CN106246485A - A kind of solar energy dynamical system based on supercharging condensation - Google Patents

A kind of solar energy dynamical system based on supercharging condensation Download PDF

Info

Publication number
CN106246485A
CN106246485A CN201610759083.1A CN201610759083A CN106246485A CN 106246485 A CN106246485 A CN 106246485A CN 201610759083 A CN201610759083 A CN 201610759083A CN 106246485 A CN106246485 A CN 106246485A
Authority
CN
China
Prior art keywords
heat
solar energy
working medium
turbine
dynamical 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.)
Withdrawn
Application number
CN201610759083.1A
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 CN201610759083.1A priority Critical patent/CN106246485A/en
Publication of CN106246485A publication Critical patent/CN106246485A/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Withdrawn legal-status Critical Current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
    • 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
    • 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

The invention discloses a kind of solar energy dynamical system based on supercharging condensation, including heat collector, gasification installation, turbine, condensing unit and one-way hydraulic pump pass sequentially through circulating line and realize circulation UNICOM, circulating line is contained within cycle fluid, heat collector and gasification installation is had to be arranged in Salar light-gathering cover, condensing unit is arranged on outside Salar light-gathering cover, condensing unit includes condensing tube, heat emission fan and booster body, booster body is arranged on condensing tube middle-end, described booster body includes charging turbine and turbine pressure regulator, turbine pressure regulator controls to connect charging turbine；Solar energy dynamical system based on supercharging condensation of the present invention has condensing rate faster, can reduce condensation row's energy, improve heat energy transformation efficiency, and stable, power adjustable.

