CN106438239A - Solar heat energy power system based on multistage pressurization condensation - Google Patents

Solar heat energy power system based on multistage pressurization condensation Download PDF

Info

Publication number
CN106438239A
CN106438239A CN201610760145.0A CN201610760145A CN106438239A CN 106438239 A CN106438239 A CN 106438239A CN 201610760145 A CN201610760145 A CN 201610760145A CN 106438239 A CN106438239 A CN 106438239A
Authority
CN
China
Prior art keywords
heat
solar energy
working medium
transformation efficiency
heat energy
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.)
Withdrawn
Application number
CN201610760145.0A
Other languages
Chinese (zh)
Inventor
郭远军
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN201610760145.0A priority Critical patent/CN106438239A/en
Publication of CN106438239A publication Critical patent/CN106438239A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • 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
    • F01K11/02—Plants characterised by the engines being structurally combined with boilers or condensers the engines being turbines
    • 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
    • F01K13/00—General layout or general methods of operation of complete plants
    • 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
    • F01K13/00—General layout or general methods of operation of complete plants
    • F01K13/006—Auxiliaries or details not otherwise provided for
    • 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
    • F01K13/00—General layout or general methods of operation of complete plants
    • F01K13/02—Controlling, e.g. stopping or starting
    • 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
    • F01K9/00—Plants characterised by condensers arranged or modified to co-operate with the engines
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
    • F03G—SPRING, WEIGHT, INERTIA OR LIKE MOTORS; MECHANICAL-POWER PRODUCING DEVICES OR MECHANISMS, NOT OTHERWISE PROVIDED FOR OR USING ENERGY SOURCES NOT OTHERWISE PROVIDED FOR
    • F03G6/00—Devices for producing mechanical power from solar energy
    • F03G6/06—Devices for producing mechanical power from solar energy with solar energy concentrating means
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00—Energy generation through renewable energy sources
    • Y02E10/40—Solar thermal energy, e.g. solar towers
    • Y02E10/46—Conversion of thermal power into mechanical power, e.g. Rankine, Stirling or solar thermal engines

Abstract

The invention discloses a solar heat energy power system based on multistage pressurization condensation. The solar heat energy power system based on multistage pressurization condensation comprises a heat collecting device, a gasifying device, a turbine, a condensing device and a one-way hydraulic pump for realizing circulating communication through circulating pipes; circulating working mediums are filled in the circulating pipes; the heat collecting device and the gasifying device are mounted in a solar light collecting cover; the condensing device is mounted out of the solar light collecting cover, and includes a condensing pipe, a cooling fan and multiple pressurization mechanisms; the cooling fan is mounted above or below the condensing pipe; and the pressurization mechanisms are uniformly distributed at the middle part of the condensing pipe stage by stage. The solar heat energy power system based on multistage pressurization condensation is quicker in condensing speed, can reduce the condensation energy discharge and improve the heat energy conversion efficiency, and is stable in operation and adjustable in power.

