CN106437893A - Heat energy power system for stable temperature gasification - Google Patents
Heat energy power system for stable temperature gasification Download PDFInfo
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- CN106437893A CN106437893A CN201610759495.5A CN201610759495A CN106437893A CN 106437893 A CN106437893 A CN 106437893A CN 201610759495 A CN201610759495 A CN 201610759495A CN 106437893 A CN106437893 A CN 106437893A
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K11/00—Plants characterised by the engines being structurally combined with boilers or condensers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K25/00—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
- F01K25/08—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours
- F01K25/10—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours the vapours being cold, e.g. ammonia, carbon dioxide, ether
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K25/00—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
- F01K25/08—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours
- F01K25/10—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours the vapours being cold, e.g. ammonia, carbon dioxide, ether
- F01K25/106—Ammonia
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- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02N—ELECTRIC MACHINES NOT OTHERWISE PROVIDED FOR
- H02N11/00—Generators or motors not provided for elsewhere; Alleged perpetua mobilia obtained by electric or magnetic means
- H02N11/002—Generators
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- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
The invention discloses a heat energy power system for stable temperature gasification. The system comprises a heat source, a gasification reactor, an acting pump, a condenser, a pressure pump and a circulating pipe; the gasification reactor, the acting pump, the condenser and the pressure pump realize circular communication through circulating pipes; the gasification reactor is contacted with the heat source; and an energy storage device is mounted in the gasification reactor. The heat energy power system for stable temperature gasification buffers the cavity heating to release or absorb one part of heat for maintaining the gasification heating quantity to effectively improve the utilization efficiency of heat energy.
Description
Technical field
The invention belongs to utilization of energy apparatus field, especially a kind of can steady wet dynamic system of heat energy.
Background technology
The energy is the important substance basis that human society is depended on for existence and development.Make a general survey of the history of human social development, people
The major progress each time of class civilization is all accompanied by improvement and the replacement of the energy.The exploitation of the energy greatly advance the world
Economy and the development of human society.
But the consumption that is continuously developed with the energy, the non-renewable energy resources such as oil, colliery, natural gas are progressively tightened, energy
The saving in source and recycling progressively is taken seriously.For responding national energy-saving strategy, increasing enterprise starts to research and develop, uses section
Energy equipment, and strengthen the utilization to discarding production capacity thing, waste heat energy.Wherein, in terms of the utilization of waste heat, mainly pass through heat energy power-generating
Equipment is realizing surplus energy utility.Existing thermal generating equipment includes plurality of classes, but can be divided mainly into two classes, and a class is to utilize
Gas expansion for doing work, heat energy is changed into mechanical energy, then mechanical energy is changed into electric energy, and the generating equipment of this kind of principle classification is relatively
For maturation, species is many；Another kind of is using pyroelectric effect principle, by thermoelectric conversion element, heat energy is directly translated into potential
Can, but as immature in terms of generation technology, electrical power is little, manufacturing cost height, and thermoelectric conversion efficiency is low, is mainly used in
Microelectronic.
At this stage, most enterprises are big due to complementary energy exclusion amount, in the utilization of waste heat, mainly also need to rely on above-mentioned first
Heat energy is changed into mechanical energy by gas expansion for doing work, then mechanical energy is changed into electric energy by class thermal generating equipment.Existing
Such thermal generating equipment mainly includes gasification installation, turbine, electromotor and condensing units；During work, cycle fluid is being followed
Pass through gasification installation first in endless tube road, working medium is gasified and is promoted turbine to rotate, the working medium after gasification is passing through turbine
When, externally doing work, temperature and air pressure can reduce, and be cooled to liquid refrigerant by condensing units.
The heat energy utilization equipment of existing utilization gas expansion for doing work, in the ideal case, the maximum rate of its heat energy conversion is
Carnot's cycle efficiency, namely 1-T0/T1, wherein T0For low temperature cold source temperature, T1For high temperature heat source；But the actual acting of thermal hardware
Process, on the one hand, due to cycle fluid in gasification installation gasification, its gasification expansion actual temperature and high temperature heat source temperature
The temperature difference of degree is larger, and actual temperature is lower than high temperature heat source temperature, its theoretical T1Drop is little, causes heat energy peak efficiency to reduce；Separately
On the one hand, the actual condensation temperature due to cycle fluid in condensing units is higher than low temperature cold source temperature, its theoretical T0Increase,
Heat energy peak efficiency is caused to reduce；Further, since turbine is low to the absorbance of gas expansion for doing work, its mechanical energy conversion effect
Rate is relatively low；In addition, impurity easily occurs in cycle fluid, cycle fluid power consumption is larger.
And existing thermal hardware causes the particular problem of above-mentioned deviation to include：1. the heat conductivity of gasification installation is poor, right
The temperature requirement height of high temperature heat source；2. the pressure of gasification installation is unstable, gasifies temperature required unstable, when temperature needed for gasification
Degree more than heat source temperature when, medium cannot realize gasification, when gasify temperature required less than heat source temperature when, gasification expansion temperature inclined
Low, to absorb heat less, net work amount diminishes；3. in condensing units, the pressure of medium is unstable, and condensation is temperature required unstable, when cold
Solidifying temperature required less than sink temperature when, it is impossible to realize condensation, when condense temperature required more than sink temperature when, temperature after condensation
Too low；4. condensation in condensing units is incomplete, gas-liquid mixed state easily occurs, causes its working medium gasifying in gasification installation
Swelling volume is less than normal；5. existing turbine torsion is less than normal, and volumetric leak amount is big, less efficient；6. the heat energy of existing thermal hardware
Transformation efficiency is low, and heat energy transformation efficiency is generally 10% to 30%；7. working medium is apt to deteriorate or impurity occurs.