Description

A kind of solar energy dynamical system based on supercharging condensation
Technical field
The invention belongs to utilization of energy apparatus field, a kind of solar energy dynamical system based on supercharging 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 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.The substance of the energy strategy of current China is: adheres to economization at first, base oneself upon Domestic, diverse development, depend on science and technology, protect environment, strengthen international mutual beneficial co-operation, make 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 adjusts, and accelerates the upgrading and optimization of industrial structure, sends 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 promotes 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, encourage the popularization and application of energy-efficient product, greatly develop 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, study and define and encourage energy-conservation property tax Policy.Advocate social energy conservation, conduct vigorous propaganda the significance saving the energy, constantly strengthen whole people's resource awareness of unexpected development and save meaning Know.
For response national energy-saving strategy, increasing enterprise starts research and development, uses energy-saving equipment, and strengthens discarded product Can thing, the utilization of waste heat energy.Wherein, utilize aspect at waste heat, mainly realize surplus energy utility 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 to utilize turbine that heat energy is changed into machine Tool energy, then changes mechanical energy is become electric energy, the generating equipment of this kind of principle classification is the most ripe, and kind is many；Another kind of is to utilize Pyroelectric effect principle, is directly translated into electric potential energy by thermoelectric conversion element by heat energy, but due to for generation technology aspect not Maturation, 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 turbine, then changes mechanical energy is become electric energy.Such heat existing Generating equipment can mainly include cycle fluid, heat collector, gasification installation, turbine, electromotor and condensing unit；During work, Cycle fluid first passes through gasification installation in circulating line, working medium is gasified and promotes turbine to rotate, and turbine drives to be sent out Electric power generation, the working medium after gasification, when by turbine, externally does work, and temperature and air pressure can reduce, and pass through condensing unit It is cooled to liquid refrigerant.
But, existing thermal generating equipment common problem is: a. is high to the temperature requirement of high temperature heat source, one As more than 200 DEG C, and heat energy transformation efficiency is on the low side, and heat energy transformation efficiency is generally 15% to 35%；B. the hot type of condensing unit Amount is relatively big, and thermal waste is big, slow by the condensation rate of natural condensation mode, and use actively condensing mode (blower fan air-cooled or Liquid pump water-cooled) need extra power consumption；C. the problem that turbine easily occurs leaking working medium；D. secondary speed is unstable, and easily goes out Existing stuck problem；E. the Heat-collecting effect of heat collector is the best, and extraneous exhaust-heat absorption rate is little, and f. working medium gasification temperature is unstable, work Matter condensation effect is the best, and working medium is apt to deteriorate or impurity occurs；G. existing equipment volume is bigger.
Existing solar energy is realizing power output procedure, first has to photoelectric effect, changes into electric energy, the most again by electronic Equipment output power；Present stage, solar energy changes into the equipment of electric energy and is mainly electro-optical package, and this photoelectric conversion process efficiency is very Low, efficiency is generally about 5%, and energy waste is serious.
Summary of the invention
The purpose that the present invention is to be realized is: efficiently utilize solar energy, improves the heat energy transformation efficiency of thermal hardware, reduces Hot type amount and thermal waste, stablize working medium gasification temperature and refrigerant flow rate, improve working medium quality, prevent working medium go bad, improve Turbine structure, it is to avoid turbine is revealed and rotary speed unstabilization, improves condensing unit, accelerates condensing rate；To solve above-mentioned background skill In art existing for existing thermal hardware: heat energy transformation efficiency is low, working medium gasification temperature is unstable, and working medium condensation effect is the best, Working medium is apt to deteriorate or impurity occurs, and refrigerant leakage easily occurs in turbine, and secondary speed is unstable and card easily occurs Extremely, 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 solar energy based on supercharging condensation Dynamical system, including heat collector, gasification installation, turbine, Salar light-gathering cover, condensing unit, circulating line, cycle fluid With one-way hydraulic pump, it is real that heat collector, gasification installation, turbine, condensing unit and one-way hydraulic pump pass sequentially through circulating line Now circulating UNICOM, circulating line is contained within cycle fluid；
It is characterized in that: described heat collector and gasification installation are arranged in Salar light-gathering cover, described condensing unit is arranged on to be kept away Light plenum area, described 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 arranged in solar energy gasification heat-absorbing chamber, and gasification pressure controller is for cycle fluid blood pressure lowering；When high-pressure liquid work Matter reaches heat source temperature after fully heating in solar energy heat collection pipe, high-pressure liquid working medium flows into solar energy gasification heat-absorbing chamber, too The gasification pressure controller that sun can gasify in heat-absorbing chamber is controlled by pressure so that it is liquid refrigerant endothermic gasification, and gasification working medium is at turbine Blood pressure lowering acting in machine；This kind of structure is compared in solar energy heat collection pipe direct gasification, and can be prevented effectively from gasification working medium to mix has Liquid refrigerant, can make working medium gasify evenly；
Described condensing unit includes condensing tube and heat emission fan, and condensing tube uniformly divides Multi-layers distributing, the mutual UNICOM of condensing tube, heat emission fan Being arranged on above or below condensing tube, heat emission fan drives with convulsion mode or pressure wind mode；
Described condensing unit also has additional booster body, and booster body is arranged on condensing tube middle-end, and described booster body includes increasing Pressure turbine and turbine pressure regulator, turbine pressure regulator controls to connect charging turbine；Use this structure can reduce turbine outlet Pressure, increases the pressure reduction with place of giving vent to anger at turbine inlet, thus increases expanding gas amount of work in the turbine, and reduce swollen The temperature of flatulence body, thus, this structure can produce preferable condensation effect, and improves the heat energy conversion ratio of dynamic system of heat energy.
Optimizing further, described booster body also includes differential pressure sensor and automatic controller, and automatic controller is by dividing Turbine pressure regulator is automatically controlled by the signal of analysis differential pressure sensor.
Optimize further, between condensing unit and heat collector, be additionally provided with contaminant filter pump.
Optimize further, between described solar energy gasification heat-absorbing chamber and solar energy heat collection pipe, be additionally provided with atomizing mouth.
Optimizing further, the horizontal cross-section of described solar energy gasification heat-absorbing chamber is that Rhizoma Nelumbinis is poroid.
Optimizing further, the horizontal cross-section of described solar energy gasification heat-absorbing chamber is all poroid in honeycomb.
Optimizing further, described solar energy gasification heat-absorbing chamber 21 is positioned at the extraction regions of Salar light-gathering cover, and solar energy gasifies Heat-absorbing chamber uses full glass heat absorption material or glass metal zoarium heat absorption material.
Optimizing further, turbine is conventional steam turbine.
Optimizing further, turbine is the steam turbine comprising multistage blade.
Optimizing further, turbine is tesla's turbine.
Optimizing further, turbine is radial outward flow turbine.
Optimizing further, the exhaust ports of described turbine is provided with precondenser；Take this structure can increase air inlet With the pressure reduction of air vent, improve the transformation efficiency of turbine.
Optimizing further, described precondenser includes working medium conduction pipe and condensation endothermic tube, and working medium conduction pipe is used for connecting Air vent and circulating line, condensation endothermic tube is for absorbing the heat of working medium conducting 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, for increasing condensation efficiency, the flow direction of heat recipient fluid and work The flow direction of matter conducting intraductal working medium is contrary.
Optimizing further, described condensation endothermic tube uses the circulating line between UNICOM's one-way hydraulic pump and heat collector； Owing to 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 recycles working medium heat in circulating line largely, increases thermal transition efficiency.
Optimizing further, described condensing tube becomes oblique type to be distributed.
Optimizing further, described condensing tube becomes horizontal or vertical distribution.
Optimizing further, when described condensing tube becomes horizontal distribution, upper and lower layer condensing tube mutually staggers.
Optimizing further, described condensing tube is copper metal tube or stability alloying metal pipe.
Optimizing further, described condensing tube is made by thermo-electric generation sheet, and 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 end at the whole story of connecting of p-type semiconductor and n-type semiconductor Connect output electrode respectively.
Optimizing further, the output electrode end of described 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 liquefaction uncooled in condensing tube enters one-way hydraulic pump, condensing tube tail end It is provided with catch box.
Optimizing further, in order to accelerate heat radiation, condensing unit is additionally provided with fin.
Optimizing further, described cycle fluid uses propanol.
Optimizing further, described cycle fluid uses methanol.
Optimizing further, described cycle fluid uses ethanol.
Optimizing further, described cycle fluid uses isopropanol.
Optimizing further, described cycle fluid uses liquefied ammonia.
Optimizing further, described cycle fluid uses conventional freon.