Description

A kind of solar energy dynamical system based on multi-stage booster condensation
Technical field
The invention belongs to utilization of energy apparatus field, especially a kind of solar heat motility based on multi-stage booster condensation 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 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.Currently the substance of the energy strategy of China is：Adhere to economization at first, base oneself upon The country, diverse development, depend on science and technology, environmental protection, strengthen international mutual beneficial co-operation, making great efforts to construct stable, economical, cleaning, safety Energy supply system, support the sustainable development of economic society with the sustainable development of the energy.
China implements the measure of energy conservation comprehensively：Push structure is adjusted, and is accelerated the upgrading and optimization of industrial structure, is sent out energetically Exhibition new high-tech industry and service trade, strictly limit highly energy-consuming, high consumptive material, highly water intensive industry development, eliminate the backward production facilities, and promote The right-about of Economic Development Mode, accelerates to build energy-saving industrial system.Strengthen industrial energy saving, accelerate technological transformation, improve Management level, reduce energy resource consumption.Implement energy conservation project, the popularization and application of energy-efficient product are encouraged, greatly develops energy-saving Ground type building, improves efficiency of energy utilization, accelerates energy-saving monitoring and technical service system construction, strengthens energy-saving monitoring, innovation clothes Business platform.Strengthen management energy-conservation, actively push forward preferentially to purchase energy-conservation（Including water saving）Product, studies and defines the property tax for encouraging energy-conservation Policy.Social energy conservation is advocated, the significance of energy saving is conducted vigorous propaganda, constantly strengthen whole people's resource awareness of unexpected development and save meaning Know.
For responding national energy-saving strategy, increasing enterprise starts to research and develop, use energy-saving equipment, and strengthens producing to discarded Can thing, the utilization of waste heat energy.Wherein, in terms of the utilization of waste heat, mainly surplus energy utility is realized by thermal generating equipment.Existing Some thermal generating equipments include plurality of classes, but can be divided mainly into two classes, and a class is, using turbine, heat energy is changed into machine Tool energy, then mechanical energy is changed into electric energy, the generating equipment of this kind of principle classification is more ripe, and species is many；Another kind of is to utilize Heat energy is directly translated into electric potential energy by thermoelectric conversion element by pyroelectric effect principle, but due to in terms of generation technology not Maturation, 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 turbine, then mechanical energy is changed into electric energy by class thermal generating equipment.Such heat existing Energy generating equipment mainly includes cycle fluid, heat collector, gasification installation, turbine, electromotor and condensing units；During work, Cycle fluid passes through gasification installation in circulating line first, working medium is gasified and is promoted turbine to rotate, and turbine drives to be sent out Electric power generation, the working medium after gasification is externally done work when by turbine, and temperature and air pressure can reduce, and passes through condensing units It is cooled to liquid refrigerant.
However, existing thermal generating equipment common problem is：A. high to the temperature requirement of high temperature heat source, one As more than 200 DEG C, and heat energy transformation efficiency is low, and heat energy transformation efficiency is generally 15% to 35%；B. the heat of condensing units is arranged Amount is larger, and thermal waste is big, slow by the condensation rate of natural condensation mode, and adopts active condensing mode（Blower fan air-cooled or Liquid pump water-cooled）Need extra power consumption；C. easily there is the problem for leaking working medium in turbine；D. secondary speed is unstable, and easily goes out Existing stuck problem；E. the Heat-collecting effect of heat collector is not good, and extraneous exhaust-heat absorption rate is little, and f. working medium gasification temperature is unstable, work Matter condensation effect is not good, and working medium is apt to deteriorate or impurity occurs；G. existing equipment volume is larger.
Power output process realized by existing solar energy, first has to photoelectric effect, changes into electric energy, then again by electronic Equipment exports power；At this stage, solar energy changes into the equipment of electric energy and is mainly electro-optical package, and the photoelectric conversion process efficiency is very Low, efficiency is generally 5% or so, and energy waste is serious.
Content of the invention
Present invention purpose to be realized is：Efficient utilization solar energy, the hot discharge capacity of reduction and thermal waste, improve heat energy Transformation efficiency, stable working medium gasification temperature and refrigerant flow rate, improve working medium quality, prevent working medium from going bad, improve turbine structure, keep away Exempt from turbine to reveal and rotary speed unstabilization, condensing units are improved, accelerate condensing rate；To solve existing heat energy in above-mentioned background technology Existing for equipment：Heat energy transformation efficiency is low, and working medium gasification temperature is unstable, and working medium condensation effect is not good, and working medium is apt to deteriorate Or there is impurity, easily there is refrigerant leakage in turbine, secondary speed unstable and easily occur stuck, condensing units The problems such as thermal waste 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 solar energy based on multi-stage booster condensation Dynamic system of heat energy, including heat collector, gasification installation, turbine, Salar light-gathering cover, condensing units, circulating line, circulation Working medium and one-way hydraulic pump, heat collector, gasification installation, turbine, condensing units and one-way hydraulic pump pass sequentially through circulation pipe Circulation UNICOM is realized in road, and circulating line is contained within cycle fluid；
It is characterized in that：The heat collector and gasification installation are in Salar light-gathering cover, and the condensing units are arranged on and keep away Light plenum area, the heat collector includes solar energy heat collection pipe and solar heat collector, and solar heat collector parallel interval is distributed, Solar energy heat collection pipe fold-type is distributed in solar heat collector；Gasification installation includes solar energy gasification heat-absorbing chamber and gasification pressure control Device, gasification pressure controller is used for cycle fluid blood pressure lowering installed in solar energy gasification heat absorption intracavity, gasification pressure controller；When high-pressure liquid work Matter reaches heat source temperature after fully heating in solar energy heat collection pipe, and high-pressure liquid working medium flows into solar energy gasification heat-absorbing chamber, too The positive gasification pressure controller that can gasify heat absorption intracavity is controlled by pressure so as to liquid refrigerant endothermic gasification, and gasification working medium is in turbine Blood pressure lowering acting in machine；This kind of structure has compared in solar energy heat collection pipe direct gasification, being prevented effectively to mix in gasification working medium Liquid refrigerant, can make working medium gasify evenly；
The condensing units include condensing tube, heat emission fan and multiple booster bodies, and heat emission fan is arranged on above or below condensing tube, Booster body is evenly distributed in the middle part of condensing tube step by step；
The booster body includes pressurized cylinder, piston, eccentric, air inlet, gas outlet, breather cheek valve, unidirectional air outlet valve and Gas-pressure adjustable valve, piston is in pressurized cylinder, and piston is driven by eccentric by push rod, and pressurized cylinder bottom is provided with air inlet And gas outlet, breather cheek valve is installed at air inlet, gas outlet is provided with unidirectional air outlet valve and gas-pressure adjustable valve；Using the knot Structure can reduce the pressure of turbine outlet, increase the pressure reduction with place of giving vent to anger at turbine inlet, exist so as to increase expanding gas Amount of work in turbine, and reduce the temperature of expanding gas, thus, the structure can produce preferable condensation effect, and improve heat The heat energy conversion ratio of active Force system.
Optimize further, between condensing units and heat collector, be additionally provided with contaminant filter pump.
Optimize further, between the solar energy gasification heat-absorbing chamber and solar energy heat collection pipe, be additionally provided with atomizing mouth.
Optimize further, the solar energy gasification heat-absorbing chamber is ellipse cavity.
Optimize further, the solar energy gasification heat-absorbing chamber becomes tapered, the horizontal cross-section of solar energy gasification heat-absorbing chamber is in Rhizoma Nelumbinis Poroid.
Optimize further, the solar energy gasification heat-absorbing chamber becomes polygon tapered, the horizontal cross-section of solar energy gasification heat-absorbing chamber All poroid in honeycomb.
Optimize further, the solar energy gasification heat-absorbing chamber 21 is located at the extraction regions of Salar light-gathering cover, solar energy gasifies Heat-absorbing chamber is using full glass heat absorption material or the fit heat absorption material of glass metal.
Optimize further, turbine is conventional steam turbine.
Optimize further, turbine is the steam turbine comprising multistage blade.
Optimize further, turbine is tesla's turbine.
Optimize further, turbine is radial outward flow turbine.
Optimize further, the exhaust ports of the turbine are provided with precondenser；Take the structure increase air inlet With the pressure reduction of air vent, the transformation efficiency of turbine is improved.
Optimize further, the precondenser includes working medium conduction pipe and condensation endothermic tube, working medium conduction pipe is used for connecting Air vent and circulating line, condensing endothermic tube is used for absorbing the heat that working medium turns on intraductal working medium, and working medium conduction pipe is inhaled with condensation Heat pipe spiral paratactic contact, is heat recipient fluid in condensation endothermic tube, is to increase condensation efficiency, the flow direction of heat recipient fluid and work The flow direction of matter conducting intraductal working medium is contrary.
Optimize further, the condensation endothermic tube adopts the circulating line between UNICOM's one-way hydraulic pump and heat collector； As the circulating line between one-way hydraulic pump and heat collector needs heat absorption, and working medium conducting intraductal working medium needs heat extraction, should Structure largely recycles working medium heat in circulating line, increases thermal transition efficiency.
Optimize further, the condensing tube becomes oblique type to be distributed.
Optimize further, the condensing tube becomes horizontal or vertical distribution.
Optimize further, when the condensing tube becomes horizontal distribution, upper and lower layer condensing tube mutually staggers.
Optimize further, the condensing tube is copper metal tube or stability alloying metal pipe.