Content of the invention
Present invention purpose to be realized is：Heat energy transformation efficiency is improved, rate of gasification of the working medium in gasification installation is improved,
Increase the drive of turbine, turbine efficiency is improved, stablize working medium gasification temperature and refrigerant flow rate, improve working medium quality, prevent
Only working medium goes bad, and improves turbine structure, it is to avoid turbine is revealed and rotary speed unstabilization, improves condensing units, accelerates condensing rate, subtracts
The thermal waste of little condensation process；To solve in above-mentioned background technology existing for existing thermal hardware：Heat energy transformation efficiency is low,
Working medium gasifies not exclusively in gasification installation, and working medium gasification temperature is unstable, and working medium condensation effect is not good, working medium apt to deteriorate or
There is impurity, the problems such as the thermal waste of condensing units is big, condensing rate is slow or needs extra power consumption.
For solving its technical problem the technical solution adopted in the present invention it is：A kind of can steady wet thermal power system
System, including thermal source, gasification reactor, acting pump, condenser, compression pump and circulating line, gasification reactor, acting pump, condensation
Device and compression pump realize circulation UNICOM by circulating line, and gasification reactor contacts thermal source；
It is characterized in that：In the gasification reactor, energy storage equipment is installed.
Further, the energy storage equipment is made using high heat capacity material；
Further, the energy storage equipment is closing water body.
Further, include multi-layer cavity in the gasification reactor.
Further, include inner chamber, exocoel and lumen in the cavity, between inner chamber and exocoel, pass through lumen UNICOM, thermal source
Circulate between inner chamber and exocoel.
Further, multiple lumens, the fan-shaped distribution of lumen are included between the inner chamber and exocoel.
Further, in a ring, the energy storage equipment is in the middle part of inner chamber for the inner chamber.
Further, the energy storage equipment is installed in the outer layer of exocoel.
Further, the energy storage equipment is flexibly connected with exocoel, and energy storage equipment is detachable.
Using said structure, the temperature of its gasification reactor has more stability, while also improving heat conduction rate；Work as the external world
When the heating load of thermal source changes, energy storage equipment can enter row buffering, release or absorption partial heat to cavity heat supply, for tieing up
Biomass gasification boiler amount is held, the utilization ratio of heat energy can be effectively improved.
Further, the cavity is in ellipse.
Further, the acting pump is impeller acting pump.
Further, the acting pump is vacuum acting pump.
Further, the acting pump is piston type acting pump.
Further, the acting pump includes circular cavity, eccentric blade and grooved runner, and grooved runner is eccentrically mounted at circle
In the eccentric shaft in chamber, the side of grooved runner offers draw-in groove, and eccentric blade is arranged on draw-in groove, the side of circular cavity by spring leaf
While being respectively arranged with air inlet and gas outlet, air inlet is more than adjacent two eccentric interlobate spacing with the pitch angles of gas outlet
Angle.
Further, the side of the circular cavity is provided with multiple gas outlets, and gas outlet is more than with the pitch angles of air inlet
Adjacent two eccentric interlobate pitch angles.
Further, the moving vane of the revolving wormgear structure includes at least three.
Further, the condenser is liquid-cooled freezing machine.
Further, the condenser includes condensing tube and multiple condensation chambers, cold by least one between two condensation chambers
Solidifying pipe connection.
Further, the condensing tube is curvilinear.
Further, the condensing tube is twist.
Further, the condenser is ventilation type freezing machine.
Further, the condensing units include condensing tube, fin and heat emission fan, and condensing tube periphery installed by fin, dissipate
Heat is fanned above or below condensing tube or side, and heat emission fan is driven with convulsion mode or pressure wind mode.
Further, the condensing tube is in multilamellar or multiple rows of distribution, the mutual UNICOM of condensing tube, and heat emission fan is on condensing tube
Side or lower section, heat emission fan is driven with convulsion mode or pressure wind mode.
Further, the UNICOM direction of the condensing tube is in vertically or horizontally or tiltedly type.
Further, the condensing tube is made by thermo-electric generation sheet.
Further, the thermo-electric generation sheet includes sheet metal, p-type semiconductor, n-type semiconductor, dielectric substrate layer and output
Electrode, dielectric substrate layer is uniformly interspersed with p-type semiconductor and n-type semiconductor, equally distributed p-type semiconductor and n-type semiconductor
Connected by sheet metal, p-type semiconductor is connected output electrode respectively with the series connection whole story end of n-type semiconductor；
Further, the working medium in the circulating line adopts pure water.
Further, the working medium in the circulating line adopts propanol.
Further, the working medium in the circulating line adopts methanol.
Further, the working medium in the circulating line adopts ethanol.
Further, the working medium in the circulating line adopts isopropanol.
Further, the working medium in the circulating line adopts liquefied ammonia.
Further, the working medium in the circulating line adopts freon.
Further, the circulating line is connected with regulating system, regulating system include pressure regulator, temperature sensor and
Medium actuator, temperature sensor is in gasification reactor, and pressure regulator control connects compression pump, and medium actuator is pacified
It is mounted in circulating line, for adjusting rate-of flow.
Further, the regulating system also includes multiple pressure transducers, and pressure transducer is evenly distributed on circulating line
In.
Further, the regulating system also includes two pressure transducers, and two pressure transducers are separately mounted to acting
The import and export end of pump.
Further, in the regulating system, pressure transducer is evenly distributed with.
Using said structure, when the temperature of working medium in gasification reactor changes, regulating system is adjusted by pressure
Device and medium actuator adjust sender matter pressure and flow velocity so as to temperature province temperature.
Further, in the gasification reactor, temperature inductor is provided with
Further, the condenser also includes collecting tank, and collecting tank is used for collecting the condensed fluid in condenser.
Using said structure, can effectively prevent liquid refrigerant in condenser from mixing a large amount of gases, cause part working medium without
Condensation liquefaction enters booster pump.
Further, the collecting tank is located at the afterbody of condenser.
Further, the entrance point of the gasification reactor is additionally provided with nebulizer.