Optimizing further, be additionally provided with working medium actuator between turbine and condensing unit, described 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 slow pressure storage stream cylinder gentle pressure piston and barostat, the top UNICOM circulating line of slow pressure storage stream cylinder, slow pressure storage The bottom UNICOM barostat of stream cylinder, slow pressure piston is arranged in slow pressure storage stream cylinder；When in circulating line working medium pressure or When flow velocity changes, turbine current limiter can realize the restriction of flow velocity by limiting the rotation of turbine structure, part work simultaneously Matter can be postponed and be pressed storage stream cylinder to flow out or flow into expansion or the compression realizing volume, thus the effect of pressure is stablized in realization.
Operation principle: solar energy dynamical system based on supercharging condensation described in this invention, during work, cycle fluid exists Absorb heat in heat collector the heat source temperature that reaches a high temperature, then flows in gasification installation, is vaporized heat absorption, work by blood pressure lowering in a small amount Flow to turbine after matter gasification, drive rotating turbine；After gasification working medium flows through turbine, owing to externally doing work, its working medium temperature Degree and air pressure all can reduce, and cause part working medium to liquefy；After gasification working medium flows through turbine, working medium flows to working medium regulation successively Device and condensing unit；Working medium actuator is for controlling the pressure of working medium, flow velocity in circulating line, and working medium actuator can be according to the external world Heat absorption district and the temperature conditions of heat release zone, regulation working medium condensing temperature or gasification temperature, convert it is thus possible to be effectively improved heat energy Efficiency；Working medium can be liquefied by condensing unit completely；After liquefaction, working medium sequentially passes through contaminant filter pump and one-way hydraulic pump, impurity mistake Filter pump can by contaminant filter in working medium out, and working medium is carried out unidirectional pumping supercharging by one-way hydraulic pump；Working medium warp successively after liquefaction After crossing contaminant filter pump and one-way hydraulic pump, and it is again introduced into gasification installation, completes a circulation.
Solar energy dynamical system based on supercharging condensation of the present invention is by arranging supercharger in condensing unit Structure, it is possible to decrease the pressure of turbine outlet, increases the pressure reduction with place of giving vent to anger at turbine inlet, thus increases expanding gas and exist Amount of work in turbine, and reduce the temperature of expanding gas largely；Thus, this structure can produce and preferably condense effect Really, and improve the heat energy conversion ratio of dynamic system of heat energy.
Beneficial effect: solar energy dynamical system based on supercharging condensation of the present invention, in hinge structure Heat energy machine, there is advantage and the progress of following several respects: 1. by setting up booster body in condensing unit, increase gas whirlpool The amount of work of turbine, can improve condensing rate largely, reduces condensation power consumption, and improves system heat energy conversion ratio；2. logical Cross and set up precondenser, it is possible to increase air inlet and the pressure reduction of air vent in turbine, and the heat energy of working medium can be recycled, it is achieved Heat absorption and heat rejection process to cycle fluid difference section comprehensively utilize, and reduce thermal waste and cooling power consumption；3. pass through Set up contaminant filter pump and one-way hydraulic pump, can effectively prevent working medium rotten and more impurity occurs, and preventing working medium from refluxing； 4. by setting up working medium actuator, pressure and flow to working medium are controlled, and can be effectively improved gasification usefulness and condensation efficiency, And stablize working medium gasification temperature and refrigerant flow rate, prevent sealing member deformation bigger, it is to avoid secondary speed is unstable and working medium is revealed and asked Topic；5. condensing tube uses thermo-electric generation sheet make, the temperature difference calorific potential utilizing condensation process can be divided, improve heat energy transformation efficiency, And the electric current produced in utilizing thermo-electric generation sheet accelerates thermal energy conduction speed；The most efficiently make use of solar energy, it is achieved the sun is active Power exports.
Accompanying drawing explanation
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 unit 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 unit vertical cross section structural representation of the present invention program 14；
Figure 17 is the condensing unit vertical cross section structural representation of the present invention program 15；
Figure 18 is the condensing unit vertical cross section structural representation of the present invention program 16；
Figure 19 is the thermo-electric generation chip architecture schematic diagram of the present invention program 17；
In figure:
1 be heat collector, 11 be solar energy heat collection pipe, 12 for solar heat collector；
2 be gasification installation, 21 be solar energy gasification heat-absorbing chamber, 22 for gasification pressure controller, 221 for differential pressure control valve, 222 for gasification Pressure induction apparatus, 23 it is atomizing mouth；
3 be turbine, 36 for precondenser, 361 for working medium conduction pipe, 362 for condensation endothermic tube；
4 is Salar light-gathering cover；
5 be condensing unit, 51 be condensing tube, 511 be thermo-electric generation sheet, 512 be sheet metal, 513 be p-type semiconductor, 514 for n Type quasiconductor, 515 be dielectric substrate layer, 516 be output electrode, 517 be manostat, 518 be booster transformer, 519 for electric power storage Pond, 52 be heat emission fan, 53 for booster body, 531 for charging turbine, 532 for turbine pressure regulator, 533 for differential pressure sensor, 534 For automatic controller, 54 be catch box, 55 for fin；
6 is circulating line；
7 is cycle fluid；
8 is contaminant filter pump；
9 is one-way hydraulic pump；
10 be working medium actuator, 101 be turbine current limiter, 102 be pressure voltage stabilizing pressure controller, 103 be turbine structure, 104 for whirlpool Wheel speed controller, 105 be slow pressure storage stream cylinder, 106 be slow pressure piston, 107 be barostat.
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 solar energy dynamical system based on supercharging condensation, including heat collector 1, gasification installation 2, turbine 3, Salar light-gathering cover 4, condensing unit 5, circulating line 6, cycle fluid 7 and one-way hydraulic pump 9, Heat collector 1, gasification installation 2, turbine 3, condensing unit 5 and one-way hydraulic pump 9 pass sequentially through circulating line 6 and realize circulation connection Logical, circulating line 6 is contained within cycle fluid 7；
(as shown in Figure 2) described heat collector 1 and gasification installation 2 are arranged in Salar light-gathering cover 4, and described heat collector 1 wraps Including solar energy heat collection pipe 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；Gasification installation 2 includes solar energy gasification heat-absorbing chamber 21 and gasification pressure controller 22, gasification control Depressor 22 is arranged in solar energy gasification heat-absorbing chamber 21, and gasification pressure controller 22 is for liquid refrigerant blood pressure lowering；When high-pressure liquid working medium Reaching heat source temperature 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 that it is liquid refrigerant endothermic gasification, and gasify working medium Blood pressure lowering acting in turbine 3；This kind of structure, compared in solar energy heat collection pipe 11 direct gasification, can be prevented effectively from gasification working medium In mix and have liquid refrigerant, working medium can be made to gasify evenly.
Having explanation further as above-mentioned embodiment, described condensing unit 5 is arranged on low temperature environment (normal temperature air In or liquid in).
Having explanation further as above-mentioned embodiment, solar heat collector 12 is in planar sheet.
(as shown in Figure 3) described condensing unit 5 includes condensing tube 51, heat emission fan 52 and booster body 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 arranged on 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) described booster body 53 is arranged on condensing tube 51 middle-end, and described booster body 53 includes charging turbine 531 With turbine pressure regulator 532, turbine pressure regulator 532 controls to connect charging turbine 531, and described booster body 53 also includes that pressure reduction senses Device 533 and automatic controller 534, automatic controller 534 is by analyzing the signal of differential pressure sensor 533 to turbine pressure regulator 532 Automatically control；Use this structure can reduce the pressure in turbine 3 exit, with place of giving vent to anger at increase turbine 3 air inlet Pressure reduction, thus increase expanding gas amount of work in turbine 3, and reduce the temperature of expanding gas, thus, this structure can produce Preferably condensation effect, and improve the heat energy conversion ratio of dynamic system of heat energy.
As further illustrating of above-mentioned embodiment, between described condensing unit 5 and heat collector 1, it is additionally provided with impurity Filter pump 8.
As further illustrating of above-mentioned embodiment, (as shown in Figure 5) described solar energy gasification heat-absorbing chamber 21 is by multiple Body is formed side by side.
As further illustrating of above-mentioned embodiment, described gasification pressure controller 22 is by keeping amount pressure with atmospheric pressure Difference realizes pressure control.
As further illustrating of above-mentioned embodiment, described turbine 3 is conventional vane type steam turbine.
As further illustrating of above-mentioned embodiment, described condensing tube 51 tail end is provided with catch box 54.
As further illustrating of above-mentioned embodiment, described condensing unit 5 is additionally provided with fin 55.
As further illustrating of above-mentioned embodiment, described cycle fluid 7 uses liquefied ammonia.