Optimize further, the condensing tube is made by thermo-electric generation sheet, thermo-electric generation sheet includes that sheet metal, p-type are partly led Body, 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 are connected by sheet metal, the whole story end of connecting of p-type semiconductor and n-type semiconductor Connect output electrode respectively.
Optimize further, the output electrode end of the thermo-electric generation sheet is connected with manostat, booster transformer, electric power storage in turn Pond, accumulator is used for heat emission fan, the power supply of one-way hydraulic pump.
Optimize further, in order to avoid the working medium of uncooled liquefaction in condensing tube enters one-way hydraulic pump, condensing tube tail end It is provided with catch box.
Optimize further, in order to accelerate radiating, condensing units are additionally provided with fin.
Optimize further, the cycle fluid adopts propanol.
Optimize further, the cycle fluid adopts methanol.
Optimize further, the cycle fluid adopts ethanol.
Optimize further, the cycle fluid adopts isopropanol.
Optimize further, the cycle fluid adopts liquefied ammonia.
Optimize further, the cycle fluid is using conventional freon.
Optimize further, working medium actuator between turbine and condensing units, is additionally provided with, the working medium actuator includes Turbine current limiter and pressure voltage stabilizing pressure controller, turbine current limiter includes turbine structure and secondary speed controller, pressure voltage stabilizing control Depressor includes the gentle pressure piston of slow pressure storage stream cylinder and barostat, delays the top UNICOM circulating line of pressure storage stream cylinder, delays pressure storage The bottom UNICOM barostat of stream cylinder, delays pressure piston in slow pressure storage stream cylinder；When the pressure of working medium in circulating line or When flow velocity changes, turbine current limiter can realize the restriction of flow velocity by limiting the rotation of turbine structure, while part work Matter can be postponed and be pressed storage stream cylinder outflow or flow into expansion or the compression for realizing volume, so as to realize the effect of stable pressure.
Operation principle：Solar energy dynamical system described in the invention based on multi-stage booster condensation, during work, circulation industrial Matter is absorbed heat the heat source temperature that reaches a high temperature in heat collector, then flows in gasification installation, is vaporized suction by the blood pressure lowering of a small amount of Heat, flows turbine after working medium gasification, drives rotating turbine；After gasification working medium flows through turbine, due to externally doing work, its work Matter temperature and air pressure can all reduce, and cause part working medium liquefaction；After gasification working medium flows through turbine, working medium flows working medium successively Actuator and condensing units；Working medium actuator be used for control the pressure of working medium, flow velocity in circulating line, working medium actuator energy according to Extraneous heat absorption area and the temperature conditionss of heat release zone, adjust working medium condensing temperature or gasification temperature, so as to effectively improve heat energy Transformation efficiency；Working medium can be liquefied by condensing units completely；After liquefaction, working medium sequentially passes through contaminant filter pump and one-way hydraulic pump, miscellaneous Matter filter pump can by contaminant filter in working medium out, and one-way hydraulic pump carries out unidirectional pumping supercharging to working medium；After liquefaction working medium according to Secondary and be again introduced into gasification installation after contaminant filter pump and one-way hydraulic pump, complete a circulation.
Solar energy dynamical system based on multi-stage booster condensation of the present invention is by setting step by step in condensing units Put booster body, it is possible to decrease the pressure of turbine outlet, increase the pressure reduction with place of giving vent to anger at turbine inlet, swollen so as to increase Flatulence body amount of work in the turbine, and largely reduce the temperature of expanding gas；Thus, the structure can be produced preferably Condensation effect, and improve the heat energy conversion ratio of dynamic system of heat energy.
Beneficial effect：Solar energy dynamical system based on multi-stage booster condensation of the present invention, with respect to existing skill Heat energy machine in art, have the advantages that following several respects and progress：1., by setting up booster body in condensing units, gas is increased The amount of work of body turbine, can largely improve condensing rate, reduce condensation power consumption, and improve system heat energy conversion ratio； 2. by setting up precondenser, it is possible to increase the pressure reduction of air inlet and air vent in turbine, and the heat energy of working medium can be recycled, Realize the heat absorption to cycle fluid difference section and heat rejection process is comprehensively utilized, reduce thermal waste and cooling power consumption；3. By contaminant filter pump and one-way hydraulic pump is set up, can effectively prevent working medium rotten and more impurity occur, and prevent working medium Backflow；4. by working medium actuator is set up, the pressure and flow of working medium is controlled, gasification efficiency and condensation can be effectively improved Efficiency, and stable working medium gasification temperature and refrigerant flow rate, prevent sealing member deformation larger, it is to avoid secondary speed is unstable and working medium is let out Dew problem；5. condensing tube is made using thermo-electric generation sheet, the temperature difference calorific potential using condensation process can be divided, improve heat energy conversion effect Rate, and accelerate thermal energy conduction speed using the electric current for producing in thermo-electric generation sheet；6. efficient utilization solar energy, realizes solar energy Power output.
Description of the drawings
Fig. 1 is the Integral connection structure schematic diagram of the present invention program one；
Fig. 2 is the Salar light-gathering cover structure schematic diagram of the present invention program one；
Fig. 3 is the condensing units attachment structure schematic diagram of the present invention program one；
Fig. 4 is the booster body structural representation of the present invention program one；
Fig. 5 is the solar energy gasification heat-absorbing chamber structural representation of the present invention program one；
Fig. 6 is the heat collector structural representation of the present invention program two；
Fig. 7 is the heat collector structural representation of the present invention program three；
Fig. 8 is the gasification pressure controller structural representation of the present invention program four；
Fig. 9 is the atomizing mouth mounting connection structure schematic diagram of the present invention program five；
Figure 10 is the solar energy gasification heat-absorbing chamber cross section structure schematic diagram of the present invention program six；
Figure 11 is the solar energy gasification heat-absorbing chamber cross section structure schematic diagram of the present invention program seven；
Figure 12 is the Integral connection structure schematic diagram of the present invention program 11；
Figure 13 is the working medium controller structure schematic diagram of the present invention program 11；
Figure 14 is the precondenser structural representation of the present invention program 12；
Figure 15 is the precondenser attachment structure schematic diagram of the present invention program 13；
Figure 16 is the condensing units vertical cross section structural representation of the present invention program 14；
Figure 17 is the condensing units vertical cross section structural representation of the present invention program 15；
Figure 18 is the condensing units vertical cross section structural representation of the present invention program 16；
Figure 19 is the thermo-electric generation sheet structural representation of the present invention program 17；
In figure：
1 is heat collector, 11 is solar energy heat collection pipe, 12 is solar heat collector；
2 is gasification installation, 21 is solar energy gasification heat-absorbing chamber, 22 is gasification pressure controller, 221 is differential pressure control valve, 222 is gasification Pressure induction apparatuss, 23 are atomizing mouth；
3 is turbine, 36 is precondenser, 361 is working medium conduction pipe, 362 is condensation endothermic tube；
4 is Salar light-gathering cover；
5 is condensing units, 51 is condensing tube, 511 is thermo-electric generation sheet, 512 is sheet metal, 513 is p-type semiconductor, 514 is n Type quasiconductor, 515 be dielectric substrate layer, 516 be output electrode, 517 be manostat, 518 be booster transformer, 519 be electric power storage Pond, 52 be heat emission fan, 53 be booster body, 531 be pressurized cylinder, 532 be piston, 533 be eccentric, 534 be air inlet, 535 For gas outlet, 536 be breather cheek valve, 537 be unidirectional air outlet valve, 538 be gas-pressure adjustable valve, 54 be catch box, 55 for radiating Piece；
6 is circulating line；
7 is cycle fluid；
8 is contaminant filter pump；
9 is one-way hydraulic pump；
10 is working medium actuator, 101 is turbine current limiter, 102 is pressure voltage stabilizing pressure controller, 103 is turbine structure, 104 is whirlpool Wheel speed controller, 105 be slow pressure storage stream cylinder, 106 for slow pressure piston, 107 be.
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 solar energy dynamical system based on multi-stage booster condensation, including thermal-arrest Device 1, gasification installation 2, turbine 3, Salar light-gathering cover 4, condensing units 5, circulating line 6, cycle fluid 7 and one-way hydraulic Pump 9, heat collector 1, gasification installation 2, turbine 3, condensing units 5 and one-way hydraulic pump 9 pass sequentially through circulating line 6 and realize following Ring UNICOM, circulating line 6 is contained within cycle fluid 7, for the biomass gasification boiler of working medium in gasification installation 2；
（As shown in Figure 2）The heat collector 1 and gasification installation 2 are in Salar light-gathering cover 4, and the heat collector 1 is wrapped Solar energy heat collection pipe 11 and solar heat collector 12 is included, 12 parallel interval of solar heat collector is distributed, 11 folding of solar energy heat collection pipe Type is distributed in solar heat collector 12；Gasification installation 2 includes solar energy gasification heat-absorbing chamber 21 and gasification pressure controller 22, gasification control Depressor 22 is in solar energy gasification heat-absorbing chamber 21, and gasification pressure controller 22 is used for liquid refrigerant blood pressure lowering；When high-pressure liquid working medium Heat source temperature is reached after fully heating in solar energy heat collection pipe 11, high-pressure liquid working medium flows into solar energy gasification heat-absorbing chamber 21, Gasification pressure controller 22 in solar energy gasification heat-absorbing chamber 21 is controlled by pressure so as to liquid refrigerant endothermic gasification, and gasify working medium Blood pressure lowering acting in the turbine 3；This kind of structure can be prevented effectively from gasification working medium compared in 11 direct gasification of solar energy heat collection pipe In mix and have liquid refrigerant, working medium can be made to gasify evenly；
（As shown in Figure 3）The condensing units 5 include condensing tube 51, heat emission fan 52 and multiple booster bodies 53, and condensing tube 51 is equal Even point of Multi-layers distributing, the mutual UNICOM of condensing tube 51, heat emission fan 52 is above or below condensing tube 51, and heat emission fan 52 is with convulsion Mode or pressure wind mode drive；