Further, the front end of the gasification reactor is additionally provided with preheating cavity；
The outer heat extraction energy of gasification reactor periphery can be utilized using said structure, reduce thermal waste.
Further, the preheating cavity is looped around gasification reactor periphery.
Further, the preheating cavity helically type.
Further, at the acting pump exhaust inlet, preliminary condensation chamber is provided with；
Take said structure increase the pressure reduction of air inlet and air vent, improve the transformation efficiency of turbine.
Further, the preliminary condensation chamber adopts air-cooled or water-cooled.
Further, the preheating cavity and preliminary condensation chamber paratactic contact；
Said structure being taken, heat absorption being needed due to preheating intracavity working medium, and preliminary condensation intracavity working medium needs heat extraction, the structure is larger
Degree recycle working medium heat in circulating line, increase thermal transition efficiency.
Further, a negative pressure pump is provided with the condenser, and negative pressure pump is arranged on condensing tube middle-end；
Take said structure, it is possible to decrease the pressure at acting pump discharge end, increase acting pump into and out of two ends pressure reduction, do so as to increase
The amount of work of work(pump, reduces the interior energy after working medium acting, improves the condensing rate of working medium, and improve heat energy efficiency.
Further, in the condenser, multiple negative pressure pumps are provided with, negative pressure pump is evenly distributed in condensing tube；
Take said structure, it is possible to decrease the pressure at acting pump discharge end, largely pressure difference is improved, preferably can realize point
Level condensation, and reduce energy consumption needed for supercharging.
Further, in the gasification reactor, energy storage equipment is installed.
Further, the energy storage equipment is made using high heat capacity material.
Further, the energy storage equipment is closing water body.
Said structure is taken, the temperature of gasification reactor inner chamber body can be stablized, so as to stablize gasification temperature.
Further, contaminant filter pump is additionally provided between the condenser and compression pump.
Operation principle is as follows：
Described in the invention can steady wet dynamic system of heat energy, during work, cycle fluid absorbs heat the heat that reaches a high temperature in thermal source
Source temperature, then flow in gasification reactor, acting pump is flowed after working medium gasification；After gasification working medium flows through acting pump, due to external
Acting, its Temperature of Working and air pressure can all reduce, and cause part working medium liquefaction；Gasification working medium flow through acting pump after, working medium according to
Secondary stream is to condenser and compression pump；Working medium is again introduced into gasification reactor after compression pump supercharging, completes a circulation.
Beneficial effect：Of the present invention can steady wet dynamic system of heat energy, the heat energy machine in hinge structure,
Have the advantages that following several respects and progress：1. the heat conduction rate of cavity is improve, stable gasification temperature, preferably avoid working medium
Liquid gasifies not exclusively in gasification installation；2. largely increase turbine turns power, and with output power evenly；
3. effectively prevent condensation incomplete, reduce intracavity pressure, improve efficiency；4. working medium gasification temperature and refrigerant flow rate can be stablized,
Gasification efficiency and condensation efficiency can be effectively improved；5. waste heat is made full use of, is increased thermal source heat absorption, increase amount of work, improve heat energy
Transformation efficiency；6. working medium heat in circulating line is recycled, largely increases thermal transition efficiency；7. working medium is improve
Degree of purity, effectively prevents the pump leakage problem that does work.
Description of the drawings
Fig. 1 is the integrated connection theory structure schematic diagram of the embodiment of the present invention one；
Fig. 2 is the gasification reactor structural representation of the embodiment of the present invention two；
Fig. 3 is the acting pump configuration schematic diagram of the embodiment of the present invention three；
Fig. 4 is the condenser structure schematic diagram of the embodiment of the present invention four；
Fig. 5 is the condenser structure schematic diagram of the embodiment of the present invention five；
Fig. 6 is the circulating line structural representation of the embodiment of the present invention six；
Fig. 7 is the condenser structure schematic diagram of the embodiment of the present invention seven；
Fig. 8 is the preheating cavity structural representation of the embodiment of the present invention eight；
Fig. 9 is the preliminary condensation cavity configuration schematic diagram of the embodiment of the present invention nine；
Figure 10 is the attachment structure schematic diagram of the preliminary condensation chamber with preheating cavity of the embodiment of the present invention ten；
Figure 11 is condenser and the negative pressure pump structural representation of the embodiment of the present invention 11；
Figure 12 is condenser and the negative pressure pump structural representation of the embodiment of the present invention 12；
In figure：
1 is thermal source；
2 is gasification reactor, 21 is cavity, 211 is inner chamber, 212 is exocoel, 213 is lumen, 22 is temperature inductor, 23 are
Nebulizer, 24 be preheating cavity, 25 be energy storage equipment；
3 is acting pump, 301 is preliminary condensation chamber, 31 is circular cavity, 311 is eccentric shaft, 32 is eccentric blade, 33 is grooved runner,
34 is draw-in groove, 35 is spring leaf, 36 is air inlet, 37 is gas outlet；
4 is that condenser, 41 is that condenser pipe, 411 is that thermo-electric generation sheet, 412 is that sheet metal, 413 is that p-type semiconductor, 414 is N-shaped Quasiconductor, 415 be dielectric substrate layer, 416 be output electrode, 42 be condensation chamber, 43 be fin, 44 be heat emission fan, 45 for collection Liquid bath, 46 are negative pressure pump;
5 is compression pump；
6 is circulating line, 61 is regulating system, 611 is pressure regulator, 612 is temperature sensor, 613 is medium actuator,
614 is pressure transducer.
Specific embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation is described；Obviously, described embodiment is only a part of embodiment of the present invention, rather than whole embodiments.It is based on
Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under the premise of creative work is not made
Embodiment, belongs to the scope of protection of the invention.
