CN106224039A - A kind of dynamic system of heat energy comprehensively utilizing acting pump waste heat - Google Patents
A kind of dynamic system of heat energy comprehensively utilizing acting pump waste heat Download PDFInfo
- Publication number
- CN106224039A CN106224039A CN201610762065.9A CN201610762065A CN106224039A CN 106224039 A CN106224039 A CN 106224039A CN 201610762065 A CN201610762065 A CN 201610762065A CN 106224039 A CN106224039 A CN 106224039A
- Authority
- CN
- China
- Prior art keywords
- heat energy
- heat
- acting pump
- transformation efficiency
- dynamic system
- Prior art date
- Legal status (The legal status 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 status listed.)
- Pending
Links
- 239000002918 waste heat Substances 0.000 title claims abstract description 62
- 238000002309 gasification Methods 0.000 claims abstract description 82
- 238000009833 condensation Methods 0.000 claims abstract description 44
- 230000005494 condensation Effects 0.000 claims abstract description 44
- 230000006835 compression Effects 0.000 claims abstract description 13
- 238000007906 compression Methods 0.000 claims abstract description 13
- 230000008676 import Effects 0.000 claims description 6
- 230000009466 transformation Effects 0.000 abstract description 123
- 230000009467 reduction Effects 0.000 abstract description 6
- 230000010512 thermal transition Effects 0.000 abstract description 4
- 239000004065 semiconductor Substances 0.000 description 28
- 239000007789 gas Substances 0.000 description 20
- 230000000694 effects Effects 0.000 description 19
- 230000033228 biological regulation Effects 0.000 description 14
- 238000002474 experimental method Methods 0.000 description 14
- 239000007788 liquid Substances 0.000 description 13
- 238000004146 energy storage Methods 0.000 description 10
- 239000012530 fluid Substances 0.000 description 10
- 238000009434 installation Methods 0.000 description 9
- 238000000034 method Methods 0.000 description 9
- 230000008569 process Effects 0.000 description 8
- 238000010586 diagram Methods 0.000 description 7
- 239000002184 metal Substances 0.000 description 7
- 239000003507 refrigerant Substances 0.000 description 7
- 239000000758 substrate Substances 0.000 description 7
- 238000009826 distribution Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 238000000605 extraction Methods 0.000 description 4
- 230000001105 regulatory effect Effects 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 206010010904 Convulsion Diseases 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 230000036461 convulsion Effects 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000007710 freezing Methods 0.000 description 3
- 230000008014 freezing Effects 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000006199 nebulizer Substances 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 101100493713 Caenorhabditis elegans bath-45 gene Proteins 0.000 description 1
- 241001582888 Lobus Species 0.000 description 1
- 238000002835 absorbance Methods 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000005183 dynamical system Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 230000035800 maturation Effects 0.000 description 1
- 238000004377 microelectronic Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 238000005381 potential energy Methods 0.000 description 1
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- -1 thermal source 1 Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01C—ROTARY-PISTON OR OSCILLATING-PISTON MACHINES OR ENGINES
- F01C1/00—Rotary-piston machines or engines
- F01C1/30—Rotary-piston machines or engines having the characteristics covered by two or more groups F01C1/02, F01C1/08, F01C1/22, F01C1/24 or having the characteristics covered by one of these groups together with some other type of movement between co-operating members
- F01C1/34—Rotary-piston machines or engines having the characteristics covered by two or more groups F01C1/02, F01C1/08, F01C1/22, F01C1/24 or having the characteristics covered by one of these groups together with some other type of movement between co-operating members having the movement defined in group F01C1/08 or F01C1/22 and relative reciprocation between the co-operating members
- F01C1/344—Rotary-piston machines or engines having the characteristics covered by two or more groups F01C1/02, F01C1/08, F01C1/22, F01C1/24 or having the characteristics covered by one of these groups together with some other type of movement between co-operating members having the movement defined in group F01C1/08 or F01C1/22 and relative reciprocation between the co-operating members with vanes reciprocating with respect to the inner member
- F01C1/3446—Rotary-piston machines or engines having the characteristics covered by two or more groups F01C1/02, F01C1/08, F01C1/22, F01C1/24 or having the characteristics covered by one of these groups together with some other type of movement between co-operating members having the movement defined in group F01C1/08 or F01C1/22 and relative reciprocation between the co-operating members with vanes reciprocating with respect to the inner member the inner and outer member being in contact along more than one line or surface
-
- 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
-
- 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
-
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B1/00—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
- F28B1/06—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using air or other gas as the cooling medium
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
The invention discloses a kind of dynamic system of heat energy comprehensively utilizing acting pump waste heat, including thermal source, gasification reactor, acting pump, condenser, compression pump and circulating line, gasification reactor, acting pump, condenser and compression pump realize circulation UNICOM by circulating line, gasification reactor contact thermal source, the front end of described gasification reactor is additionally provided with preheating cavity, preliminary condensation chamber, described preheating cavity and preliminary condensation chamber paratactic contact it is provided with at described acting pump exhaust inlet；The dynamic system of heat energy of comprehensive utilization acting pump waste heat of the present invention can increase the pressure reduction of acting pump steam inlet and air vent, improves the transformation efficiency of turbine, working medium heat in integrated reuse-recycle pipeline simultaneously, increases thermal transition efficiency.
Description
Technical field
The invention belongs to utilization of energy apparatus field, a kind of thermal power system comprehensively utilizing acting pump waste heat
System.
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 along with improvement and the replacement of the energy.The exploitation of the energy greatly advance the world
Economy and the development of human society.
But along with the consumption that is continuously developed of the energy, the non-renewable energy resources such as oil, colliery, natural gas progressively tighten, energy
The saving in source and recycling progressively is taken seriously.For response national energy-saving strategy, increasing enterprise starts research and development, uses joint
Energy equipment, and strengthen discarded production capacity thing, the utilization of waste heat energy.Wherein, utilize aspect at waste heat, mainly pass through heat energy power-generating
Equipment realizes 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, changes into heat energy mechanical energy, then changes mechanical energy is become electric energy, and the generating equipment of this kind of principle classification is relatively
For maturation, kind is many；Another kind of is to utilize pyroelectric effect principle, by thermoelectric conversion element, heat energy is directly translated into electromotive force
Can, but due to immature for generation technology aspect, electrical power is little, and manufacturing cost is high, and thermoelectric conversion efficiency is low, is mainly used in
Microelectronic.