By in above-described embodiment one based on supercharging condensation solar energy dynamical system test, 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 time, in low-temperature receiver temperature In the case of degree is 18 DEG C, stable according to the solar energy dynamical system condensed based on supercharging of refrigerant flow rate in circulation pipe Property is adjusted；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 17%, working medium gasification temperature When degree is about 55 DEG C, heat energy transformation efficiency is about 7%, and when working medium gasification temperature is about 60 DEG C, heat energy transformation efficiency is about 10%, when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 12%, when working medium gasification temperature is about 70 DEG C, and heat Can be about 14.4% by transformation efficiency, in the present embodiment one, the heat energy of solar energy dynamical system based on supercharging condensation converts effect Rate is compared, this enforcement than conventional thermal energy power machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%) The heat energy transformation efficiency of the solar energy dynamical system based on supercharging condensation of example is than the heat energy of conventional solar power plant Transformation efficiency mean height about 7%；Meanwhile, the solar energy dynamical system cooldown rate that the present embodiment condenses based on supercharging is fast, Hot driving is little, runs noise little, good operation stability, can realize power output regulation simultaneously.
Embodiment two (as shown in Fig. 6): be with embodiment one difference: the solar heat collector 12 of heat collector 1 Lamellar in curved surface.
By in above-described embodiment two based on supercharging condensation solar energy dynamical system test, 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 time, in low-temperature receiver temperature In the case of degree is 18 DEG C, stable according to the solar energy dynamical system condensed based on supercharging of refrigerant flow rate in circulation pipe Property is adjusted；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 17.5%, and working medium gasifies When temperature is about 55 DEG C, heat energy transformation efficiency is about 8%, and when working medium gasification temperature is about 60 DEG C, heat energy transformation efficiency is about 10.4%, when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 12.4%, and working medium gasification temperature is about 70 DEG C Time, heat energy transformation efficiency is about 14.8%, and in the present embodiment two, the heat energy of solar energy dynamical system based on supercharging condensation turns Change efficiency to compare than conventional thermal energy power machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%), this The heat energy transformation efficiency of the solar energy dynamical system based on supercharging condensation of embodiment is than conventional solar power plant Heat energy transformation efficiency mean height about 7.8%.
Embodiment three (shown in Fig. 7): be with embodiment one difference: as described in the solar energy heating of heat collector 1 Sheet 12 is in being in staggered distribution.
By in above-described embodiment three based on supercharging condensation solar energy dynamical system test, 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 time, in low-temperature receiver temperature In the case of degree is 18 DEG C, stable according to the solar energy dynamical system condensed based on supercharging of refrigerant flow rate in circulation pipe Property is adjusted；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 17.5%, and working medium gasifies When temperature is about 55 DEG C, heat energy transformation efficiency is about 8.4%, and when working medium gasification temperature is about 60 DEG C, heat energy transformation efficiency is about Being 10.6%, when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 12.6%, and working medium gasification temperature is about 70 DEG C Time, heat energy transformation efficiency is about 15%；In the present embodiment three, the heat energy of solar energy dynamical system based on supercharging condensation converts Efficiency is compared, this reality than conventional thermal energy power machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%) Execute the heat energy transformation efficiency of solar energy dynamical system based on supercharging condensation of example than the heat of conventional solar power plant Can transformation efficiency mean height about 6.2%.
Embodiment four (as shown in Figure 8): be with embodiment one difference: described gasification pressure controller 22 includes pressure reduction control Valve 221 processed and gasification pressure induction apparatus 222, differential pressure control valve 221 is positioned at the front end of solar energy gasification heat-absorbing chamber 21, and gasify pressure Induction apparatus 222 is positioned at solar energy gasification heat-absorbing chamber 21 rear end；Differential pressure control valve 221 is used for regulating pressure reduction, and gasify pressure induction apparatus 222 in sensing solar energy gasification heat-absorbing chamber 21 pressure of working medium, when pressure is bigger, increase the pressure of differential pressure control valve 221 Difference, when pressure is less, reduces the pressure reduction of differential pressure control valve 221, thus realizes the pressure control to solar energy gasification heat-absorbing chamber 21 System.
By in above-described embodiment four based on supercharging condensation solar energy dynamical system test, 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 time, in low-temperature receiver temperature In the case of degree is 18 DEG C, stable according to the solar energy dynamical system condensed based on supercharging of refrigerant flow rate in circulation pipe Property is adjusted；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 5%, working medium gasification temperature When degree is about 55 DEG C, heat energy transformation efficiency is about 8.7%, and when working medium gasification temperature is about 60 DEG C, heat energy transformation efficiency is about 10.8%, when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 13.2%, and working medium gasification temperature is about 70 DEG C Time, heat energy transformation efficiency is about 16.2%, and in the present embodiment four, the heat energy of solar energy dynamical system based on supercharging condensation turns Change efficiency to compare than conventional thermal energy power machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%), this The heat energy transformation efficiency of the solar energy dynamical system based on supercharging condensation of embodiment is than conventional solar power plant Heat energy transformation efficiency mean height about 7.5%.
Embodiment five (as shown in Figure 9): be with embodiment four difference: described solar energy gasification heat-absorbing chamber 21 with too Sun can be additionally provided with atomizing mouth 23 between thermal-collecting tube 11.
Tested, by difference by the solar energy dynamical system based on supercharging condensation of above-described embodiment five The sunlight of intensity, working medium gasification temperature respectively reach 50 DEG C, 55 DEG C, 60 DEG C, 65 DEG C, 70 DEG C time, in sink temperature be In the case of 18 DEG C, in circulation pipe, refrigerant flow rate enters according to the operation stability of the solar energy dynamical system condensed based on supercharging Row sum-equal matrix；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 6%, and working medium gasification temperature is When about 55 DEG C, heat energy transformation efficiency is about 9.2%, and when working medium gasification temperature is about 60 DEG C, heat energy transformation efficiency is about 11.2%, when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 14%, when working medium gasification temperature is about 70 DEG C, Heat energy transformation efficiency is about 17%, and in the present embodiment five, the heat energy of solar energy dynamical system based on supercharging condensation converts effect Rate is compared, this enforcement than conventional thermal energy power machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%) The heat energy transformation efficiency of the solar energy dynamical system based on supercharging condensation of example is than the heat energy of conventional solar power plant Transformation efficiency mean height about 8%.
Embodiment six (as shown in Figure 10): be with embodiment five difference: described solar energy gasification heat-absorbing chamber 21 Horizontal cross-section is that Rhizoma Nelumbinis is poroid.
By in above-described embodiment six based on supercharging condensation solar energy dynamical system test, 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 time, in low-temperature receiver temperature In the case of degree is 18 DEG C, stable according to the solar energy dynamical system condensed based on supercharging of refrigerant flow rate in circulation pipe Property is adjusted；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 7%, working medium gasification temperature When degree is about 55 DEG C, heat energy transformation efficiency is about 9.6%, and when working medium gasification temperature is about 60 DEG C, heat energy transformation efficiency is about 12%, when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 14.8%, when working medium gasification temperature is about 70 DEG C, Heat energy transformation efficiency is about 17.4%, and in the present embodiment six, the heat energy of solar energy dynamical system based on supercharging condensation converts Efficiency is compared, this reality than conventional thermal energy power machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%) Execute the heat energy transformation efficiency of solar energy dynamical system based on supercharging condensation of example than the heat of conventional solar power plant Can transformation efficiency mean height about 9.3%.
Embodiment seven (as shown in figure 11): be with embodiment five difference: described solar energy gasification heat-absorbing chamber 21 Horizontal cross-section is all poroid in honeycomb.
By in above-described embodiment seven based on supercharging condensation solar energy dynamical system test, 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 time, in low-temperature receiver temperature In the case of degree is 18 DEG C, stable according to the solar energy dynamical system condensed based on supercharging of refrigerant flow rate in circulation pipe Property is adjusted；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 7.5%, and working medium gasifies When temperature is about 55 DEG C, heat energy transformation efficiency is about 9.8%, and when working medium gasification temperature is about 60 DEG C, heat energy transformation efficiency is about Being 12.2%, when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 15.5%, and working medium gasification temperature is about 70 DEG C Time, heat energy transformation efficiency is about 17.8%, and in the present embodiment seven, the heat energy of solar energy dynamical system based on supercharging condensation turns Change efficiency to compare than conventional thermal energy power machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%), this The heat energy transformation efficiency of the solar energy dynamical system based on supercharging condensation of embodiment is than conventional solar power plant Heat energy transformation efficiency mean height about 9%.
Embodiment eight: be with embodiment seven difference: described turbine 3 is the steamturbine comprising multistage blade Machine.