Embodiment one（As shown in Figure 1）：A kind of can steady wet dynamic system of heat energy, including thermal source 1, gasification reactor
2nd, acting pump 3, condenser 4, compression pump 5 and circulating line 6, gasification reactor 2, acting pump 3, condenser 4 and compression pump 5 pass through
Circulating line 6 realizes circulation UNICOM, and gasification reactor 2 contacts thermal source 1；
Used as illustrating for above-mentioned implementation process, the thermal source 1 adopts high temperature combustion gas.
As illustrating for above-mentioned implementation process, in the gasification reactor 2, include one layer of cavity 21；The cavity 21
In ellipse.
Used as illustrating for above-mentioned implementation process, the acting pump 3 is impeller acting pump.
Used as illustrating for above-mentioned implementation process, the condenser 4 is ventilation type freezing machine.
Used as illustrating for above-mentioned implementation process, the compression pump 5 is liquid pressure pump.
Used as illustrating for above-mentioned implementation process, the working medium in the circulating line 6 adopts pure water.
By in above-described embodiment can the dynamic system of heat energy of steady wet test, heat source temperature is respectively
120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 350 DEG C, the ambient temperature of condenser 4 is 25 DEG C, refrigerant flow rate in circulation pipe
According to can the operation stability of the steady dynamic system of heat energy of wet be adjusted；Experiment effect is：Heat source temperature is 120 DEG C,
Heat energy transformation efficiency is about 8%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 10%, when heat source temperature is 200 DEG C, heat
Energy transformation efficiency is about 15%, and heat source temperature is that 250 DEG C, heat energy transformation efficiency is about 20%, when heat source temperature is 300 DEG C, heat energy
Transformation efficiency is about 25%, and when heat source temperature is 350 DEG C, heat energy transformation efficiency is about 28%；In 120-350 DEG C of thermal source section, this reality
Apply in example can the comprehensive heat energy transformation efficiency of the steady dynamic system of heat energy of wet be about 18%.
Embodiment two（As shown in Figure 2）：It is with one difference of embodiment：In the gasification reactor 2, storage is installed
Can device 25；The energy storage equipment 25 is made using high heat capacity material；The energy storage equipment 25 is closing water body；The gasified reverse
Answering in device includes multi-layer cavity 21；Include inner chamber 211, exocoel 212 and lumen 213, inner chamber 211 and exocoel in the cavity 21
Pass through 213 UNICOM of lumen between 212, thermal source 1 is circulated between inner chamber 211 and exocoel 212；The inner chamber 211 and exocoel 212 it
Between include multiple lumens 213, the fan-shaped distribution of lumen 213；The energy storage equipment 25 is installed in the outer layer of exocoel 212；The storage
Energy device 25 is flexibly connected with exocoel 212, and energy storage equipment 25 is detachable.
Using said structure, the temperature of its gasification reactor has more stability, while also improving heat conduction rate；Work as the external world
When the heating load of thermal source changes, energy storage equipment 25 can enter row buffering, release or absorption partial heat to cavity heat supply, be used for
Biomass gasification boiler amount is maintained, the utilization ratio of heat energy can be effectively improved.
By in above-described embodiment can the dynamic system of heat energy of steady wet test, heat source temperature is respectively
120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 350 DEG C, the ambient temperature of condenser 4 is 25 DEG C, refrigerant flow rate in circulation pipe
According to can the operation stability of the steady dynamic system of heat energy of wet be adjusted；Experiment effect is：Heat source temperature is 120 DEG C,
Heat energy transformation efficiency is about 12%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 14%, when heat source temperature is 200 DEG C,
Heat energy transformation efficiency is about 19%, and heat source temperature is that 250 DEG C, heat energy transformation efficiency is about 24%, when heat source temperature is 300 DEG C, heat
Energy transformation efficiency is about 29%, and when heat source temperature is 350 DEG C, heat energy transformation efficiency is about 32%；In 120-350 DEG C of thermal source section, this
In embodiment can the comprehensive heat energy transformation efficiency of the steady dynamic system of heat energy of wet be about 22%；With respect to embodiment one, heat energy turns
Change improved efficiency about 4%.
Embodiment three（As shown in Figure 3）：It is with one difference of embodiment：The acting pump 3 includes circular cavity 31, partially
Lobus cardiacus piece 32 and grooved runner 33, grooved runner 33 is eccentrically mounted in the eccentric shaft 311 of circular cavity 31, the side of grooved runner 33
While offer draw-in groove 34, eccentric blade 32 is arranged on draw-in groove 34 by spring leaf 35, the side of circular cavity 31 be respectively arranged with into
QI KOU 36 and gas outlet 37, air inlet 36 is with the pitch angles of gas outlet 37 more than the pitch angle between adjacent two eccentric blades 32
Degree；The side of the circular cavity 31 is provided with multiple gas outlets 37, and gas outlet 37 is with the pitch angles of air inlet 36 more than adjacent
Pitch angles between two eccentric blades 32；The eccentric blade 32 of the acting pump 3 includes four.
Using said structure, between adjacent eccentric blade 32, constitute isolation chamber, communicate with air inlet 36 for expansion chamber,
Communicate with gas outlet 37 for exhaust chamber；Due to the area difference of 36 both sides of air inlet bias blade 32, expansion chamber is intended to
Volume becomes general orientation rotation, so that blade is rotated；The vane stress of this kind of acting pump 3 be gas-static poor by force, and do work away from
From larger, conventional rotating vane acting pump 3 is compared（Pressure is produced by flow of fluid to drive, namely gas-kinetic pressure is poor）, tool
There is larger thrust, can be more fully hereinafter using kinetic energy and the potential energy of gasification working medium, with preferable heat energy transformation efficiency.