Present stage, most enterprises is big due to complementary energy eliminating amount, in the utilization of waste heat, the most also needs to rely on above-mentioned first
Class thermal generating equipment, changes into heat energy mechanical energy by gas expansion for doing work, then changes mechanical energy is become electric energy.Existing
Such thermal generating equipment mainly includes gasification installation, turbine, electromotor and condensing unit；During work, cycle fluid is following
Endless tube first passes through gasification installation in road, working medium is gasified and promotes turbine to rotate, and the working medium after gasification is passing through turbine
Time, externally doing work, temperature and air pressure can reduce, and are cooled to liquid refrigerant by condensing unit.
The existing heat energy utilization equipment utilizing gas expansion for doing work, in the ideal case, the maximum rate that its heat energy converts 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 gasification in gasification installation, the actual temperature of its gasification expansion and high temperature heat source temperature
The temperature difference of degree is relatively big, and actual temperature is lower than high temperature heat source temperature, the T of its theory1Drop little, cause heat energy peak efficiency to reduce；Separately
On the one hand, owing to the cycle fluid actual condensation temperature in condensing unit is higher than low temperature cold source temperature, the T of its theory0Increase,
Heat energy peak efficiency is caused to reduce；Additionally, due to turbine is on the low side to the absorbance of gas expansion for doing work, its changes mechanical energy is imitated
Rate is relatively low；It addition, impurity easily occurs in cycle fluid, cycle fluid power consumption is bigger.
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 of high temperature heat source is high；2. the pressure of gasification installation is unstable, and gasify temperature required instability, when the required temperature of gasification
Degree more than heat source temperature time, medium cannot realize gasification, when gasify temperature required less than heat source temperature time, gasification expansion temperature inclined
Low, to absorb heat less, net work amount diminishes；3. in condensing unit, the pressure of medium is unstable, condenses temperature required instability, when cold
Solidifying temperature required less than sink temperature time, it is impossible to realize condensation, when condense temperature required more than sink temperature time, temperature after condensation
Too low；4. the condensation in condensing unit is incomplete, gas-liquid mixed state easily occurs, causes its working medium gasifying in gasification installation
Expansion volume is less than normal；The most existing turbine torsion is less than normal, and volumetric leak amount is big, inefficient；The heat energy of the most existing thermal hardware
Transformation efficiency is on the low side, and heat energy transformation efficiency is generally 10% to 30%；7. working medium is apt to deteriorate or impurity occurs.
Summary of the invention
The purpose that the present invention is to be realized is: improve heat energy transformation efficiency, improves working medium rate of gasification in gasification installation,
Increase the drive of turbine, improve turbine efficiency, stablize working medium gasification temperature and refrigerant flow rate, improve working medium quality, anti-
Only working medium goes bad, and improves turbine structure, it is to avoid turbine is revealed and rotary speed unstabilization, improves condensing unit, accelerates condensing rate, subtracts
The thermal waste of little condensation process；Existing for existing thermal hardware in the above-mentioned background technology of solution: 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 the best, working medium apt to deteriorate or
Impurity occur, the thermal waste of condensing unit is big, condensing rate slow or needs the problems such as extra power consumption.
For solving its technical problem the technical solution adopted in the present invention it is: a kind of heat energy comprehensively utilizing acting pump waste heat
Dynamical system, including thermal source, gasification reactor, acting pump, condenser, compression pump and circulating line, gasification reactor, acting
Pump, condenser and compression pump realize circulation UNICOM, gasification reactor contact thermal source by circulating line；
It is characterized in that: the front end of described gasification reactor is additionally provided with preheating cavity, is provided with pre-at described acting pump exhaust inlet
Condensation chamber, described preheating cavity and preliminary condensation chamber paratactic contact.
Take said structure can increase the pressure reduction of air inlet and air vent, improve the transformation efficiency of turbine；Simultaneously as
In preheating cavity, working medium needs heat absorption, and preliminary condensation intracavity working medium needs heat extraction, and this structure recycles circulating line largely
Interior working medium heat, increases thermal transition efficiency.
Further, described preheating cavity and preliminary condensation chamber spiral paratactic contact.
Further, described preheating cavity flows to contrary with the working medium in preliminary condensation chamber.
Further, the import and export two ends of described preheating cavity are provided with flow velocity display table.
Further, described preheating cavity is additionally provided with flow control valve.
Further, described current limliting pressure charging valve uses manual type flow control valve.
Further, described current limliting pressure charging valve uses electric-controlled type flow control valve.
Further, it is provided with preliminary condensation chamber at described acting pump exhaust inlet；
Further, at least one of which cavity is included in described gasification reactor.
Further, one layer of cavity is included in described gasification reactor.
Further, two-layer cavity is included in described gasification reactor.
Further, at least four layers of cavity are included in described gasification reactor.
Further, described cavity comprises inner chamber, exocoel and lumen, and the inside and outside end of lumen connects inner chamber, exocoel respectively.
Using said structure, the heat conduction rate of its gasification reactor is greatly improved, and liquid refrigerant enters in cavity, can concentrate
Gasify rapidly in cavity portion region, can preferably avoid working medium gasification not exclusively.
Further, comprising multiple lumen between described inner chamber and exocoel, lumen sector is distributed.
Further, described cavity is ellipse.
Further, at least one of which cavity is included in described gasification reactor.
Further, described acting pump is impeller acting pump.
Further, described acting pump is vacuum acting pump.
Further, described acting pump is piston type acting pump.
Further, described 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 by spring leaf, the side of circular cavity
While be 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 described circular cavity is provided with multiple gas outlet, and gas outlet is more than with the pitch angles of air inlet
Adjacent two eccentric interlobate pitch angles.
Further, the moving vane of described revolving wormgear structure comprises at least three.