（As shown in Figure 4）The booster body 53 is evenly distributed on 51 middle part of condensing tube step by step, and the booster body 53 includes to increase Cylinder pressure 531, piston 532, eccentric 533, air inlet 534, gas outlet 535, breather cheek valve 536, unidirectional air outlet valve 537 and can Regulating QI pressure valve 538, piston 532 is in pressurized cylinder 531, and piston 532 is driven by eccentric 533 by push rod, pressurized cylinder 531 Bottom is provided with air inlet 534 and gas outlet 535, is provided with breather cheek valve 536 at air inlet 534, and gas outlet 535 is provided with Unidirectional air outlet valve 537 and gas-pressure adjustable valve 538；The pressure in 3 exit of turbine can be reduced using the structure, increase turbine 3 Pressure reduction at air inlet with place of giving vent to anger, so as to increase expanding gas amount of work in turbine 3, and reduces the temperature of expanding gas, Thus, the structure can produce preferable condensation effect, and improve the heat energy conversion ratio of dynamic system of heat energy.
As further illustrating for above-mentioned embodiment, between the condensing units 5 and heat collector 1, impurity is additionally provided with Filter pump 8.
As further illustrating for above-mentioned embodiment,（As shown in Figure 5）The solar energy gasification heat-absorbing chamber 21 is by multiple Body is formed side by side.
Used as further illustrating for above-mentioned embodiment, the turbine 3 is conventional vane type steam turbine.
Used as further illustrating for above-mentioned embodiment, 51 tail end of the condensing tube is provided with catch box 54.
Used as further illustrating for above-mentioned embodiment, the condensing units 5 are additionally provided with fin 55.
Used as further illustrating for above-mentioned embodiment, the cycle fluid 7 adopts liquefied ammonia.
By to being tested based on the solar energy dynamical system of multi-stage booster condensation in above-described embodiment one, leading to Cross the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, cold In the case of source temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is according to the solar energy dynamical system for being condensed based on multi-stage booster Operation stability is adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 17%, work When matter gasification temperature is 55 DEG C or so, heat energy transformation efficiency is about 7%, when working medium gasification temperature is 60 DEG C or so, heat energy conversion effect Rate is about 10%, and when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 12%, and working medium gasification temperature is 70 DEG C or so When, heat energy transformation efficiency is about 14.4%, the heat of the solar energy dynamical system for being condensed based on multi-stage booster in the present embodiment one Energy transformation efficiency is than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very low, and efficiency is less than 5%）Phase Than the heat energy transformation efficiency of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment is more active than the conventional sun The heat energy transformation efficiency mean height 7% or so of power equipment；Meanwhile, the solar heat that the present embodiment is condensed based on multi-stage booster is active Force system cooldown rate is fast, and hot driving is little, and operation noise is little, good operation stability, while can achieve power output regulation.
Embodiment two（As shown in Fig. 6）：It is with one difference of embodiment：The solar heat collector 12 of heat collector 1 Lamellar in curved surface.
By to being tested based on the solar energy dynamical system of multi-stage booster condensation in above-described embodiment two, leading to Cross the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, cold In the case of source temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is according to the solar energy dynamical system for being condensed based on multi-stage booster Operation stability is adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 17.5%, When working medium gasification temperature is 55 DEG C or so, heat energy transformation efficiency is about 8%, and when working medium gasification temperature is 60 DEG C or so, heat energy is converted Efficiency is about 10.4%, and when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 12.4%, and working medium gasification temperature is 70 DEG C or so when, heat energy transformation efficiency is about 14.8%, in the present embodiment two based on multi-stage booster condensation solar energy dynamical system The heat energy transformation efficiency of system is than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very low, and efficiency is less than 5%）Compare, the heat energy transformation efficiency of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment is than routine too The heat energy transformation efficiency mean height 7.8% or so of positive motility equipment.
Embodiment three（As shown in Fig. 7）：It is with one difference of embodiment：The solar energy heating of the heat collector 1 Piece 12 is in be in staggered distribution.
By to being tested based on the solar energy dynamical system of multi-stage booster condensation in above-described embodiment three, leading to Cross the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, cold In the case of source temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is according to the solar energy dynamical system for being condensed based on multi-stage booster Operation stability is adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 17.5%, When working medium gasification temperature is 55 DEG C or so, heat energy transformation efficiency is about 8.4%, and when working medium gasification temperature is 60 DEG C or so, heat energy turns Change efficiency and be about 10.6%, when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 12.6%, and working medium gasification temperature is When 70 DEG C or so, heat energy transformation efficiency is about 15%；Solar energy dynamical system in the present embodiment three based on multi-stage booster condensation The heat energy transformation efficiency of system is than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very low, and efficiency is less than 5%）Compare, the heat energy transformation efficiency of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment is than routine too The heat energy transformation efficiency mean height 6.2% or so of positive motility equipment.
Example IV（As shown in Figure 8）：It is with one difference of embodiment：The gasification pressure controller 22 includes pressure reduction control Valve processed 221 and gasification pressure induction apparatuss 222, differential pressure control valve 221 is located at the front end of solar energy gasification heat-absorbing chamber 21, and gasify pressure Induction apparatuss 222 are located at solar energy gasification 21 rear end of heat-absorbing chamber；Differential pressure control valve 221 is used for adjusting pressure reduction, and gasify pressure induction apparatuss 222 are used for sensing the pressure of working medium in solar energy gasification heat-absorbing chamber 21, when pressure is larger, increase the pressure of differential pressure control valve 221 Difference, when pressure is compared with hour, reduces the pressure reduction of differential pressure control valve 221, so as to realize the pressure control to solar energy gasification heat-absorbing chamber 21 System.
By to being tested based on the solar energy dynamical system of multi-stage booster condensation in above-described embodiment four, leading to Cross the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, cold In the case of source temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is according to the solar energy dynamical system for being condensed based on multi-stage booster Operation stability is adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 5%, work When matter gasification temperature is 55 DEG C or so, heat energy transformation efficiency is about 8.7%, and when working medium gasification temperature is 60 DEG C or so, heat energy is converted Efficiency is about 10.8%, and when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 13.2%, and working medium gasification temperature is 70 DEG C or so when, heat energy transformation efficiency is about 16.2%, in the present embodiment four based on multi-stage booster condensation solar energy dynamical system The heat energy transformation efficiency of system is than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very low, and efficiency is less than 5%）Compare, the heat energy transformation efficiency of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment is than routine too The heat energy transformation efficiency mean height 7.5% or so of positive motility equipment.
Embodiment five（As shown in Figure 9）：It is with example IV difference：Solar energy gasification heat-absorbing chamber 21 with too Sun can be additionally provided with atomizing mouth 23 between thermal-collecting tube 11.
Being tested based on the solar energy dynamical system of multi-stage booster condensation by above-described embodiment five, by The sunlight of varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, in low-temperature receiver temperature Spend for, in the case of 18 DEG C, in circulation pipe, refrigerant flow rate is according to the operation of the solar energy dynamical system for being condensed based on multi-stage booster Stability is adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 6%, working medium gas When changing temperature for 55 DEG C or so, heat energy transformation efficiency is about 9.2%, when working medium gasification temperature is 60 DEG C or so, heat energy transformation efficiency About 11.2%, when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 14%, and working medium gasification temperature is 70 DEG C or so When, heat energy transformation efficiency is about 17%, the heat energy of the solar energy dynamical system for being condensed based on multi-stage booster in the present embodiment five Transformation efficiency is than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very low, and efficiency is less than 5%）Compare, The heat energy transformation efficiency of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment is than conventional solar power The heat energy transformation efficiency mean height 8% or so of equipment.
Embodiment six（As shown in Figure 10）：It is with five difference of embodiment：The solar energy gasification heat-absorbing chamber 21 Horizontal cross-section is poroid in Rhizoma Nelumbinis.
By to being tested based on the solar energy dynamical system of multi-stage booster condensation in above-described embodiment six, leading to Cross the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, cold In the case of source temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is according to the solar energy dynamical system for being condensed based on multi-stage booster Operation stability is adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 7%, work When matter gasification temperature is 55 DEG C or so, heat energy transformation efficiency is about 9.6%, and when working medium gasification temperature is 60 DEG C or so, heat energy is converted Efficiency is about 12%, and when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 14.8%, and working medium gasification temperature is 70 DEG C During left and right, heat energy transformation efficiency is about 17.4%, the solar energy dynamical system in the present embodiment six based on multi-stage booster condensation Heat energy transformation efficiency than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very low, and efficiency is less than 5%）Compare, the heat energy transformation efficiency of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment is than routine too The heat energy transformation efficiency mean height 9.3% or so of positive motility equipment.
Embodiment seven（As shown in figure 11）：It is with five difference of embodiment：The solar energy gasification heat-absorbing chamber 21 Horizontal cross-section is all poroid in honeycomb.