By in above-described embodiment can the dynamic system of heat energy of steady wet test, heat source temperature is respectively
120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 350 DEG C, the ambient temperature of condenser 4 is 25 DEG C, refrigerant flow rate in circulation pipe
According to can the operation stability of the steady dynamic system of heat energy of wet be adjusted；Experiment effect is：Heat source temperature is 120 DEG C,
Heat energy transformation efficiency is about 14%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 16%, when heat source temperature is 200 DEG C,
Heat energy transformation efficiency is about 21%, and heat source temperature is that 250 DEG C, heat energy transformation efficiency is about 26%, when heat source temperature is 300 DEG C, heat
Energy transformation efficiency is about 31%, and when heat source temperature is 350 DEG C, heat energy transformation efficiency is about 33%；In 120-350 DEG C of thermal source section, this
In embodiment can the comprehensive heat energy transformation efficiency of the steady dynamic system of heat energy of wet be about 24%；With respect to embodiment one, heat energy turns
Change improved efficiency about 6%.
Example IV（As shown in Figure 4）：It is with one difference of embodiment：The condenser 4 adopts the cold mode of liquid, institute
Stating condenser 4 includes condensing tube 41 and four condensation chambers 42, is connected by many condensing tubes 41 between two condensation chambers 42；Described
Condensing tube 41 is curvilinear；The condensing tube 41 is twist.
Using said structure, as the working medium in its condenser 4 is through multiple mixed flow and shunting, with extraneous contact area
Greatly, working medium can realize the separation of air-liquid state in condensation chamber 42, can be prevented effectively from condensation not exclusively, reduce the pressure of condensation chamber 42
By force, the amount of work of acting pump 3 is improved, meanwhile, working medium expansion rate in the gasification reactor 2 can be also improved, so as to improve effect
Rate.
By in above-described embodiment can the dynamic system of heat energy of steady wet test, heat source temperature is respectively
120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 350 DEG C, the ambient temperature of condenser 4 is 25 DEG C, refrigerant flow rate in circulation pipe
According to can the operation stability of the steady dynamic system of heat energy of wet be adjusted；Experiment effect is：Heat source temperature is 120 DEG C,
Heat energy transformation efficiency is about 13%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 15%, when heat source temperature is 200 DEG C,
Heat energy transformation efficiency is about 20%, and heat source temperature is that 250 DEG C, heat energy transformation efficiency is about 25%, when heat source temperature is 300 DEG C, heat
Energy transformation efficiency is about 30%, and when heat source temperature is 350 DEG C, heat energy transformation efficiency is about 32%；In 120-350 DEG C of thermal source section, this
In embodiment can the comprehensive heat energy transformation efficiency of the steady dynamic system of heat energy of wet be about 23%；With respect to embodiment one, heat energy turns
Change improved efficiency about 5%.
Embodiment five（As shown in Figure 5）：It is with one difference of embodiment：The condenser 4 adopts air cooling way, institute
Stating condensing units 4 includes condensing tube 41, fin 43 and heat emission fan 44, and fin 43 installs 41 periphery of condensing tube, heat emission fan 44
Above or below condensing tube 41 or side, heat emission fan 44 is driven with convulsion mode or pressure wind mode；The condensing tube 41
In multilamellar or multiple rows of distribution, the mutual UNICOM of condensing tube 41；The condensing tube 41 is made by thermo-electric generation sheet 411；The temperature difference
Generating piece 411 includes sheet metal 412, p-type semiconductor 413, n-type semiconductor 414, dielectric substrate layer 415 and output electrode 416,
Dielectric substrate layer 415 is uniformly interspersed with p-type semiconductor 413 and n-type semiconductor 414, equally distributed p-type semiconductor 413 and N-shaped
Quasiconductor 414 is connected by sheet metal 412, and p-type semiconductor 413 is connected output respectively with the series connection whole story end of n-type semiconductor 414
Electrode 416.
Using said structure, as in its condenser 4, condensing tube 41 adopts thermo-electric generation sheet 41, the p of thermo-electric generation sheet 41
Type quasiconductor 413 and n-type semiconductor 414, can produce potential when two ends have the temperature difference, the heat source side of p-type semiconductor 413 and cold
Source is respectively low potential end and high potential end, and the heat source side of n-type semiconductor 414 and low-temperature receiver end are respectively high potential end and low electricity
Gesture end, can achieve voltage superposition when p-type semiconductor 413 and n-type semiconductor 414 are connected, so as to realize generating electricity；Therefore, the temperature difference
Its partial heat can be changed into electromotive force while heat is driven by generating piece；The structure preferably can reduce heat-energy losses,
Improve heat energy transformation efficiency.
By in above-described embodiment can the dynamic system of heat energy of steady wet test, heat source temperature is respectively
120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 350 DEG C, the ambient temperature of condenser 4 is 25 DEG C, refrigerant flow rate in circulation pipe
According to can the operation stability of the steady dynamic system of heat energy of wet be adjusted；Experiment effect is：Heat source temperature is 120 DEG C,
Heat energy transformation efficiency is about 12%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 14%, when heat source temperature is 200 DEG C,
Heat energy transformation efficiency is about 19%, and heat source temperature is that 250 DEG C, heat energy transformation efficiency is about 24%, when heat source temperature is 300 DEG C, heat
Energy transformation efficiency is about 29%, and when heat source temperature is 350 DEG C, heat energy transformation efficiency is about 31%；In 120-350 DEG C of thermal source section, this
In embodiment can the comprehensive heat energy transformation efficiency of the steady dynamic system of heat energy of wet be about 22%；With respect to embodiment one, heat energy turns
Change improved efficiency about 4%.
Embodiment six（As shown in Figure 6）：It is with one difference of embodiment：The circulating line 6 is connected with regulation system
System 61, regulating system 61 includes pressure regulator 611, temperature sensor 612 and medium actuator 613, and temperature sensor 612 is pacified
It is mounted in gasification reactor 2, the control connection compression pump 5 of pressure regulator 611, medium actuator 613 is arranged on circulating line 6
In, for adjusting rate-of flow；The regulating system 61 also includes two pressure transducers 614,614 points of two pressure transducers
An Zhuan not do work the import and export end of pump 3.