Further, described condenser is liquid-cooled freezing machine.
Further, described condenser includes condensing tube and multiple condensation chamber, cold by least one between two condensation chambers
Solidifying pipe connection.
Further, described condensing tube is curvilinear.
Further, described condensing tube is twist.
Further, described condenser is ventilation type freezing machine.
Further, described condensing unit includes condensing tube, fin and heat emission fan, and condensing tube periphery installed by fin, dissipates
Heat fan is positioned at above or below condensing tube or side, and heat emission fan drives with convulsion mode or pressure wind mode.
Further, described condensing tube is multilamellar or multiple rows of distribution, and the mutual UNICOM of condensing tube, heat emission fan is arranged on condensing tube
Side or lower section, heat emission fan drives with convulsion mode or pressure wind mode.
Further, the UNICOM direction of described condensing tube is in vertically or horizontally or tiltedly type.
Further, described condensing tube is made by thermo-electric generation sheet.
Further, described 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
Being connected by sheet metal, p-type semiconductor is connected output electrode respectively with the series connection end at the whole story of n-type semiconductor；
Further, the working medium in described circulating line uses pure water.
Further, the working medium in described circulating line uses propanol.
Further, the working medium in described circulating line uses methanol.
Further, the working medium in described circulating line uses ethanol.
Further, the working medium in described circulating line uses isopropanol.
Further, the working medium in described circulating line uses liquefied ammonia.
Further, the working medium in described circulating line uses freon.
Further, described circulating line connect have regulation system, regulation system include pressure regulator, temperature sensor and
Medium actuator, temperature sensor is arranged in gasification reactor, and pressure regulator controls to connect compression pump, and medium actuator is pacified
It is contained in circulating line, is used for regulating rate-of flow.
Further, described regulation system also includes multiple pressure transducer, and pressure transducer is evenly distributed on circulating line
In.
Further, described regulation system also includes that two pressure transducers, two pressure transducers are separately mounted to acting
The import and export end of pump.
Further, it is evenly distributed with pressure transducer in described regulation system.
Using said structure, when in gasification reactor, the temperature of working medium changes, regulation system is regulated by pressure
Device and medium actuator regulate sender matter pressure and flow velocity so that it is temperature province temperature.
Further, it is provided with temperature inductor in described gasification reactor
Further, described condenser also includes collecting tank, and collecting tank is for collecting the condensed fluid in condenser.
Use said structure, can effectively prevent liquid refrigerant in condenser from mixing a large amount of gas, cause part working medium without
Condensation liquefaction enters booster pump.
Further, described collecting tank is positioned at the afterbody of condenser.
Further, the entrance point of described gasification reactor is additionally provided with nebulizer.
Further, the front end of described gasification reactor is additionally provided with preheating cavity；
Use said structure to may utilize the outer heat extraction energy of gasification reactor periphery, reduce thermal waste.
Further, described preheating cavity is looped around gasification reactor periphery.
Further, described preheating cavity helically type.
Further, being provided with a negative pressure pump in described condenser, negative pressure pump is arranged on condensing tube middle-end；
Taking said structure, it is possible to decrease the pressure of acting pump discharge end, increase acting pump is into and out of two ends pressure reduction, thus increases and do
The amount of work of merit pump, reduces the interior energy after working medium acting, improves the condensing rate of working medium, and improve heat energy efficiency.
Further, being provided with multiple negative pressure pump in described condenser, negative pressure pump is evenly distributed in condensing tube；
Take said structure, it is possible to decrease the pressure of acting pump discharge end, improve pressure difference largely, can preferably realize point
Level condensation, and reduce energy consumption needed for supercharging.
Further, in described gasification reactor, energy storage equipment is installed.
Further, described energy storage equipment uses high heat capacity material to make.
Further, described energy storage equipment is for closing water body.
Take said structure, the temperature of gasification reactor inner chamber body can be stablized, thus stablize gasification temperature.
Further, contaminant filter pump it is additionally provided with between described condenser and compression pump.
Operation principle is as follows:
The dynamic system of heat energy of this invention described comprehensive utilization acting pump waste heat, during work, cycle fluid absorbs heat in thermal source and reaches
To high temperature heat source temperature, then flow in gasification reactor, flow to, after working medium gasification, the pump that does work；After gasification working medium flows through acting pump,
Due to externally acting, its Temperature of Working and air pressure all can reduce, and cause part working medium to liquefy；Gasification working medium flows through acting pump
After, working medium flows to condenser and compression pump successively；Working medium, after compression pump supercharging, is again introduced into gasification reactor, completes one
Circulation.
Beneficial effect: the dynamic system of heat energy of comprehensive utilization of the present invention acting pump waste heat, in hinge structure
Heat energy machine, there is advantage and the progress of following several respects: 1. improve the heat conduction rate of cavity, preferably avoid working medium liquid to exist
In gasification installation, gasification is not exclusively；Increase turbine the most largely turns power, and has output power evenly；3. have
Effect avoids condensation not exclusively, reduces intracavity pressure, improves efficiency；4. can stablize working medium gasification temperature and refrigerant flow rate, can have
Effect improves gasification usefulness and condensation efficiency；5. make full use of waste heat, increase thermal source heat absorption, increase amount of work, improve heat energy and convert
Efficiency；6. recycle working medium heat in circulating line, increase thermal transition efficiency largely；7. improve working medium pure
Degree, effectively prevents the pump leakage problem that does work.