By in above-described embodiment eight based on supercharging condensation solar energy dynamical system test, 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 time, in low-temperature receiver temperature In the case of degree is 18 DEG C, stable according to the solar energy dynamical system condensed based on supercharging of refrigerant flow rate in circulation pipe Property is adjusted；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 8.7%, and working medium gasifies When temperature is about 55 DEG C, heat energy transformation efficiency is about 10.4%, when working medium gasification temperature is about 60 DEG C, heat energy transformation efficiency Being about 12.8%, when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 16.6%, and working medium gasification temperature is 70 DEG C of left sides Time right, heat energy transformation efficiency is about 18%, and in the present embodiment eight, the heat energy of solar energy dynamical system based on supercharging condensation turns Change efficiency to compare than conventional thermal energy power machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%), this The heat energy transformation efficiency of the solar energy dynamical system based on supercharging condensation of embodiment is than conventional solar power plant Heat energy transformation efficiency mean height about 10.8%.
Embodiment nine: be with embodiment seven difference: described turbine 3 is tesla's turbine.
By in above-described embodiment nine based on supercharging condensation solar energy dynamical system test, 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 time, in low-temperature receiver temperature In the case of degree is 18 DEG C, stable according to the solar energy dynamical system condensed based on supercharging of refrigerant flow rate in circulation pipe Property is adjusted；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 9%, working medium gasification temperature When degree is about 55 DEG C, heat energy transformation efficiency is about 10.6%, and when working medium gasification temperature is about 60 DEG C, heat energy transformation efficiency is about Being 13%, when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 16.8%, and working medium gasification temperature is about 70 DEG C Time, heat energy transformation efficiency is about 18.4%, and in the present embodiment nine, the heat energy of solar energy dynamical system based on supercharging condensation turns Change efficiency to compare than conventional thermal energy power machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%), this The heat energy transformation efficiency of the solar energy dynamical system based on supercharging condensation of embodiment is than conventional solar power plant Heat energy transformation efficiency mean height about 11.4%.
Embodiment ten: be with embodiment one difference: described turbine 3 is radial outward flow turbine.
By in above-described embodiment ten based on supercharging condensation solar energy dynamical system test, 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 time, in low-temperature receiver temperature In the case of degree is 18 DEG C, stable according to the solar energy dynamical system condensed based on supercharging of refrigerant flow rate in circulation pipe Property is adjusted；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 8.7%, and working medium gasifies When temperature is about 55 DEG C, heat energy transformation efficiency is about 10.4%, when working medium gasification temperature is about 60 DEG C, heat energy transformation efficiency Being about 12.8%, when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 16.8%, and working medium gasification temperature is 70 DEG C of left sides Time right, heat energy transformation efficiency is about 18.1%, the heat energy of solar energy dynamical system based on supercharging condensation in the present embodiment ten Transformation efficiency is compared than conventional thermal energy power machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%), The heat energy transformation efficiency of the solar energy dynamical system based on supercharging condensation of the present embodiment is than conventional solar power plant Heat energy transformation efficiency mean height about 11%.
Embodiment 11 (shown in Figure 12 and 13): be with embodiment ten difference: as described in turbine 3 be centrifugal Working medium actuator 10 it is additionally provided with between turbine 3 and condensing unit 5 described in formula turbine；Working medium actuator 10 includes that turbine limits 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 slow pressure storage stream cylinder 105 gentle pressure piston 106 and barostat 107, slow pressure storage stream cylinder 105 Top UNICOM circulating line 6, the bottom UNICOM barostat 107 of slow pressure storage stream cylinder 105, slow pressure piston 106 is arranged on 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, part working medium pressure storage stream cylinder 105 of can postponing flows out or flows into and realizes body simultaneously Long-pending expansion or compression, thus realize stablizing the effect of pressure.
By the solar energy dynamical system based on supercharging condensation in above-described embodiment 11 is tested, pass through In 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 time, at low-temperature receiver In the case of temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is steady according to the operation of the solar energy dynamical system condensed based on supercharging Qualitative it is adjusted；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 9%, and working medium gasifies When temperature is about 55 DEG C, heat energy transformation efficiency is about 10.6%, when working medium gasification temperature is about 60 DEG C, heat energy transformation efficiency Being about 13.2%, when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 17.4%, and working medium gasification temperature is 70 DEG C of left sides Time right, heat energy transformation efficiency is about 47%, and in the present embodiment ten, the heat energy of solar energy dynamical system based on supercharging condensation turns Change efficiency to compare than conventional thermal energy power machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%), this The heat energy transformation efficiency of the solar energy dynamical system based on supercharging condensation of embodiment is than conventional solar power plant Heat energy transformation efficiency mean height about 11.6%.
Embodiment 12 (as shown in figure 14): be with embodiment 11 difference: in order to increase turbine air inlet With the pressure reduction of air vent, the exhaust ports of described turbine 3 is additionally provided with precondenser 36.
Being further elaborated with as above-described embodiment, described 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 used for absorbing working medium leads The heat of working medium in siphunculus 361, working medium conduction pipe 361 and condensation endothermic tube 362 spiral paratactic contact, in condensation endothermic tube 362 For heat recipient fluid, for increasing condensation efficiency, the flow direction of heat recipient fluid and the flow direction phase of working medium in working medium conduction pipe 361 Instead.
By the solar energy dynamical system based on supercharging condensation in above-described embodiment 12 is tested, pass through In 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 time, at low-temperature receiver In the case of temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is steady according to the operation of the solar energy dynamical system condensed based on supercharging Qualitative it is adjusted；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 9.2%, working medium gas When change temperature is about 55 DEG C, heat energy transformation efficiency is about 10.8%, and when working medium gasification temperature is about 60 DEG C, heat energy converts effect Rate is about 13.6%, and when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 17.8%, and working medium gasification temperature is 70 DEG C During left and right, heat energy transformation efficiency is about 19%, the heat energy of solar energy dynamical system based on supercharging condensation in the present embodiment ten Transformation efficiency is compared than conventional thermal energy power machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%), The heat energy transformation efficiency of the solar energy dynamical system based on supercharging condensation of the present embodiment is than conventional solar power plant Heat energy transformation efficiency mean height about 11.4%.
Embodiment 13 (as shown in figure 15): be with embodiment 12 difference: described condensation endothermic tube 362 uses Circulating line 6 between UNICOM's 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 this structure recycles circulating line 6 largely Interior working medium heat, increases thermal transition efficiency.
By the solar energy dynamical system based on supercharging condensation in above-described embodiment 13 is tested, pass through In 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 time, at low-temperature receiver In the case of temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is steady according to the operation of the solar energy dynamical system condensed based on supercharging Qualitative it is adjusted；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 9.4%, working medium gas When change temperature is about 55 DEG C, heat energy transformation efficiency is about 11%, when working medium gasification temperature is about 60 DEG C, heat energy transformation efficiency Being about 13.8%, when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 17.8%, and working medium gasification temperature is 70 DEG C of left sides Time right, heat energy transformation efficiency is about 19.1%；The heat energy of solar energy dynamical system based on supercharging condensation in the present embodiment ten Transformation efficiency is compared than conventional thermal energy power machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%), The heat energy transformation efficiency of the solar energy dynamical system based on supercharging condensation of the present embodiment is than conventional solar power plant Heat energy transformation efficiency mean height about 11.9%.
Embodiment 14 (as shown in figure 16): be with embodiment 13 difference: described condensing tube 51 becomes oblique type to divide Cloth.
By the solar energy dynamical system based on supercharging condensation in above-described embodiment 14 is tested, pass through In 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 time, at low-temperature receiver In the case of temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is steady according to the operation of the solar energy dynamical system condensed based on supercharging Qualitative it is adjusted；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 9.4%, working medium gas When change temperature is about 55 DEG C, heat energy transformation efficiency is about 11.2%, and when working medium gasification temperature is about 60 DEG C, heat energy converts effect Rate is about 14%, and when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 18%, and working medium gasification temperature is about 70 DEG C Time, heat energy transformation efficiency is about 19.3%, the heat energy of solar energy dynamical system based on supercharging condensation in the present embodiment 14 Transformation efficiency is compared than conventional thermal energy power machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%), The heat energy transformation efficiency of the solar energy dynamical system based on supercharging condensation of the present embodiment is than conventional solar power plant Heat energy transformation efficiency mean height about 11.3%.