Using said structure, when the temperature of working medium in gasification reactor 2 changes, regulating system 61 is adjusted by pressure
Section device 611 and medium actuator 613 adjust sender matter pressure and flow velocity so as to temperature province temperature stabilization, Jie that preferably can avoid
The low temperature of the low efficiency that is shone of matter temperature, and avoid condensing insufficient or condense the too low efficiency reduction that shines, from
And improve heat energy transformation efficiency.
By in above-described embodiment can the dynamic system of heat energy of steady wet test, heat source temperature is respectively
120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 350 DEG C, the ambient temperature of condenser 4 is 25 DEG C, refrigerant flow rate in circulation pipe
According to can the operation stability of the steady dynamic system of heat energy of wet be adjusted；Experiment effect is：Heat source temperature is 120 DEG C,
Heat energy transformation efficiency is about 16%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 18%, when heat source temperature is 200 DEG C,
Heat energy transformation efficiency is about 23%, and heat source temperature is that 250 DEG C, heat energy transformation efficiency is about 28%, when heat source temperature is 300 DEG C, heat
Energy transformation efficiency is about 33%, and when heat source temperature is 350 DEG C, heat energy transformation efficiency is about 35%；In 120-350 DEG C of thermal source section, this
In embodiment can the comprehensive heat energy transformation efficiency of the steady dynamic system of heat energy of wet be about 26%；With respect to embodiment one, heat energy turns
Change improved efficiency about 8%.
Embodiment seven（As shown in Figure 7）：It is with one difference of embodiment：The condenser 4 also includes collecting tank
45, collecting tank 45 is used for collecting the condensed fluid in condenser 4；The collecting tank 45 is located at the afterbody of condenser 4.
Using said structure, can effectively prevent liquid refrigerant in condenser 4 from mixing a large amount of gases, it is to avoid part working medium without
Condensation liquefaction enters booster pump 3, can preferably increase media expansion heat absorption, increase amount of work, improve heat energy transformation efficiency.
By in above-described embodiment can the dynamic system of heat energy of steady wet test, heat source temperature is respectively
120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 350 DEG C, the ambient temperature of condenser 4 is 25 DEG C, refrigerant flow rate in circulation pipe
According to can the operation stability of the steady dynamic system of heat energy of wet be adjusted；Experiment effect is：Heat source temperature is 120 DEG C,
Heat energy transformation efficiency is about 14%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 16%, when heat source temperature is 200 DEG C,
Heat energy transformation efficiency is about 21%, and heat source temperature is that 250 DEG C, heat energy transformation efficiency is about 26%, when heat source temperature is 300 DEG C, heat
Energy transformation efficiency is about 31%, and when heat source temperature is 350 DEG C, heat energy transformation efficiency is about 33%；In 120-350 DEG C of thermal source section, this
In embodiment can the comprehensive heat energy transformation efficiency of the steady dynamic system of heat energy of wet be about 24%；With respect to embodiment one, heat energy turns
Change improved efficiency about 6%.
Embodiment eight（As shown in Figure 8）：It is with one difference of embodiment：The front end of the gasification reactor 2 also sets
It is equipped with preheating cavity 24；The preheating cavity 24 is looped around 2 periphery of gasification reactor；The helically type of the preheating cavity 24.
Using said structure, the outer heat extraction energy of 2 periphery of gasification reactor can be made full use of, is reduced thermal waste, improve heat energy
Transformation efficiency.
By in above-described embodiment can the dynamic system of heat energy of steady wet test, heat source temperature is respectively
120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 350 DEG C, the ambient temperature of condenser 4 is 25 DEG C, refrigerant flow rate in circulation pipe
According to can the operation stability of the steady dynamic system of heat energy of wet be adjusted；Experiment effect is：Heat source temperature is 120 DEG C,
Heat energy transformation efficiency is about 15%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 17%, when heat source temperature is 200 DEG C,
Heat energy transformation efficiency is about 22%, and heat source temperature is that 250 DEG C, heat energy transformation efficiency is about 27%, when heat source temperature is 300 DEG C, heat
Energy transformation efficiency is about 32%, and when heat source temperature is 350 DEG C, heat energy transformation efficiency is about 34%；In 120-350 DEG C of thermal source section, this
In embodiment can the comprehensive heat energy transformation efficiency of the steady dynamic system of heat energy of wet be about 25%；With respect to embodiment one, heat energy turns
Change improved efficiency about 7%.
Embodiment nine（As shown in Figure 9）：It is with one difference of embodiment：Acting 3 exhaust ports of pump are provided with
Preliminary condensation chamber 301；The preliminary condensation chamber 301 adopts air-cooled or water-cooled.
Take said structure, it is possible to increase air inlet and the pressure reduction of air vent, improve the heat energy transformation efficiency of acting pump 3.
By in above-described embodiment can the dynamic system of heat energy of steady wet test, heat source temperature is respectively
120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 350 DEG C, the ambient temperature of condenser 4 is 25 DEG C, refrigerant flow rate in circulation pipe
According to can the operation stability of the steady dynamic system of heat energy of wet be adjusted；Experiment effect is：Heat source temperature is 120 DEG C,
Heat energy transformation efficiency is about 14%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 16%, when heat source temperature is 200 DEG C,
Heat energy transformation efficiency is about 21%, and heat source temperature is that 250 DEG C, heat energy transformation efficiency is about 26%, when heat source temperature is 300 DEG C, heat
Energy transformation efficiency is about 31%, and when heat source temperature is 350 DEG C, heat energy transformation efficiency is about 33%；In 120-350 DEG C of thermal source section, this
In embodiment can the comprehensive heat energy transformation efficiency of the steady dynamic system of heat energy of wet be about 24%；With respect to embodiment one, heat energy turns
Change improved efficiency about 6%.
Embodiment ten（As shown in Figure 10）：It is with one difference of embodiment：The preheating cavity 24 and preliminary condensation chamber 301
Paratactic contact；
Said structure is taken, as working medium needs heat absorption in preheating cavity 24, and in preliminary condensation chamber 301, working medium needs heat extraction, the knot
Structure largely recycles working medium heat in circulating line, increases thermal transition efficiency.