Accompanying drawing explanation
Fig. 1 is the integrated connection theory structure schematic diagram of the embodiment of the present invention one；
Fig. 2 is the preliminary condensation chamber attachment structure schematic diagram with preheating cavity 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 gasification reactor structural representation 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；
Figure 13 is the gasification reactor structural representation of the embodiment of the present invention 13；
In figure:
1 is thermal source；
2 it is gasification reactor, 21 is cavity, 211 is inner chamber, 212 is exocoel, 213 is lumen, 22 is temperature inductor, 23 is
Nebulizer, 24 be preheating cavity, 241 be flow velocity display table, 242 be flow control valve, 25 for energy storage equipment；
3 be acting pump, 301 be preliminary condensation chamber, 31 be circular cavity, 311 be eccentric shaft, 32 be eccentric blade, 33 be grooved runner,
34 be draw-in groove, 35 be spring leaf, 36 be air inlet, 37 for gas outlet；
4 be condenser, 41 be condensing tube, 411 be thermo-electric generation sheet, 412 be sheet metal, 413 be p-type semiconductor, 414 for N-shaped
Quasiconductor, 415 be dielectric substrate layer, 416 for output electrode, 42 for condensation chamber, 43 for fin, 44 for heat emission fan, 45 for collection
Liquid bath, 46 it is negative pressure pump；
5 is compression pump；
6 be circulating line, 61 for regulation system, 611 for pressure regulator, 612 for temperature sensor, 613 for medium actuator,
614 is pressure transducer.
Detailed description of the invention
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
Describe wholely；Obviously, described embodiment is only a part of embodiment of the present invention rather than whole embodiments.Based on
Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under not making creative work premise
Embodiment, broadly falls into the scope of protection of the invention.
Embodiment one (as shown in Figure 1): a kind of dynamic system of heat energy comprehensively utilizing acting pump waste heat, including thermal source 1, gas
Change reactor 2, acting pump 3, condenser 4, compression pump 5 and circulating line 6, gasification reactor 2, acting pump 3, condenser 4 and pressure
Power pump 5 realizes circulation UNICOM by circulating line 6, and gasification reactor 2 contacts thermal source 1；
As illustrating of above-mentioned implementation process, high-temperature fuel gas in the employing of described thermal source 1.
As illustrating of above-mentioned implementation process, in described gasification reactor 2, include one layer of cavity 21；Described cavity 21
In ellipse.
As illustrating of above-mentioned implementation process, described acting pump 3 is impeller acting pump.
As illustrating of above-mentioned implementation process, described condenser 4 is ventilation type freezing machine.
As illustrating of above-mentioned implementation process, described compression pump 5 is liquid pressure pump.
As illustrating of above-mentioned implementation process, the working medium in described circulating line 6 uses pure water.
By the dynamic system of heat energy of the comprehensive utilization acting pump waste heat in above-described embodiment is tested, heat source temperature
Being 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, work in circulation pipe
Mass flow speed is adjusted according to the operation stability of the dynamic system of heat energy of comprehensive utilization acting pump waste heat；Experiment effect is: heat
Source temperature is 120 DEG C, and heat energy transformation efficiency is about 8%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 10%, thermal source temperature
When degree is 200 DEG C, heat energy transformation efficiency is about 15%, and heat source temperature is 250 DEG C, and heat energy transformation efficiency is about 20%, heat source temperature
When being 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%；At 120-350
DEG C thermal source section, in the present embodiment, the comprehensive heat energy transformation efficiency of the dynamic system of heat energy of comprehensive utilization acting pump waste heat is about 18%.
Embodiment two (as shown in Figure 2): be with embodiment one difference: the front end of described gasification reactor 2 also sets
Being equipped with preheating cavity 24, described acting pump 3 exhaust ports is provided with preliminary condensation chamber 301, and described preheating cavity 24 is with preliminary condensation chamber 301 also
Row contact；Described preheating cavity 24 and preliminary condensation chamber 301 spiral paratactic contact；Described preheating cavity 24 and the working medium in preliminary condensation chamber 301
Flow to contrary；The import and export two ends of described preheating cavity 24 are provided with flow velocity display table 241；Described preheating cavity 24 is additionally provided with
Flow control valve 242；Described current limliting pressure charging valve 242 uses electric-controlled type flow control valve.
Taking said structure, owing in preheating cavity 24, working medium needs heat absorption, and in preliminary condensation chamber 301, working medium needs heat extraction,
This structure recycles working medium heat in circulating line largely, increases thermal transition efficiency.
By the dynamic system of heat energy of the comprehensive utilization acting pump waste heat in above-described embodiment is tested, heat source temperature
Being 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, work in circulation pipe
Mass flow speed is adjusted according to the operation stability of the dynamic system of heat energy of comprehensive utilization acting pump waste heat；Experiment effect is: heat
Source temperature is 120 DEG C, and heat energy transformation efficiency is about 12%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 14%, thermal source
When temperature is 200 DEG C, heat energy transformation efficiency is about 19%, and heat source temperature is 250 DEG C, and heat energy transformation efficiency is about 24%, thermal source temperature
When degree 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%；At 120-
350 DEG C of thermal source sections, in the present embodiment, the comprehensive heat energy transformation efficiency of the dynamic system of heat energy of comprehensive utilization acting pump waste heat is about
22%；Embodiment one relatively, heat energy transformation efficiency promotes about 4%.
Embodiment three (as shown in Figure 3): be with embodiment one difference: described acting pump 3 includes circular cavity 31, partially
Lobus cardiacus sheet 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 more than the pitch angle between adjacent two eccentric blades 32 with the pitch angles of gas outlet 37
Degree；The side of described circular cavity 31 is provided with multiple gas outlet 37, and gas outlet 37 is more than adjacent with the pitch angles of air inlet 36
Pitch angles between two eccentric blades 32；The eccentric blade 32 of described acting pump 3 comprises four.
Use 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；Owing to the area of air inlet 36 both sides bias blade 32 is different, expansion chamber trends towards
Volume becomes general orientation and rotates, so that blade rotates；The vane stress of this kind of acting pump 3 is that gas-static is the poorest, and acting away from
From relatively big, the rotating vane acting pump 3(comparing routine is driven by fluid flowing generation pressure, namely gas-kinetic pressure is poor), tool
There is bigger thrust, can more fully hereinafter utilize kinetic energy and the potential energy of gasification working medium, there is preferable heat energy transformation efficiency.