By to being tested based on the solar energy dynamical system of multi-stage booster condensation in above-described embodiment seven, leading to Cross the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, cold In the case of source temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is according to the solar energy dynamical system for being condensed based on multi-stage booster Operation stability is adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 7.5%, When working medium gasification temperature is 55 DEG C or so, heat energy transformation efficiency is about 9.8%, and when working medium gasification temperature is 60 DEG C or so, heat energy turns Change efficiency and be about 12.2%, when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 15.5%, and working medium gasification temperature is When 70 DEG C or so, heat energy transformation efficiency is about 17.8%, the solar heat motility in the present embodiment seven based on multi-stage booster condensation The heat energy transformation efficiency of system is than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very low, and efficiency is low In 5%）Compare, the heat energy transformation efficiency of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment is than conventional The heat energy transformation efficiency mean height 9% or so of solar power plant.
Embodiment eight：It is with seven difference of embodiment：The turbine 3 is the steamturbine comprising multistage blade Machine.
By to being tested based on the solar energy dynamical system of multi-stage booster condensation in above-described embodiment eight, leading to Cross the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, cold In the case of source temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is according to the solar energy dynamical system for being condensed based on multi-stage booster Operation stability is adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 8.7%, When working medium gasification temperature is 55 DEG C or so, heat energy transformation efficiency is about 10.4%, when working medium gasification temperature is 60 DEG C or so, heat energy Transformation efficiency is about 12.8%, and when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 16.6%, working medium gasification temperature During for 70 DEG C or so, heat energy transformation efficiency is about 18%, the solar heat motility in the present embodiment eight based on multi-stage booster condensation The heat energy transformation efficiency of system is than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very low, and efficiency is low In 5%）Compare, the heat energy transformation efficiency of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment is than conventional The heat energy transformation efficiency mean height 10.8% or so of solar power plant.
Embodiment nine：It is with seven difference of embodiment：The turbine 3 is tesla's turbine.
By to being tested based on the solar energy dynamical system of multi-stage booster condensation in above-described embodiment nine, leading to Cross the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, cold In the case of source temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is according to the solar energy dynamical system for being condensed based on multi-stage booster Operation stability is adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 9%, work When matter gasification temperature is 55 DEG C or so, heat energy transformation efficiency is about 10.6%, and when working medium gasification temperature is 60 DEG C or so, heat energy turns Change efficiency and be about 13%, when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 16.8%, working medium gasification temperature is 70 DEG C or so when, heat energy transformation efficiency is about 18.4%, in the present embodiment nine based on multi-stage booster condensation solar energy dynamical system The heat energy transformation efficiency of system is than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very low, and efficiency is less than 5%）Compare, the heat energy transformation efficiency of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment is than routine too The heat energy transformation efficiency mean height 11.4% or so of positive motility equipment.
Embodiment ten：It is with one difference of embodiment：The turbine 3 is radial outward flow turbine.
By to being tested based on the solar energy dynamical system of multi-stage booster condensation in above-described embodiment ten, leading to Cross the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, cold In the case of source temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is according to the solar energy dynamical system for being condensed based on multi-stage booster Operation stability is adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 8.7%, When working medium gasification temperature is 55 DEG C or so, heat energy transformation efficiency is about 10.4%, when working medium gasification temperature is 60 DEG C or so, heat energy Transformation efficiency is about 12.8%, and when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 16.8%, working medium gasification temperature During for 70 DEG C or so, heat energy transformation efficiency is about 18.1%, and the solar heat in the present embodiment ten based on multi-stage booster condensation is active The heat energy transformation efficiency of Force system is than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very low, efficiency Less than 5%）Compare, the heat energy transformation efficiency of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment is than normal The heat energy transformation efficiency mean height 11% or so of rule solar power plant.
Embodiment 11（As shown in Figure 12 and 13）：It is with ten difference of embodiment：The turbine 3 is centrifugation Working medium actuator 10 is additionally provided with described in formula turbine between turbine 3 and condensing units 5；Working medium actuator 10 includes that turbine is limited Stream device 101 and pressure voltage stabilizing pressure controller 102, turbine current limiter 101 includes turbine structure 103 and secondary speed controller 104, pressure Strong voltage stabilizing pressure controller 102 includes the gentle pressure piston 106 of slow pressure storage stream cylinder 105 and barostat 107, delays pressure storage stream cylinder 105 Top UNICOM circulating line 6, delays the bottom UNICOM barostat 107 of pressure storage stream cylinder 105, delays pressure piston 106 installed in slow pressure In storage stream cylinder 105；When in circulating line 6, the pressure of working medium or flow velocity change, turbine current limiter 101 can be by limiting whirlpool The rotation of wheel construction 103 and realize the restriction of flow velocity, while part working medium can be postponed, pressure storage stream cylinder 105 flows out or flows into and realizes body The expansion of product or compression, so as to realize the effect of stable pressure.
By testing to the solar energy dynamical system for being condensed based on multi-stage booster in above-described embodiment 11, By the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, In the case of sink temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is according to the solar energy dynamical system for being condensed based on multi-stage booster Operation stability be adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 9%, When working medium gasification temperature is 55 DEG C or so, heat energy transformation efficiency is about 10.6%, when working medium gasification temperature is 60 DEG C or so, heat energy Transformation efficiency is about 13.2%, and when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 17.4%, working medium gasification temperature During for 70 DEG C or so, heat energy transformation efficiency is about 47%, the solar heat motility in the present embodiment ten based on multi-stage booster condensation The heat energy transformation efficiency of system is than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very low, and efficiency is low In 5%）Compare, the heat energy transformation efficiency of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment is than conventional The heat energy transformation efficiency mean height 11.6% or so of solar power plant.
Embodiment 12（As shown in figure 14）：It is with 11 difference of embodiment：In order to increase turbine air inlet With the pressure reduction of air vent, the exhaust ports of the turbine 3 are additionally provided with precondenser 36.
Being further elaborated with as above-described embodiment, the precondenser 36 includes working medium conduction pipe 361 and condensation Endothermic tube 362, working medium conduction pipe 361 is used for connecting air vent and circulating line 6, and condensation endothermic tube 362 is led for absorbing working medium The heat of working medium in siphunculus 361, working medium conduction pipe 361 and condensation 362 spiral paratactic contact of endothermic tube, in condensation endothermic tube 362 For heat recipient fluid, it is to increase condensation efficiency, the flow direction phase of the flow direction of heat recipient fluid and working medium in working medium conduction pipe 361 Instead.
By testing to the solar energy dynamical system for being condensed based on multi-stage booster in above-described embodiment 12, By the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, In the case of sink temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is according to the solar energy dynamical system for being condensed based on multi-stage booster Operation stability be adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 9.2%, when working medium gasification temperature is 55 DEG C or so, heat energy transformation efficiency is about 10.8%, when working medium gasification temperature is 60 DEG C or so, Heat energy transformation efficiency is about 13.6%, and when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 17.8%, and working medium gasifies When temperature is 70 DEG C or so, heat energy transformation efficiency is about 19%, the solar energy in the present embodiment ten based on multi-stage booster condensation The heat energy transformation efficiency of dynamical system is than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very low, effect Rate is less than 5%）Compare, the heat energy transformation efficiency ratio of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment The heat energy transformation efficiency mean height 11.4% or so of conventional solar power plant.
Embodiment 13（As shown in figure 15）：It is with 12 difference of embodiment：The condensation endothermic tube 362 is adopted Circulating line 6 between UNICOM one-way hydraulic pump 9 and heat collector 1；Due to the circulation between one-way hydraulic pump 9 and heat collector Pipeline 6 needs heat absorption, and in working medium conduction pipe 361, working medium needs heat extraction, and the structure largely recycles circulating line 6 Interior working medium heat, increases thermal transition efficiency.
By testing to the solar energy dynamical system for being condensed based on multi-stage booster in above-described embodiment 13, By the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, In the case of sink temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is according to the solar energy dynamical system for being condensed based on multi-stage booster Operation stability be adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 9.4%, when working medium gasification temperature is 55 DEG C or so, heat energy transformation efficiency is about 11%, when working medium gasification temperature is 60 DEG C or so, heat Energy transformation efficiency is about 13.8%, and when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 17.8%, working medium gasification temperature When spending for 70 DEG C or so, heat energy transformation efficiency is about 19.1%；Solar energy in the present embodiment ten based on multi-stage booster condensation The heat energy transformation efficiency of dynamical system is than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very low, effect Rate is less than 5%）Compare, the heat energy transformation efficiency ratio of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment The heat energy transformation efficiency mean height 11.9% or so of conventional solar power plant.
Embodiment 14（As shown in figure 16）：It is with 13 difference of embodiment：The oblique type of 51 one-tenth of the condensing tube divides Cloth.