By in above-described embodiment can the dynamic system of heat energy of steady wet test, heat source temperature is respectively
120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 350 DEG C, the ambient temperature of condenser 4 is 25 DEG C, refrigerant flow rate in circulation pipe
According to can the operation stability of the steady dynamic system of heat energy of wet be adjusted；Experiment effect is：Heat source temperature is 120 DEG C,
Heat energy transformation efficiency is about 17%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 19%, when heat source temperature is 200 DEG C,
Heat energy transformation efficiency is about 24%, and heat source temperature is that 250 DEG C, heat energy transformation efficiency is about 29%, when heat source temperature is 300 DEG C, heat
Energy transformation efficiency is about 33%, and when heat source temperature is 350 DEG C, heat energy transformation efficiency is about 36%；In 120-350 DEG C of thermal source section, this
In embodiment can the comprehensive heat energy transformation efficiency of the steady dynamic system of heat energy of wet be about 27%；With respect to embodiment one, heat energy turns
Change improved efficiency about 9%.
Embodiment 11（As shown in figure 11）：It is with one difference of embodiment：One is provided with the condenser 4
Negative pressure pump 46, negative pressure pump 46 is arranged on condensing tube middle-end.
Take said structure, it is possible to decrease the pressure of acting 3 port of export of pump, increase acting pump 3 into and out of two ends pressure reduction, so as to
Increase the amount of work of acting pump 3, reduce the interior energy after working medium acting, the condensing rate of working medium is improved, and improves heat energy efficiency.
By in above-described embodiment can the dynamic system of heat energy of steady wet test, heat source temperature is respectively
120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 350 DEG C, the ambient temperature of condenser 4 is 25 DEG C, refrigerant flow rate in circulation pipe
According to can the operation stability of the steady dynamic system of heat energy of wet be adjusted；Experiment effect is：Heat source temperature is 120 DEG C,
Heat energy transformation efficiency is about 16%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 18%, when heat source temperature is 200 DEG C,
Heat energy transformation efficiency is about 23%, and heat source temperature is that 250 DEG C, heat energy transformation efficiency is about 28%, when heat source temperature is 300 DEG C, heat
Energy transformation efficiency is about 33%, and when heat source temperature is 350 DEG C, heat energy transformation efficiency is about 35%；In 120-350 DEG C of thermal source section, this
In embodiment can the comprehensive heat energy transformation efficiency of the steady dynamic system of heat energy of wet be about 26%；With respect to embodiment one, heat energy turns
Change improved efficiency about 8%.
Embodiment 12（As shown in figure 12）：It is with one difference of embodiment：It is provided with the condenser 4 multiple
Negative pressure pump 46, negative pressure pump 46 is evenly distributed in condensing tube；
Take said structure, it is possible to decrease the pressure of acting 3 port of export of pump, largely pressure difference is improved, preferably can realize
Fractional condensaion, and reduce energy consumption needed for supercharging.
By in above-described embodiment can the dynamic system of heat energy of steady wet test, heat source temperature is respectively
120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 350 DEG C, the ambient temperature of condenser 4 is 25 DEG C, refrigerant flow rate in circulation pipe
According to can the operation stability of the steady dynamic system of heat energy of wet be adjusted；Experiment effect is：Heat source temperature is 120 DEG C,
Heat energy transformation efficiency is about 17%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 19%, when heat source temperature is 200 DEG C,
Heat energy transformation efficiency is about 24%, and heat source temperature is that 250 DEG C, heat energy transformation efficiency is about 29%, when heat source temperature is 300 DEG C, heat
Energy transformation efficiency is about 34%, and when heat source temperature is 350 DEG C, heat energy transformation efficiency is about 36%；In 120-350 DEG C of thermal source section, this
In embodiment can the comprehensive heat energy transformation efficiency of the steady dynamic system of heat energy of wet be about 27%；With respect to embodiment one, heat energy turns
Change improved efficiency about 9%.
Embodiment 13：It is with one difference of embodiment：Include four layers of cavity 21 in the gasification reactor 2；Institute
Cavity 21 is stated comprising inner chamber 211, exocoel 212 and lumen 213, the inside and outside end of lumen 213 connects inner chamber 211, exocoel 212 respectively；
Include multiple lumens 213, the fan-shaped distribution of lumen 213 between the inner chamber 211 and exocoel 212.
The acting pump 3 includes circular cavity 31, eccentric blade 32 and grooved runner 33, and grooved runner 33 is eccentrically mounted at circle
In the eccentric shaft 311 in shape chamber 31, the side of grooved runner 33 offers draw-in groove 34, and eccentric blade 32 is arranged on by spring leaf 35
Draw-in groove 34, the side of circular cavity 31 is respectively arranged with air inlet 36 and gas outlet 37, the pitch angle of air inlet 36 and gas outlet 37
Degree is more than the pitch angles between adjacent two eccentric blades 32；The side of the circular cavity 31 is provided with multiple gas outlets 37, gives vent to anger
Mouth 37 is with the pitch angles of air inlet 36 more than the pitch angles between adjacent two eccentric blades 32；The eccentric leaf of the acting pump 3
Piece 32 includes four.
The condenser 4 adopts the cold mode of liquid, and the condenser 4 includes condensing tube 41 and four condensation chambers 42, and two cold
Connected by many condensing tubes 41 between solidifying chamber 42；The condensing tube 41 is curvilinear；The condensing tube 41 is twist.