By the dynamic system of heat energy of the comprehensive utilization acting pump waste heat in above-described embodiment is tested, heat source temperature
Being 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, work in circulation pipe
Mass flow speed is adjusted according to the operation stability of the dynamic system of heat energy of comprehensive utilization acting pump waste heat；Experiment effect is: heat
Source temperature is 120 DEG C, and heat energy transformation efficiency is about 14%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 16%, thermal source
When temperature is 200 DEG C, heat energy transformation efficiency is about 21%, and heat source temperature is 250 DEG C, and heat energy transformation efficiency is about 26%, thermal source temperature
When degree 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%；At 120-
350 DEG C of thermal source sections, in the present embodiment, the comprehensive heat energy transformation efficiency of the dynamic system of heat energy of comprehensive utilization acting pump waste heat is about
24%；Embodiment one relatively, heat energy transformation efficiency promotes about 6%.
Embodiment four (as shown in Figure 4): be with embodiment one difference: described condenser 4 uses the cold mode of liquid, institute
State condenser 4 and include condensing tube 41 and four condensation chambers 42, connected by many condensing tubes 41 between two condensation chambers 42；Described
Condensing tube 41 is curvilinear；Described condensing tube 41 is twist.
Use said structure, owing to the working medium in its condenser 4 is through repeatedly mixed flow and shunting, with extraneous contact area
Greatly, working medium can the air-liquid state that realizes in condensation chamber 42 separate, and can be prevented effectively from condensation not exclusively, reduce the pressure of condensation chamber 42
By force, improve the amount of work of acting pump 3, meanwhile, also can improve working medium expansion rate in the gasification reactor 2, thus improve effect
Rate.
By the dynamic system of heat energy of the comprehensive utilization acting pump waste heat in above-described embodiment is tested, heat source temperature
Being 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, work in circulation pipe
Mass flow speed is adjusted according to the operation stability of the dynamic system of heat energy of comprehensive utilization acting pump waste heat；Experiment effect is: heat
Source temperature is 120 DEG C, and heat energy transformation efficiency is about 13%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 15%, thermal source
When temperature is 200 DEG C, heat energy transformation efficiency is about 20%, and heat source temperature is 250 DEG C, and heat energy transformation efficiency is about 25%, thermal source temperature
When degree 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%；At 120-
350 DEG C of thermal source sections, in the present embodiment, the comprehensive heat energy transformation efficiency of the dynamic system of heat energy of comprehensive utilization acting pump waste heat is about
23%；Embodiment one relatively, heat energy transformation efficiency promotes about 5%.
Embodiment five (as shown in Figure 5): be with embodiment one difference: described condenser 4 uses air cooling way, institute
Stating condensing unit 4 and include condensing tube 41, fin 43 and heat emission fan 44, fin 43 installs condensing tube 41 periphery, heat emission fan 44
Being positioned at above or below condensing tube 41 or side, heat emission fan 44 drives with convulsion mode or pressure wind mode；Described condensing tube 41
In multilamellar or multiple rows of distribution, the mutual UNICOM of condensing tube 41；Described condensing tube 41 is made by thermo-electric generation sheet 411；The described temperature difference
Generating sheet 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 end at the whole story of n-type semiconductor 414
Electrode 416.
Use said structure, owing in its condenser 4, condensing tube 41 uses thermo-electric generation sheet 41, the p of thermo-electric generation sheet 41
Type quasiconductor 413 and n-type semiconductor 414, can produce electromotive force when there is the temperature difference at two ends, 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 realize voltage superposition, thus realize generating when p-type semiconductor 413 and n-type semiconductor 414 are connected；Therefore, the temperature difference
Its partial heat, while transmission heat, can be changed into electromotive force by generating sheet；This structure can preferably reduce heat-energy losses,
Improve heat energy transformation efficiency.
By the dynamic system of heat energy of the comprehensive utilization acting pump waste heat in above-described embodiment is tested, heat source temperature
Being 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, work in circulation pipe
Mass flow speed is adjusted according to the operation stability of the dynamic system of heat energy of comprehensive utilization acting pump waste heat；Experiment effect is: heat
Source temperature is 120 DEG C, and heat energy transformation efficiency is about 12%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 14%, thermal source
When temperature is 200 DEG C, heat energy transformation efficiency is about 19%, and heat source temperature is 250 DEG C, and heat energy transformation efficiency is about 24%, thermal source temperature
When degree 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%；At 120-
350 DEG C of thermal source sections, in the present embodiment, the comprehensive heat energy transformation efficiency of the dynamic system of heat energy of comprehensive utilization acting pump waste heat is about
22%；Embodiment one relatively, heat energy transformation efficiency promotes about 4%.
Embodiment six (as shown in Figure 6): be with embodiment one difference: described circulating line 6 is connected regulation system
System 61, regulation system 61 includes pressure regulator 611, temperature sensor 612 and medium actuator 613, and temperature sensor 612 is pacified
Being contained in gasification reactor 2, pressure regulator 611 controls to connect compression pump 5, and medium actuator 613 is arranged on circulating line 6
In, it is used for regulating rate-of flow；Described regulation system 61 also includes two pressure transducers 614, two pressure transducers 614 points
It is not arranged on the import and export end of acting pump 3.
Using said structure, when in gasification reactor 2, the temperature of working medium changes, regulation system 61 is adjusted by pressure
Joint device 611 and medium actuator 613 regulate sender matter pressure and flow velocity so that it is temperature province temperature stabilization, Jie that can preferably avoid
The efficiency temperature on the low side that matter temperature is on the low side is shone, and avoid condensing insufficient or condensing the too low usefulness shone reduction, from
And improve heat energy transformation efficiency.
By the dynamic system of heat energy of the comprehensive utilization acting pump waste heat in above-described embodiment is tested, heat source temperature
Being 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, work in circulation pipe
Mass flow speed is adjusted according to the operation stability of the dynamic system of heat energy of comprehensive utilization acting pump waste heat；Experiment effect is: heat
Source temperature is 120 DEG C, and heat energy transformation efficiency is about 16%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 18%, thermal source
When temperature is 200 DEG C, heat energy transformation efficiency is about 23%, and heat source temperature is 250 DEG C, and heat energy transformation efficiency is about 28%, thermal source temperature
When degree 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%；At 120-
350 DEG C of thermal source sections, in the present embodiment, the comprehensive heat energy transformation efficiency of the dynamic system of heat energy of comprehensive utilization acting pump waste heat is about
26%；Embodiment one relatively, heat energy transformation efficiency promotes about 8%.