Embodiment 15 (as shown in figure 17): be with embodiment one difference: described condensing tube 51 becomes vertical distribution.
By the solar energy dynamical system based on supercharging condensation in above-described embodiment 15 is tested, pass through In 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 time, at low-temperature receiver In the case of temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is steady according to the operation of the solar energy dynamical system condensed based on supercharging Qualitative it is adjusted；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 9.4%, working medium gas When change temperature is about 55 DEG C, heat energy transformation efficiency is about 11.2%, and when working medium gasification temperature is about 60 DEG C, heat energy converts effect Rate is about 14.2%, and when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 18.1%, and working medium gasification temperature is 70 DEG C During left and right, heat energy transformation efficiency is about 49.5%；Solar energy dynamical system based on supercharging condensation in the present embodiment 15 Heat energy transformation efficiency is than conventional thermal energy power machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%) Comparing, the heat energy transformation efficiency of the solar energy dynamical system based on supercharging condensation of the present embodiment is than conventional solar power The heat energy transformation efficiency mean height 11.7% of equipment.
Embodiment 16 (as shown in figure 18): be with embodiment one difference: described condensing tube 51 becomes horizontal distribution Time, upper and lower layer condensing tube mutually staggers.
By the solar energy dynamical system based on supercharging condensation in above-described embodiment 16 is tested, pass through In 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 time, at low-temperature receiver In the case of temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is steady according to the operation of the solar energy dynamical system condensed based on supercharging Qualitative it is adjusted；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 9.4%, working medium gas When change temperature is about 55 DEG C, heat energy transformation efficiency is about 11.2%, and when working medium gasification temperature is about 60 DEG C, heat energy converts effect Rate is about 14%, and when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 18%, and working medium gasification temperature is about 70 DEG C Time, heat energy transformation efficiency is about 19.3%, the heat energy of solar energy dynamical system based on supercharging condensation in the present embodiment 16 Transformation efficiency is compared than conventional thermal energy power machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%), The heat energy transformation efficiency of the solar energy dynamical system based on supercharging condensation of the present embodiment is than conventional solar power plant Heat energy transformation efficiency mean height about 11.3%.
Embodiment 17 (as shown in figure 19): be with embodiment 16 difference: described condensing tube 51 passes through the temperature difference Generating sheet 511 is made, and described 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, uniformly divides P-type semiconductor 513 and the n-type semiconductor 514 of cloth are connected by sheet metal 512, p-type semiconductor 513 and n-type semiconductor 514 Series connection end at the whole story connects output electrode 516 respectively；Output electrode 516 voltage of thermo-electric generation sheet 511 reaches more than 3V.
Having explanation further as above-mentioned embodiment, output electrode 516 end of described thermo-electric generation sheet 511 is successively Connecting and have manostat 517, booster transformer 518, accumulator 519, accumulator 519 is for heat emission fan 52, the confession of one-way hydraulic pump 9 Electricity.
By the solar energy dynamical system based on supercharging condensation in above-described embodiment 17 is tested, pass through In 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 time, at low-temperature receiver In the case of temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is steady according to the operation of the solar energy dynamical system condensed based on supercharging Qualitative it is adjusted；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 9.8%, working medium gas When change temperature is about 55 DEG C, heat energy transformation efficiency is about 11.8%, and when working medium gasification temperature is about 60 DEG C, heat energy converts effect Rate is about 14.6%, and when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 18.1%, and working medium gasification temperature is 70 DEG C During left and right, heat energy transformation efficiency is about 19.4%,；Solar energy dynamical system based on supercharging condensation in the present embodiment 17 Heat energy transformation efficiency than conventional thermal energy power machine, (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%) comparing, the heat energy transformation efficiency of the solar energy dynamical system based on supercharging condensation of the present embodiment is than conventional solar energy The heat energy transformation efficiency mean height 11.8% of power-equipment.
Embodiment 18: be with embodiment 17 difference: described cycle fluid 7 uses the freon of routine；Adopt With freon as working medium, can be used for the utilization of lower temperature thermal source, but owing to it needs the pressure in circulating line 6 higher, The processing technology of circulating line 6 and seal member is required higher by implementation process.
By the solar energy dynamical system based on supercharging condensation in above-described embodiment 18 is tested, pass through In 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 time, at low-temperature receiver In the case of temperature is 18 DEG C, heightens the pressure of working medium in condensing unit 5, heighten sender matter pressure in gasification installation 2, circulation pipe simultaneously Interior refrigerant flow rate is adjusted according to the operation stability of the solar energy dynamical system condensed based on supercharging；Experiment effect For: when working medium gasification temperature is about 50 DEG C, heat energy transformation efficiency is about 9.2%, when working medium gasification temperature is about 55 DEG C, heat Can be about 11.2% by transformation efficiency, when working medium gasification temperature is about 60 DEG C, heat energy transformation efficiency is about 14%, working medium gasification temperature When being about 65 DEG C, heat energy transformation efficiency is about 18%, and when working medium gasification temperature is about 70 DEG C, heat energy transformation efficiency is about 19.3%, in the present embodiment 18, the heat energy transformation efficiency of solar energy dynamical system based on supercharging condensation is than conventional warm Motility machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%) is compared, the present embodiment based on supercharging The heat energy transformation efficiency of the solar energy dynamical system of condensation is average than the heat energy transformation efficiency of conventional solar power plant High by about 11.2%.
Embodiment 19: be with embodiment 17 difference: described cycle fluid 7 uses 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, high to the sealing requirements of circulating line.
By the solar energy dynamical system based on supercharging condensation in above-described embodiment 19 is tested, pass through In 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 time, at low-temperature receiver In the case of temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is steady according to the operation of the solar energy dynamical system condensed based on supercharging Qualitative it is adjusted；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 9.4%, working medium gas When change temperature is about 55 DEG C, heat energy transformation efficiency is about 11.4%, and when working medium gasification temperature is about 60 DEG C, heat energy converts effect Rate is about 14.2%, and when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 18.1%, and working medium gasification temperature is 70 DEG C During left and right, heat energy transformation efficiency is about 49.5%；Solar energy dynamical system based on supercharging condensation in the present embodiment 19 Heat energy transformation efficiency is than conventional thermal energy power machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%) Comparing, the heat energy transformation efficiency of the solar energy dynamical system based on supercharging condensation of the present embodiment is than conventional solar power The heat energy transformation efficiency mean height about 11.7% of equipment.
Embodiment 20: be with embodiment 17 difference: described cycle fluid 7 uses 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 for being less than The low temperature heat resource power generation of 100 DEG C, but high to the sealing requirements of circulating line.
By the solar energy dynamical system based on supercharging condensation in above-described embodiment 20 is tested, pass through In 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 time, at low-temperature receiver In the case of temperature is 18 DEG C, in circulation pipe, refrigerant flow rate is steady according to the operation of the solar energy dynamical system condensed based on supercharging Qualitative it is adjusted；Experiment effect is: when working medium gasification temperature is about 50 DEG C, and heat energy transformation efficiency is about 9.6%, working medium gas When change temperature is about 55 DEG C, heat energy transformation efficiency is about 11.6%, and when working medium gasification temperature is about 60 DEG C, heat energy converts effect Rate is about 14.4%, and when working medium gasification temperature is about 65 DEG C, heat energy transformation efficiency is about 18%, and working medium gasification temperature is 70 DEG C of left sides Time right, heat energy transformation efficiency is about 19.5%, the heat of solar energy dynamical system based on supercharging condensation in the present embodiment 20 Energy transformation efficiency is than conventional thermal energy power machine (conventional solar power plant, transformation efficiency is the lowest, and efficiency is less than 5%) phase Ratio, the heat energy transformation efficiency of the solar energy dynamical system based on supercharging condensation of the present embodiment sets than conventional solar power Standby heat energy transformation efficiency mean height about 11.2%.
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 (10)

