heat absorbing low grade heat source heater (17) is arranged on the gas communication passage (9).
7、 如权利要求 5所述小温升低熵混燃发动机, 其特征在于: 在所述气体 连通通道 (9 ) 上和 /或在所述进气道 (10) 上和 /或在所述排气道 (1 1 ) 上设 气体放热环境冷却器 (18)。 7. The low temperature rise and low entropy co-firing engine according to claim 5, characterized by: on said gas communication passage (9) and/or on said intake passage (10) and/or in said Exhaust duct (1 1 ) Gas exothermic environment cooler (18).
8、 如权利要求 1 所述小温升低墒混燃发动机, 其特征在于: 在所述燃烧 室的排气道 (1 1 )处设气液分离器 (1 100), 所述膨胀剂源 (2) 设为所述气液 分离器 (1 100) 的液体出口, 所述气液分离器 (1 100) 内的液体作为所述膨胀 剂使用。  8. The low temperature rise and low enthalpy co-firing engine according to claim 1, wherein: a gas-liquid separator (1 100) is disposed at an exhaust passage (1 1 ) of said combustion chamber, said expansion agent source (2) A liquid outlet of the gas-liquid separator (1 100) is used, and a liquid in the gas-liquid separator (1 100) is used as the expansion agent.
9、 如权利要求 1 所述小温升低熵混燃发动机, 其特征在于: 所述膨胀剂 源 (2) 内的膨胀剂设为气体液化物。  9. The low temperature rise and low entropy co-firing engine according to claim 1, wherein: the expansion agent in the expansion agent source (2) is a gas liquefaction.
10、 如权利要求 1所述小温升低熵混燃发动机, 其特征在于: 所述燃料源 (3) 内的燃料设为乙醇, 所述膨胀剂源 (2) 内的膨胀剂设为水, 所述燃料源 ( 3) 和所述膨胀剂源 (2) 设为同一个乙醇水溶液储罐。  10. The low temperature rise and low entropy co-firing engine according to claim 1, wherein: the fuel in the fuel source (3) is set to ethanol, and the expansion agent in the expansion agent source (2) is set to water. The fuel source (3) and the expansion agent source (2) are set to be the same aqueous ethanol storage tank.
1 1、 如权利要求 1所述小温升低熵混燃发动机, 其特征在于: 所述燃烧室 设为绝热燃烧室。  A small temperature rise and low entropy co-firing engine according to claim 1, wherein: said combustion chamber is set as an adiabatic combustion chamber.
12、 一种提高如权利要求 1 至 1 1任意之一所述小温升低熵混燃发动机效 率和环保性的方法, 其特征在于: 在所述燃烧室设为所述活塞式发动机燃烧室 12. A method of improving the efficiency and environmental friendliness of a small temperature rise and low entropy co-firing engine according to any one of claims 1 to 11, characterized in that: the combustion chamber is set as the piston engine combustion chamber
( 101 ) 的结构中调整发动机的压縮比使压縮冲程完了燃烧前的被压縮气体的 温度在 1800K的正负 200K的范围内,在所述燃烧室设为所述轮机燃烧室(102 ) 的结构中调整压气机 (6 ) 和动力涡轮 (7 ) 的流量使所述轮机燃烧室 (102 ) 内燃烧前气体的温度在 1800K的正负 200K的范围内; 调整导入所述燃烧室内 的所述膨胀剂源 (2) 内的膨胀剂的量和导入所述燃烧室内的所述燃料源 (3) 内的燃料的量, 使导入所述燃烧室的所述燃料源 (3 ) 内的燃料燃烧所产生的 热量的全部或近乎全部在所述燃烧室内被已导入所述燃烧室内的所述膨胀剂 源 (2 ) 内的膨胀剂吸收; 调整燃料在所述燃烧室内燃烧后所述燃烧室内的气 体温度最高值在有害化合物 NOx生成温度以下以提高发动机的环保性。 The structure of (101) adjusts the compression ratio of the engine such that the compression stroke is completed. The temperature of the compressed gas before combustion is in the range of plus or minus 200K of 1800K, and the combustion chamber is set to the turbine combustion chamber (102). The flow rate of the compressor (6) and the power turbine (7) is adjusted such that the temperature of the gas before combustion in the turbine combustion chamber (102) is within a range of plus or minus 200 K of 1800 K; adjustment is introduced into the combustion chamber. The amount of the expansion agent in the expansion agent source (2) and the amount of fuel introduced into the fuel source (3) in the combustion chamber are introduced into the fuel source (3) of the combustion chamber All or nearly all of the heat generated by the combustion of the fuel is absorbed in the combustion chamber by the expansion agent introduced into the expansion agent source (2) in the combustion chamber; adjusting the combustion of the fuel after combustion in the combustion chamber The highest gas temperature in the room is below the harmful compound NOx generation temperature to improve the environmental friendliness of the engine.