By testing to the solar energy dynamical system for being condensed based on multi-stage booster in above-described embodiment 14, By the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, In the case of sink temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is according to the solar energy dynamical system for being condensed based on multi-stage booster Operation stability be adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 9.4%, when working medium gasification temperature is 55 DEG C or so, heat energy transformation efficiency is about 11.2%, when working medium gasification temperature is 60 DEG C or so, Heat energy transformation efficiency is about 14%, and when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 18%, working medium gasification temperature During for 70 DEG C or so, heat energy transformation efficiency is about 19.3%, the solar energy in the present embodiment 14 based on multi-stage booster condensation The heat energy transformation efficiency of dynamical system is than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very low, effect Rate is less than 5%）Compare, the heat energy transformation efficiency ratio of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment The heat energy transformation efficiency mean height 11.3% or so of conventional solar power plant.
Embodiment 15（As shown in figure 17）：It is with one difference of embodiment：51 one-tenth vertical distribution of the condensing tube.
By testing to the solar energy dynamical system for being condensed based on multi-stage booster in above-described embodiment 15, By the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, In the case of sink temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is according to the solar energy dynamical system for being condensed based on multi-stage booster Operation stability be adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 9.4%, when working medium gasification temperature is 55 DEG C or so, heat energy transformation efficiency is about 11.2%, when working medium gasification temperature is 60 DEG C or so, Heat energy transformation efficiency is about 14.2%, and when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 18.1%, and working medium gasifies When temperature is 70 DEG C or so, heat energy transformation efficiency is about 49.5%；Solar energy in the present embodiment 15 based on multi-stage booster condensation The heat energy transformation efficiency of dynamic system of heat energy is than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very Low, efficiency is less than 5%）Compare, the heat energy conversion effect of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment Rate is than the heat energy transformation efficiency mean height 11.7% of conventional solar power plant.
Embodiment 16（As shown in figure 18）：It is with one difference of embodiment：51 one-tenth horizontal distribution of the condensing tube When, upper and lower layer condensing tube mutually staggers.
By testing to the solar energy dynamical system for being condensed based on multi-stage booster in above-described embodiment 16, By the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, In the case of sink temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is according to the solar energy dynamical system for being condensed based on multi-stage booster Operation stability be adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 9.4%, when working medium gasification temperature is 55 DEG C or so, heat energy transformation efficiency is about 11.2%, when working medium gasification temperature is 60 DEG C or so, Heat energy transformation efficiency is about 14%, and when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 18%, working medium gasification temperature During for 70 DEG C or so, heat energy transformation efficiency is about 19.3%, the solar energy in the present embodiment 16 based on multi-stage booster condensation The heat energy transformation efficiency of dynamical system is than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very low, effect Rate is less than 5%）Compare, the heat energy transformation efficiency ratio of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment The heat energy transformation efficiency mean height 11.3% or so of conventional solar power plant.
Embodiment 17（As shown in figure 19）：It is with 16 difference of embodiment：The condensing tube 51 passes through the temperature difference Generating piece 511 is made, and the thermo-electric generation sheet 511 includes sheet metal 512, p-type semiconductor 513, n-type semiconductor 514, insulation base Matter layer 515 and output electrode 516, dielectric substrate layer 515 is uniformly interspersed with p-type semiconductor 513 and n-type semiconductor 514, uniform point The p-type semiconductor 513 and n-type semiconductor 514 of cloth is connected by sheet metal 512, p-type semiconductor 513 and n-type semiconductor 514 Series connection whole story end connects output electrode 516 respectively；516 voltage of output electrode of thermo-electric generation sheet 511 reaches more than 3V.
Illustrate, 516 end of output electrode of the thermo-electric generation sheet 511 is successively as having further for above-mentioned embodiment Manostat 517, booster transformer 518, accumulator 519 is connected with, accumulator 519 is used for heat emission fan 52, the confession of one-way hydraulic pump 9 Electricity.
By testing to the solar energy dynamical system for being condensed based on multi-stage booster in above-described embodiment 17, By the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, In the case of sink temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is according to the solar energy dynamical system for being condensed based on multi-stage booster Operation stability be adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 9.8%, when working medium gasification temperature is 55 DEG C or so, heat energy transformation efficiency is about 11.8%, when working medium gasification temperature is 60 DEG C or so, Heat energy transformation efficiency is about 14.6%, and when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 18.1%, and working medium gasifies When temperature is 70 DEG C or so, heat energy transformation efficiency is about 19.5%；Solar energy in the present embodiment 17 based on multi-stage booster condensation The heat energy transformation efficiency of dynamic system of heat energy is than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very Low, efficiency is less than 5%）Compare, the heat energy conversion effect of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment Rate is than the heat energy transformation efficiency mean height 11.8% of conventional solar power plant.
Embodiment 18：It is with 17 difference of embodiment：The cycle fluid 7 is using conventional freon；Adopt With freon as working medium, can be used for the utilization of lower temperature thermal source, but as which needs the pressure in circulating line 6 higher, Implementation process requires higher to the processing technology of circulating line 6 and seal member.
By testing to the solar energy dynamical system for being condensed based on multi-stage booster in above-described embodiment 18, By the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, In the case of sink temperature is 18 DEG C, the pressure of working medium in condensing units 5 is heightened, while sender matter pressure in gasification installation 2 is heightened, is followed In endless tube, refrigerant flow rate is adjusted according to the operation stability of the solar energy dynamical system for being condensed based on multi-stage booster；Real Testing effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 9.2%, and working medium gasification temperature is 55 DEG C or so When, heat energy transformation efficiency is about 11.2%, and when working medium gasification temperature is 60 DEG C or so, heat energy transformation efficiency is about 14%, working medium gas When changing temperature for 65 DEG C or so, heat energy transformation efficiency is about 18%, when working medium gasification temperature is 70 DEG C or so, heat energy transformation efficiency About 19.3%, the heat energy transformation efficiency ratio of the solar energy dynamical system for being condensed based on multi-stage booster in the present embodiment 18 Conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very low, and efficiency is less than 5%）Compare, the present embodiment The heat energy transformation efficiency of the solar energy dynamical system for being condensed based on multi-stage booster is than the heat energy of conventional solar power plant Transformation efficiency mean height 11.2% or so.
Embodiment 19：It is with 17 difference of embodiment：The cycle fluid 7 adopts methanol；This kind of working medium Boiling point at normal temperatures is 64.7 DEG C, easily gasifies, relatively low to the temperature requirement of high temperature heat source, can be used for the low temperature less than 100 DEG C Heat resource power generation, but belong to poisonous and harmful inflammable gas, the sealing requirements height to circulating line.
By testing to the solar energy dynamical system for being condensed based on multi-stage booster in above-described embodiment 19, By the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, In the case of sink temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is according to the solar energy dynamical system for being condensed based on multi-stage booster Operation stability be adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 9.4%, when working medium gasification temperature is 55 DEG C or so, heat energy transformation efficiency is about 11.4%, when working medium gasification temperature is 60 DEG C or so, Heat energy transformation efficiency is about 14.2%, and when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 18.1%, and working medium gasifies When temperature is 70 DEG C or so, heat energy transformation efficiency is about 49.5%；Solar energy in the present embodiment 19 based on multi-stage booster condensation The heat energy transformation efficiency of dynamic system of heat energy is than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very Low, efficiency is less than 5%）Compare, the heat energy conversion effect of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment Rate is than the heat energy transformation efficiency mean height 11.7% or so of conventional solar power plant.
Embodiment 20：It is with 17 difference of embodiment：The cycle fluid 7 adopts ethanol；This kind of working medium Boiling point at normal temperatures is 78.15 DEG C, and easily gasify incendivity, relatively low to the temperature requirement of high temperature heat source, can be used to be less than 100 DEG C of low temperature heat resource power generation, but the sealing requirements height to circulating line.
By testing to the solar energy dynamical system for being condensed based on multi-stage booster in above-described embodiment 20, By the sunlight in varying strength, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C when, In the case of sink temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is according to the solar energy dynamical system for being condensed based on multi-stage booster Operation stability be adjusted；Experiment effect is：When working medium gasification temperature is 50 DEG C or so, heat energy transformation efficiency is about 9.6%, when working medium gasification temperature is 55 DEG C or so, heat energy transformation efficiency is about 11.6%, when working medium gasification temperature is 60 DEG C or so, Heat energy transformation efficiency is about 14.4%, and when working medium gasification temperature is 65 DEG C or so, heat energy transformation efficiency is about 18%, working medium gasification temperature When spending for 70 DEG C or so, heat energy transformation efficiency is about 19.5%, the solar heat in the present embodiment 20 based on multi-stage booster condensation The heat energy transformation efficiency of active Force system is than conventional thermal energy power machine（Conventional solar power plant, transformation efficiency is very low, Efficiency is less than 5%）Compare, the heat energy transformation efficiency of the solar energy dynamical system based on multi-stage booster condensation of the present embodiment Heat energy transformation efficiency mean height 11.2% or so than conventional solar power plant.
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 (10)