1. a solar energy dynamical system based on supercharging condensation, including heat collector (1), gasification installation (2), turbine (3), Salar light-gathering cover (4), condensing unit (5), circulating line (6), cycle fluid (7) and one-way hydraulic pump (9), collection hot charging Put (1), gasification installation (2), turbine (3), condensing unit (5) and one-way hydraulic pump (9) and pass sequentially through the realization of circulation pipe (6) road Circulation UNICOM, circulating line (6) is contained within cycle fluid (7), and condensing unit (5) comprises condensing tube (51), it is characterized in that: described Heat collector (1) and gasification installation (2) are arranged in Salar light-gathering cover (4), and described heat collector (1) includes solar energy heating Pipe (11) and solar heat collector (12), solar heat collector (12) parallel interval is distributed, and solar energy heat collection pipe (11) fold-type divides Cloth is in solar heat collector (12), and gasification installation (2) includes solar energy gasification heat-absorbing chamber (21) and gasification pressure controller (22), gas Changing pressure controller (22) to be arranged in solar energy gasification heat-absorbing chamber (21), gasification pressure controller (22) is for cycle fluid pressure control, described Condensing unit (5) includes condensing tube (51), heat emission fan (52) and booster body (53), and booster body (53) is arranged on condensing tube (51) middle-end, described booster body (53) includes charging turbine (531) and turbine pressure regulator (532), and turbine pressure regulator (532) is controlled System connects charging turbine (531), is additionally provided with contaminant filter pump (8) between condensing unit (5) and gasification installation (2).
Solar energy dynamical system based on supercharging condensation the most according to claim 1, is characterized in that: described supercharger Structure (53) also includes differential pressure sensor (533) and automatic controller (534), and automatic controller (534) senses by analyzing pressure reduction Turbine pressure regulator (532) is automatically controlled by the signal of device (533).
The most according to claim 1 and 2 based on supercharging condensation solar energy dynamical system, it is characterized in that: described too Sun can gasify and be additionally provided with atomizing mouth (23) between heat-absorbing chamber (21) and solar energy heat collection pipe (11).
Solar energy dynamical system based on supercharging condensation the most according to claim 3, is characterized in that: described solar energy The horizontal cross-section of gasification heat-absorbing chamber (21) is that Rhizoma Nelumbinis is poroid.
Solar energy dynamical system based on supercharging condensation the most according to claim 3, is characterized in that: described solar energy The horizontal cross-section of gasification heat-absorbing chamber (21) is all poroid in honeycomb.
Solar energy dynamical system based on supercharging condensation the most according to claim 3, is characterized in that: described solar energy Heat collecting sheet (12) is in planar sheet.
Solar energy dynamical system based on supercharging condensation the most according to claim 3, is characterized in that: described solar energy Heat collecting sheet (12) lamellar in curved surface.
Solar energy dynamical system based on supercharging condensation the most according to claim 3, is characterized in that: described solar energy Heat collecting sheet (12) is in being in staggered distribution.
Solar energy dynamical system based on supercharging condensation the most according to claim 3, is characterized in that: described solar energy Gasification heat-absorbing chamber (21) is positioned at the extraction regions of Salar light-gathering cover (4), and solar energy gasification heat-absorbing chamber (21) uses full glass to absorb heat Material or glass metal zoarium heat absorption material.
Solar energy dynamical system based on supercharging condensation the most according to claim 1, is characterized in that: described turbine Machine (3) is any one in conventional steam turbine, multiple-stage steam turbine, tesla's turbine or radial outward flow turbine.
CN201610759083.1A 2016-08-30 2016-08-30 A kind of solar energy dynamical system based on supercharging condensation Withdrawn CN106246485A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610759083.1A CN106246485A (en) 2016-08-30 2016-08-30 A kind of solar energy dynamical system based on supercharging condensation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610759083.1A CN106246485A (en) 2016-08-30 2016-08-30 A kind of solar energy dynamical system based on supercharging condensation