Embodiment seven (as shown in Figure 7): be with embodiment one difference: described condenser 4 also includes collecting tank
45, collecting tank 45 is for collecting the condensed fluid in condenser 4；Described collecting tank 45 is positioned at the afterbody of condenser 4.
Use said structure, can effectively prevent liquid refrigerant in condenser 4 from mixing a large amount of gas, 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 the dynamic system of heat energy of the comprehensive utilization acting pump waste heat in above-described embodiment is tested, heat source temperature
Being 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, work in circulation pipe
Mass flow speed is adjusted according to the operation stability of the dynamic system of heat energy of comprehensive utilization acting pump waste heat；Experiment effect is: heat
Source temperature is 120 DEG C, and heat energy transformation efficiency is about 14%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 16%, thermal source
When temperature is 200 DEG C, heat energy transformation efficiency is about 21%, and heat source temperature is 250 DEG C, and heat energy transformation efficiency is about 26%, thermal source temperature
When degree 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%；At 120-
350 DEG C of thermal source sections, in the present embodiment, the comprehensive heat energy transformation efficiency of the dynamic system of heat energy of comprehensive utilization acting pump waste heat is about
24%；Embodiment one relatively, heat energy transformation efficiency promotes about 6%.
Embodiment eight (as shown in Figure 8): be with embodiment one difference: the front end of described gasification reactor 2 also sets
It is equipped with preheating cavity 24；Described preheating cavity 24 is looped around gasification reactor 2 periphery；Described preheating cavity 24 helically type.
Use said structure, the outer heat extraction energy of gasification reactor 2 periphery can be made full use of, reduce thermal waste, improve heat energy
Transformation efficiency.
By the dynamic system of heat energy of the comprehensive utilization acting pump waste heat in above-described embodiment is tested, heat source temperature
Being 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, work in circulation pipe
Mass flow speed is adjusted according to the operation stability of the dynamic system of heat energy of comprehensive utilization acting pump waste heat；Experiment effect is: heat
Source temperature is 120 DEG C, and heat energy transformation efficiency is about 15%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 17%, thermal source
When temperature is 200 DEG C, heat energy transformation efficiency is about 22%, and heat source temperature is 250 DEG C, and heat energy transformation efficiency is about 27%, thermal source temperature
When degree 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%；At 120-
350 DEG C of thermal source sections, in the present embodiment, the comprehensive heat energy transformation efficiency of the dynamic system of heat energy of comprehensive utilization acting pump waste heat is about
25%；Embodiment one relatively, heat energy transformation efficiency promotes about 7%.
Embodiment nine (as shown in Figure 9): be with embodiment one difference:
Described acting pump 3 exhaust ports is provided with preliminary condensation chamber 301；Described preliminary condensation chamber 301 uses 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 the dynamic system of heat energy of the comprehensive utilization acting pump waste heat in above-described embodiment is tested, heat source temperature
Being 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, work in circulation pipe
Mass flow speed is adjusted according to the operation stability of the dynamic system of heat energy of comprehensive utilization acting pump waste heat；Experiment effect is: heat
Source temperature is 120 DEG C, and heat energy transformation efficiency is about 14%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 16%, thermal source
When temperature is 200 DEG C, heat energy transformation efficiency is about 21%, and heat source temperature is 250 DEG C, and heat energy transformation efficiency is about 26%, thermal source temperature
When degree 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%；At 120-
350 DEG C of thermal source sections, in the present embodiment, the comprehensive heat energy transformation efficiency of the dynamic system of heat energy of comprehensive utilization acting pump waste heat is about
24%；Embodiment one relatively, heat energy transformation efficiency promotes about 6%.
Embodiment ten (as shown in Figure 10): be with embodiment one difference: include four layers in described gasification reactor 2
Cavity 21；Described cavity 21 comprises inner chamber 211, exocoel 212 and lumen 213, and the inside and outside end of lumen 213 connects inner chamber respectively
211, exocoel 212；Multiple lumen 213 is comprised, the fan-shaped distribution of lumen 213 between described inner chamber 211 and exocoel 212.
Using said structure, the heat conduction rate of its gasification reactor 2 is greatly improved, and liquid refrigerant enters in cavity, can collect
In gasify rapidly in cavity 21 subregion, can preferably avoid working medium gasification not exclusively.
By the dynamic system of heat energy of the comprehensive utilization acting pump waste heat in above-described embodiment is tested, heat source temperature
Being 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, work in circulation pipe
Mass flow speed is adjusted according to the operation stability of the dynamic system of heat energy of comprehensive utilization acting pump waste heat；Experiment effect is: heat
Source temperature is 120 DEG C, and heat energy transformation efficiency is about 17%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 19%, thermal source
When temperature is 200 DEG C, heat energy transformation efficiency is about 24%, and heat source temperature is 250 DEG C, and heat energy transformation efficiency is about 29%, thermal source temperature
When degree 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%；At 120-
350 DEG C of thermal source sections, in the present embodiment, the comprehensive heat energy transformation efficiency of the dynamic system of heat energy of comprehensive utilization acting pump waste heat is about
27%；Embodiment one relatively, heat energy transformation efficiency promotes about 9%.
Embodiment 11 (as shown in figure 11): be with embodiment one difference: be provided with one in described 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 acting pump 3 port of export pressure, increase acting pump 3 into and out of two ends pressure reduction, thus
Increase the amount of work of acting pump 3, reduce the interior energy after working medium acting, improve the condensing rate of working medium, and improve heat energy efficiency.