The condenser 4 adopts air cooling way, and the condensing units 4 include condensing tube 41, fin 43 and heat emission fan 44,
41 periphery of condensing tube installed by fin 43, and heat emission fan 44 is located above or below condensing tube 41 or side, and heat emission fan 44 is to take out
Wind mode or pressure wind mode drive；The condensing tube 41 in multilamellar or multiple rows of distribution, the mutual UNICOM of condensing tube 41；The condensing tube
41 are made by thermo-electric generation sheet 411；The thermo-electric generation sheet 411 includes sheet metal 412, p-type semiconductor 413, n-type semiconductor
414th, dielectric substrate layer 415 and output electrode 416, dielectric substrate layer 415 is uniformly interspersed with p-type semiconductor 413 and n-type semiconductor
414, equally distributed p-type semiconductor 413 and n-type semiconductor 414 are connected by sheet metal 412, p-type semiconductor 413 and N-shaped half
The series connection whole story end of conductor 414 connects output electrode 416 respectively.
The circulating line 6 is connected with regulating system 61, and regulating system 61 includes pressure regulator 611, temperature sensor
612 and medium actuator 613, temperature sensor 612 in gasification reactor 2, the control connection pressure of pressure regulator 611
Pump 5, medium actuator 613 is arranged in circulating line 6, for adjusting rate-of flow；The regulating system 61 also includes two
Pressure transducer 614, two pressure transducers 614 are separately mounted to the import and export end of acting pump 3.
The condenser 4 also includes collecting tank 45, and collecting tank 45 is used for collecting the condensed fluid in condenser 4；The collection
Liquid bath 45 is located at the afterbody of condenser 4.
The front end of the gasification reactor 2 is additionally provided with preheating cavity 24；The preheating cavity 24 is looped around gasification reactor 2 weeks
Side；The helically type of the preheating cavity 24.
Acting 3 exhaust ports of pump are provided with preliminary condensation chamber 301；The preliminary condensation chamber 301 adopts air-cooled or water-cooled.
A negative pressure pump 46 is provided with the condenser 4, negative pressure pump 46 is arranged on condensing tube middle-end.
In the gasification reactor 2, energy storage equipment 25 is installed；The energy storage equipment 25 is made using high heat capacity material；Institute
Energy storage equipment 25 is stated for closing water body.
Said structure is taken, the temperature of 2 inner chamber body 21 of gasification reactor can be stablized, so as to stablize gasification temperature.
By in above-described embodiment can the dynamic system of heat energy of steady wet test, heat source temperature is respectively
120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 350 DEG C, the ambient temperature of condenser 4 is 25 DEG C, refrigerant flow rate in circulation pipe
According to can the operation stability of the steady dynamic system of heat energy of wet be adjusted；Experiment effect is：Heat source temperature is 120 DEG C,
Heat energy transformation efficiency is about 21%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 23%, when heat source temperature is 200 DEG C,
Heat energy transformation efficiency is about 28%, and heat source temperature is that 250 DEG C, heat energy transformation efficiency is about 33%, when heat source temperature is 300 DEG C, heat
Energy transformation efficiency is about 38%, and when heat source temperature is 350 DEG C, heat energy transformation efficiency is about 40%；In 120-350 DEG C of thermal source section, this
In embodiment can the comprehensive heat energy transformation efficiency of the steady dynamic system of heat energy of wet be about 31%；With respect to embodiment one, heat energy turns
Change improved efficiency about 13%.
Finally it should be noted that：The preferred embodiments of the present invention are the foregoing is only, the present invention are not limited to,
Although being described in detail to the present invention with reference to the foregoing embodiments, for a person skilled in the art, which still may be used
To modify to the technical scheme described in foregoing embodiments, or equivalent is carried out to which part technical characteristic,
All any modification, equivalent substitution and improvement that within the spirit and principles in the present invention, is made etc., should be included in the present invention's
Within protection domain.
Claims (8)
1. a kind of can steady wet dynamic system of heat energy, including thermal source (1), gasification reactor (2), acting pump (3), condenser
(4), compression pump (5) and circulating line (6), gasification reactor (2), acting pump (3), condenser (4) and compression pump (5) are by following
Circulation UNICOM, gasification reactor (2) contact thermal source (1) are realized in endless tube road (6), it is characterised in that：In gasification reactor (2)
Energy storage equipment (25) is installed.
2. according to claim 1 can steady wet dynamic system of heat energy, it is characterized in that：Energy storage equipment (25) adopt
Made with high heat capacity material.
3. according to claim 2 can steady wet dynamic system of heat energy, it is characterized in that：Energy storage equipment (25) are
Closing water body.
4. according to claim 1 can steady wet dynamic system of heat energy, it is characterized in that：Gasification reactor (2)
Including multiple cavities（21）, cavity（21）Including inner chamber (211), exocoel (212) and lumen (213), inner chamber (211) and exocoel
(212) pass through lumen (213) UNICOM between, thermal source (1) is circulated between inner chamber (211) and exocoel (212).
5. according to claim 1 can steady wet dynamic system of heat energy, it is characterized in that：Inner chamber (211) with outer
Include multiple lumen (213) between chamber (212), the fan-shaped distribution of lumen (213).
6. according to claim 4 can steady wet dynamic system of heat energy, it is characterized in that：Described inner chamber (211) are in ring
Shape, described energy storage equipment (25) are in the middle part of inner chamber (211).
7. according to claim 4 can steady wet dynamic system of heat energy, it is characterized in that：Described energy storage equipment (25) pacify
It is mounted in the outer layer of exocoel (212).
8. according to claim 7 can steady wet dynamic system of heat energy, it is characterized in that：Energy storage equipment (25) with
Exocoel (212) is flexibly connected, and energy storage equipment (25) is detachable.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108533328A (en) * | 2018-04-28 | 2018-09-14 | 曹连国 | A kind of new type low temperature steam engine inversely applied based on air-conditioning principle |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108533328A (en) * | 2018-04-28 | 2018-09-14 | 曹连国 | A kind of new type low temperature steam engine inversely applied based on air-conditioning principle |
| WO2019205486A1 (en) * | 2018-04-28 | 2019-10-31 | Cao Lianguo | Novel steam engine based on reverse application of air conditioning principle |
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Application publication date: 20170222 |