1. a kind of solar energy dynamical system based on multi-stage booster condensation, including heat collector（1）, gasification installation（2）, whirlpool Turbine（3）, Salar light-gathering cover（4）, condensing units（5）, circulating line（6）, cycle fluid（7）With one-way hydraulic pump（9）, collection Thermal（1）, gasification installation（2）, turbine（3）, condensing units（5）With one-way hydraulic pump（9）Pass sequentially through circulation pipe（6）Road Realize circulation UNICOM, circulating line（6）It is contained within cycle fluid（7）, condensing units（5）Comprising condensing tube（51）, it is characterized in that： The heat collector（1）And gasification installation（2）Installed in Salar light-gathering cover（4）Interior, the heat collector（1）Including solar energy Thermal-collecting tube（11）And solar heat collector（12）, solar heat collector（12）Parallel interval is distributed, solar energy heat collection pipe（11）Folding Type is distributed in solar heat collector（12）In, gasification installation（2）Including solar energy gasification heat-absorbing chamber（21）With gasification pressure controller （22）, gasify pressure controller（22）Installed in solar energy gasification heat-absorbing chamber（21）Interior, gasify pressure controller（22）For circulation industrial Quality Control Pressure, the condensing units（5）Including condensing tube（51）, heat emission fan（52）With multiple booster bodies (53）, heat emission fan（52）Install In condensing tube（51）Above or below, booster body (53）Condensing tube is evenly distributed on step by step（51）Middle part, the booster body (53）Including pressurized cylinder (531）, piston (532）, eccentric (533）, air inlet (534）, gas outlet (535）, breather cheek valve (536）, unidirectional air outlet valve (537）With gas-pressure adjustable valve (538）, piston (532）Installed in pressurized cylinder (531）Interior, piston (532） By push rod by eccentric (533）Drive, pressurized cylinder (531）Bottom is provided with air inlet (534）With gas outlet (535）, air inlet Mouth (534）Place is provided with breather cheek valve (536）, gas outlet (535）Unidirectional air outlet valve (537 is installed）With gas-pressure adjustable valve (538）, condensing units（5）With gasification installation（2）Between be additionally provided with contaminant filter pump（8）.
2. the solar energy dynamical system based on multi-stage booster condensation according to claim 1, is characterized in that：The increasing Press mechanism (53）Also include differential pressure sensor (533）With automatic controller (534）, automatic controller (534）By analyzing pressure reduction Induction apparatuss (533）Signal to turbine pressure regulator (532）Automatically controlled.
3. the solar energy dynamical system based on multi-stage booster condensation according to claim 2, is characterized in that：Described too Sun can gasify heat-absorbing chamber（21）With solar energy heat collection pipe（11）Between be additionally provided with atomizing mouth（23）.
4. the solar energy dynamical system based on multi-stage booster condensation according to claim 3, is characterized in that：Described too Sun can gasify heat-absorbing chamber（21）Horizontal cross-section in Rhizoma Nelumbinis poroid.
5. the solar energy dynamical system based on multi-stage booster condensation according to claim 3, is characterized in that：Described too Sun can gasify heat-absorbing chamber（21）Horizontal cross-section all poroid in honeycomb.
6. the solar energy dynamical system based on multi-stage booster condensation according to claim 3, is characterized in that：Described too Sun can heat collecting sheet（12）In planar sheet.
7. the solar energy dynamical system based on multi-stage booster condensation according to claim 3, is characterized in that：Described too Sun can heat collecting sheet（12）Lamellar in curved surface.
8. the solar energy dynamical system based on multi-stage booster condensation according to claim 3, is characterized in that：Described too Sun can heat collecting sheet（12）It is in be in staggered distribution.
9. the solar energy dynamical system based on multi-stage booster condensation according to claim 3, is characterized in that：Described too Sun can gasify heat-absorbing chamber（21）Positioned at Salar light-gathering cover（4）Extraction regions, solar energy gasify heat-absorbing chamber（21）Using full glass Heat absorption material or the fit heat absorption material of glass metal.
10. the solar energy dynamical system based on multi-stage booster condensation according to claim 1, is characterized in that：Described Turbine（3）For any one in conventional steam turbine, multiple-stage steam turbine, tesla's turbine or radial outward flow turbine Kind.
CN201610760145.0A 2016-08-30 2016-08-30 Solar heat energy power system based on multistage pressurization condensation Withdrawn CN106438239A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610760145.0A CN106438239A (en) 2016-08-30 2016-08-30 Solar heat energy power system based on multistage pressurization condensation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610760145.0A CN106438239A (en) 2016-08-30 2016-08-30 Solar heat energy power system based on multistage pressurization condensation