By the dynamic system of heat energy of the comprehensive utilization acting pump waste heat in above-described embodiment is tested, heat source temperature
Being 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, work in circulation pipe
Mass flow speed is adjusted according to the operation stability of the dynamic system of heat energy of comprehensive utilization acting pump waste heat；Experiment effect is: heat
Source temperature is 120 DEG C, and heat energy transformation efficiency is about 16%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 18%, thermal source
When temperature is 200 DEG C, heat energy transformation efficiency is about 23%, and heat source temperature is 250 DEG C, and heat energy transformation efficiency is about 28%, thermal source temperature
When degree 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%；At 120-
350 DEG C of thermal source sections, in the present embodiment, the comprehensive heat energy transformation efficiency of the dynamic system of heat energy of comprehensive utilization acting pump waste heat is about
26%；Embodiment one relatively, heat energy transformation efficiency promotes about 8%.
Embodiment 12 (as shown in figure 12): be with embodiment one difference: be provided with multiple in described condenser 4
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 pump 3 port of export, improve pressure difference largely, can preferably realize
Fractional condensaion, and reduce energy consumption needed for supercharging.
By the dynamic system of heat energy of the comprehensive utilization acting pump waste heat in above-described embodiment is tested, heat source temperature
Being 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, work in circulation pipe
Mass flow speed is adjusted according to the operation stability of the dynamic system of heat energy of comprehensive utilization acting pump waste heat；Experiment effect is: heat
Source temperature is 120 DEG C, and heat energy transformation efficiency is about 17%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 19%, thermal source
When temperature is 200 DEG C, heat energy transformation efficiency is about 24%, and heat source temperature is 250 DEG C, and heat energy transformation efficiency is about 29%, thermal source temperature
When degree 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%；At 120-
350 DEG C of thermal source sections, in the present embodiment, the comprehensive heat energy transformation efficiency of the dynamic system of heat energy of comprehensive utilization acting pump waste heat is about
27%；Embodiment one relatively, heat energy transformation efficiency promotes about 9%.
Embodiment 13 (as shown in figure 13): be with embodiment one difference: be provided with in described gasification reactor 2
Energy storage equipment 25；Described energy storage equipment 25 uses high heat capacity material to make；Described energy storage equipment 25 is for closing water body.
Take said structure, the temperature of gasification reactor 2 inner chamber body 21 can be stablized, thus stablize gasification temperature.
By the dynamic system of heat energy of the comprehensive utilization acting pump waste heat in above-described embodiment is tested, heat source temperature
Being 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, work in circulation pipe
Mass flow speed is adjusted according to the operation stability of the dynamic system of heat energy of comprehensive utilization acting pump waste heat；Experiment effect is: heat
Source temperature is 120 DEG C, and heat energy transformation efficiency is about 14%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 16%, thermal source
When temperature is 200 DEG C, heat energy transformation efficiency is about 21%, and heat source temperature is 250 DEG C, and heat energy transformation efficiency is about 26%, thermal source temperature
When degree 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%；At 120-
350 DEG C of thermal source sections, in the present embodiment, the comprehensive heat energy transformation efficiency of the dynamic system of heat energy of comprehensive utilization acting pump waste heat is about
24%；Embodiment one relatively, heat energy transformation efficiency promotes about 6%.
Embodiment 14: be with embodiment one difference: include four layers of cavity 21 in described gasification reactor 2；Institute
Stating cavity 21 and comprise inner chamber 211, exocoel 212 and lumen 213, the inside and outside end of lumen 213 connects inner chamber 211, exocoel 212 respectively；
Multiple lumen 213 is comprised, the fan-shaped distribution of lumen 213 between described inner chamber 211 and exocoel 212.
Described 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, air inlet 36 and the pitch angle of gas outlet 37
Degree is more than the pitch angles between adjacent two eccentric blades 32；The side of described circular cavity 31 is provided with multiple gas outlet 37, gives vent to anger
Mouth 37 is more than the pitch angles between adjacent two eccentric blades 32 with the pitch angles of air inlet 36；The eccentric leaf of described acting pump 3
Sheet 32 comprises four.
Described condenser 4 uses the cold mode of liquid, described condenser 4 to include condensing tube 41 and four condensation chambers 42, and two cold
Connected by many condensing tubes 41 between solidifying chamber 42；Described condensing tube 41 is curvilinear；Described condensing tube 41 is twist.
Described condenser 4 uses air cooling way, described condensing unit 4 to include condensing tube 41, fin 43 and heat emission fan 44,
Condensing tube 41 periphery installed by fin 43, and heat emission fan 44 is positioned at above or below condensing tube 41 or side, and heat emission fan 44 is to take out
Wind mode or pressure wind mode drive；Described condensing tube 41 is in multilamellar or multiple rows of distribution, the mutual UNICOM of condensing tube 41；Described condensing tube
41 are made by thermo-electric generation sheet 411；Described thermo-electric generation sheet 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-type semiconductor 414 are connected by sheet metal 412, p-type semiconductor 413 and N-shaped half
The series connection end at the whole story of conductor 414 connects output electrode 416 respectively.
Described circulating line 6 connects has regulation system 61, regulation system 61 to include pressure regulator 611, temperature sensor
612 and medium actuator 613, temperature sensor 612 is arranged in gasification reactor 2, and pressure regulator 611 controls to connect pressure
Pump 5, medium actuator 613 is arranged in circulating line 6, is used for regulating rate-of flow；Described regulation 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.
Described condenser 4 also includes collecting tank 45, and collecting tank 45 is for collecting the condensed fluid in condenser 4；Described collection
Liquid bath 45 is positioned at the afterbody of condenser 4.
The front end of described gasification reactor 2 is additionally provided with preheating cavity 24；Described preheating cavity 24 is looped around gasification reactor 2 weeks
Limit；Described preheating cavity 24 helically type.
Described acting pump 3 exhaust ports is provided with preliminary condensation chamber 301；Described preliminary condensation chamber 301 uses air-cooled or water-cooled.
Being provided with a negative pressure pump 46 in described condenser 4, negative pressure pump 46 is arranged on condensing tube middle-end.
In described gasification reactor 2, energy storage equipment 25 is installed；Described energy storage equipment 25 uses high heat capacity material to make；Institute
State energy storage equipment 25 for closing water body.
Take said structure, the temperature of gasification reactor 2 inner chamber body 21 can be stablized, thus stablize gasification temperature.