13、 一种提高如权利要求 1 至 1 1任意之一所述小温升低熵混燃发动机效 率和环保性的方法, 其特征在于: 调整导入所述燃烧室内的所述膨胀剂源(2 ) 内的膨胀剂的量和导入所述燃烧室内的所述燃料源 (3 ) 内的燃料的量, 使导 入所述燃烧室的所述燃料源 (3 ) 内的燃料燃烧所产生的热量的全部或近乎全 部在所述燃烧室内被已导入所述燃烧室内的所述膨胀剂源 (2 ) 内的膨胀剂吸 收; 燃料在所述燃烧室燃烧前后所述燃烧室内的温度基本维持不变压力增加, 以提高发动机的效率。 13. A method of improving the efficiency and environmental friendliness of a small temperature rise and low entropy co-combustion engine according to any one of claims 1 to 11, characterized in that: adjusting said expansion agent source introduced into said combustion chamber (2) The amount of the expanding agent and the amount of fuel introduced into the fuel source (3) in the combustion chamber to cause heat generated by combustion of the fuel introduced into the fuel source (3) of the combustion chamber All or nearly all of the expansion agent in the combustion chamber is introduced into the combustion chamber source (2) in the combustion chamber The temperature in the combustion chamber is substantially maintained at a constant pressure before and after combustion of the combustion chamber to increase the efficiency of the engine.
14、 一种提高如权利要求 1 至 1 1任意之一所述小温升低熵混燃发动机效 率和环保性的方法, 其特征在于: 在所述燃烧室设为所述活塞式发动机燃烧室 A method for improving the efficiency and environmental friendliness of a small temperature rise and low entropy co-firing engine according to any one of claims 1 to 11, characterized in that: the combustion chamber is set as the piston engine combustion chamber
( 101 ) 的结构中调整发动机的压縮比使压縮冲程完了燃烧前的被压縮气体的 温度在 1000K以上, 在所述燃烧室设为所述轮机燃烧室 (102) 的结构中调整 压气机 (6) 和动力涡轮 (7 ) 的体积流量比使所述轮机燃烧室 (102 ) 内燃烧 前气体的温度在 1000K以上。 In the structure of (101), the compression ratio of the engine is adjusted such that the compression stroke is completed, and the temperature of the compressed gas before combustion is 1000 K or more, and the compression is adjusted in the structure in which the combustion chamber is set to the turbine combustion chamber (102). The volumetric flow ratio of the machine (6) and the power turbine (7) is such that the temperature of the gas before combustion in the turbine combustion chamber (102) is above 1000K.
15、 一种提高如权利要求 1至 1 1任意之一所述小温升低熵混燃发动机效 率和环保性的方法, 其特征在于: 调整导入所述燃烧室内的所述膨胀剂源(2) 内的膨胀剂的量和导入所述燃烧室内的所述燃料源 (3 ) 内的燃料的量, 使导 入所述燃烧室的所述燃料源 (3) 内的燃料燃烧所产生的热量的 5%以上在所述 燃烧室内被已导入所述燃烧室内的所述膨胀剂源 (2 ) 内的膨胀剂吸收。  15. A method of improving the efficiency and environmental friendliness of a small temperature rise and low entropy co-combustion engine according to any one of claims 1 to 11, characterized in that: the expansion agent source introduced into the combustion chamber is adjusted (2) The amount of the expanding agent and the amount of fuel introduced into the fuel source (3) in the combustion chamber to cause heat generated by combustion of the fuel introduced into the fuel source (3) of the combustion chamber More than 5% of the expansion agent in the expansion agent source (2) introduced into the combustion chamber is absorbed in the combustion chamber.
16、 一种提高如权利要求 1至 1 1任意之一所述小温升低熵混燃发动机效 率和环保性的方法,其特征在于:调整即将开始作功的气体工质的温度到 2000K 以下, 调整即将开始作功的气体工质的压力到 15MPa以上, 使即将开始作功的 气体工质的温度和压力符合类绝热关系。  16. A method for improving the efficiency and environmental friendliness of a small temperature rise and low entropy co-combustion engine according to any one of claims 1 to 11, characterized in that the temperature of the gas working medium to be started to work is adjusted to below 2000 K. Adjust the pressure of the gas working fluid that is about to start work to 15 MPa or more, so that the temperature and pressure of the gas working fluid that is about to start work are in line with the adiabatic relationship.
PCT/CN2011/001430 2010-08-27 2011-08-26 Small temperature rise low-entropy mixed-fuel engine WO2012024898A1 (en)

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