Publications (1)

Publication Number Publication Date
CN106438239A true CN106438239A (en) 2017-02-22

Family

ID=58090204

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610760145.0A Withdrawn CN106438239A (en) 2016-08-30 2016-08-30 Solar heat energy power system based on multistage pressurization condensation

Country Status (1)

Country Link
CN (1) CN106438239A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108151209A (en) * 2017-12-22 2018-06-12 江苏心日源建筑节能科技股份有限公司 Natural energy resources air-conditioning
CN108204520A (en) * 2017-11-21 2018-06-26 卢松华 A kind of new medical oxygen filling apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108204520A (en) * 2017-11-21 2018-06-26 卢松华 A kind of new medical oxygen filling apparatus
CN108151209A (en) * 2017-12-22 2018-06-12 江苏心日源建筑节能科技股份有限公司 Natural energy resources air-conditioning

Similar Documents

Publication Publication Date Title
CN106437900A (en) Biomass heat energy power system based on pressurized condensation
CN106438239A (en) Solar heat energy power system based on multistage pressurization condensation
CN106437891A (en) Solar heat energy power system based on eccentric turbine
CN106224037A (en) A kind of exhaust dynamic system of heat energy based on semi-conductor condensation
CN106246259A (en) A kind of oil field based on semi-conductor condensation heat energy from waste gas dynamical system
CN106224032A (en) A kind of exhaust dynamic system of heat energy based on pressure-adjustable voltage stabilizing condensation
CN106437908A (en) Internal combustion engine tail gas utilization heat energy power system based on multistage pressurization condensation
CN106246484A (en) A kind of solar energy dynamical system based on semi-conductor condensation
CN106438240A (en) Solar heat energy power system based on working medium circulating condensation
CN106437899A (en) Solar heat energy power system based on pressure adjusting condensation
CN106246270A (en) A kind of semi-conductor condensation dynamic system of heat energy utilizing nuclear power station heat drain
CN106224029A (en) A kind of solar energy dynamical system based on the gasification of honeycomb chamber
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
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
CN106437888A (en) Biological fermentation heat energy power system based on multistage pressurization condensation
CN106437971A (en) Internal combustion engine tail gas utilization heat energy power system based on eccentric turbine
CN106437893A (en) Heat energy power system for stable temperature gasification
CN106224043A (en) A kind of biofermentation dynamic system of heat energy based on supercharging condensation
CN106224044A (en) A kind of dynamic system of heat energy based on condenser negative pressure
CN106437890A (en) Fuel gas heat energy power system based on multilevel pressurizing condensation
CN106224026A (en) A kind of oil field heat energy from waste gas dynamical system based on pressure-adjustable voltage stabilizing condensation
CN106246272A (en) A kind of multi-stage booster condensation dynamic system of heat energy utilizing nuclear power station heat drain
CN106437887A (en) Biomass heat energy power system based on multistage pressurizing 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
WW01 Invention patent application withdrawn after publication
WW01 Invention patent application withdrawn after publication

Application publication date: 20170222