By the dynamic system of heat energy of the comprehensive utilization acting pump waste heat in above-described embodiment is tested, heat source temperature
Being 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, work in circulation pipe
Mass flow speed is adjusted according to the operation stability of the dynamic system of heat energy of comprehensive utilization acting pump waste heat；Experiment effect is: heat
Source temperature is 120 DEG C, and heat energy transformation efficiency is about 21%, and when heat source temperature is 150 DEG C, heat energy transformation efficiency is about 23%, thermal source
When temperature is 200 DEG C, heat energy transformation efficiency is about 28%, and heat source temperature is 250 DEG C, and heat energy transformation efficiency is about 33%, thermal source temperature
When degree 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%；At 120-
350 DEG C of thermal source sections, in the present embodiment, the comprehensive heat energy transformation efficiency of the dynamic system of heat energy of comprehensive utilization acting pump waste heat is about
31%；Embodiment one relatively, heat energy transformation efficiency promotes about 13%.
Finally it is noted that the foregoing is only the preferred embodiments of the present invention, it is not limited to the present invention,
Although being described in detail the present invention with reference to previous embodiment, for a person skilled in the art, it still may be used
So that the technical scheme described in foregoing embodiments to be modified, or wherein portion of techniques feature is carried out equivalent,
All within the spirit and principles in the present invention, any modification, equivalent substitution and improvement etc. made, should be included in the present invention's
Within protection domain.
Claims (7)
1. comprehensively utilize a dynamic system of heat energy for acting pump waste heat, 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 pressure
Pump (5) realizes circulation UNICOM, gasification reactor (2) contact thermal source (1) by circulating line (6), it is characterised in that: described gasification
The front end of reactor (2) is additionally provided with preheating cavity (24), and described acting pump (3) exhaust ports is provided with preliminary condensation chamber (301), institute
State preheating cavity (24) and preliminary condensation chamber (301) paratactic contact.
The dynamic system of heat energy of comprehensive utilization acting pump waste heat the most according to claim 1, is characterized in that: described preheating cavity
(24) with preliminary condensation chamber (301) spiral paratactic contact.
The dynamic system of heat energy of comprehensive utilization acting pump waste heat the most according to claim 1, is characterized in that: described preheating cavity
(24) flow to contrary with the working medium of preliminary condensation chamber (301).
The dynamic system of heat energy of comprehensive utilization acting pump waste heat the most according to claim 1, is characterized in that: described preheating cavity
(24) import and export two ends are provided with flow velocity display table (241).
The dynamic system of heat energy of comprehensive utilization acting pump waste heat the most according to claim 4, is characterized in that: described preheating cavity
(24) flow control valve (242) it is additionally provided with in.
The dynamic system of heat energy of comprehensive utilization acting pump waste heat the most according to claim 5, is characterized in that: described current limliting increases
Pressure valve (242) uses manual type flow control valve.
The dynamic system of heat energy of comprehensive utilization acting pump waste heat the most according to claim 5, is characterized in that: described current limliting increases
Pressure valve (242) uses electric-controlled type flow control valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610762065.9A CN106224039A (en) | 2016-08-30 | 2016-08-30 | A kind of dynamic system of heat energy comprehensively utilizing acting pump waste heat |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610762065.9A CN106224039A (en) | 2016-08-30 | 2016-08-30 | A kind of dynamic system of heat energy comprehensively utilizing acting pump waste heat |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106224039A true CN106224039A (en) | 2016-12-14 |
Family
ID=58073040
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610762065.9A Pending CN106224039A (en) | 2016-08-30 | 2016-08-30 | A kind of dynamic system of heat energy comprehensively utilizing acting pump waste heat |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106224039A (en) |
-
2016
- 2016-08-30 CN CN201610762065.9A patent/CN106224039A/en active Pending
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106224044A (en) | A kind of dynamic system of heat energy based on condenser negative pressure | |
| CN106224037A (en) | A kind of exhaust dynamic system of heat energy based on semi-conductor condensation | |
| CN106437893A (en) | Heat energy power system for stable temperature gasification | |
| CN106224039A (en) | A kind of dynamic system of heat energy comprehensively utilizing acting pump waste heat | |
| CN106438239A (en) | Solar heat energy power system based on multistage pressurization condensation | |
| CN106224028A (en) | A kind of dynamic system of heat energy based on voltage stabilizing homoiothermic | |
| CN106224032A (en) | A kind of exhaust dynamic system of heat energy based on pressure-adjustable voltage stabilizing condensation | |
| CN106246259A (en) | A kind of oil field based on semi-conductor condensation heat energy from waste gas dynamical system | |
| CN106246255A (en) | A kind of dynamic system of heat energy based on condensation liquid collecting | |
| CN106224027A (en) | A kind of shunting polymerization chamber dynamic system of heat energy | |
| CN106437891A (en) | Solar heat energy power system based on eccentric turbine | |
| CN106224038A (en) | A kind of dynamic system of heat energy based on bias acting pump | |
| CN106437914A (en) | Heat energy power system based on gasification preheating | |
| CN106437892A (en) | Heat energy power system for liquid condensation | |
| CN106246484A (en) | A kind of solar energy dynamical system based on semi-conductor condensation | |
| CN106437894A (en) | Semiconductor condensation-based heat energy power system | |
| CN106246270A (en) | A kind of semi-conductor condensation dynamic system of heat energy utilizing nuclear power station heat drain | |
| CN106437908A (en) | Internal combustion engine tail gas utilization heat energy power system based on multistage pressurization condensation | |
| CN106224029A (en) | A kind of solar energy dynamical system based on the gasification of honeycomb chamber | |
| CN106246485A (en) | A kind of solar energy dynamical system based on supercharging condensation | |
| CN106224025A (en) | A kind of biofermentation dynamic system of heat energy based on centering type turbine | |
| CN106437899A (en) | Solar heat energy power system based on pressure adjusting condensation | |
| CN106437971A (en) | Internal combustion engine tail gas utilization heat energy power system based on eccentric turbine | |
| CN106437902A (en) | Pressure-adjustable condensation heat energy power system using nuclear power plant hot drained water | |
| CN106246253A (en) | A kind of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20161214 |