Publications (1)

Publication Number Publication Date
CN106246485A true CN106246485A (en) 2016-12-21

Family

ID=57597546

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610759083.1A Withdrawn CN106246485A (en) 2016-08-30 2016-08-30 A kind of solar energy dynamical system based on supercharging condensation

Country Status (1)

Country Link
CN (1) CN106246485A (en)

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
CN106246259A (en) A kind of oil field based on semi-conductor condensation heat energy from waste gas dynamical system
CN106246484A (en) A kind of solar energy dynamical system based on semi-conductor condensation
CN106224037A (en) A kind of exhaust dynamic system of heat energy based on semi-conductor condensation
CN106437891A (en) Solar heat energy power system based on eccentric turbine
CN106224032A (en) A kind of exhaust dynamic system of heat energy based on pressure-adjustable voltage stabilizing condensation
CN106246485A (en) A kind of solar energy dynamical system based on supercharging condensation
CN106224029A (en) A kind of solar energy dynamical system based on the gasification of honeycomb chamber
CN106246253A (en) A kind of oil field heat energy from waste gas dynamical system based on multi-stage booster 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
CN106438240A (en) Solar heat energy power system based on working medium circulating condensation
CN106437908A (en) Internal combustion engine tail gas utilization heat energy power system based on multistage pressurization condensation
CN106224043A (en) A kind of biofermentation dynamic system of heat energy based on supercharging condensation
CN106224025A (en) A kind of biofermentation dynamic system of heat energy based on centering type turbine
CN106224026A (en) A kind of oil field heat energy from waste gas dynamical system based on pressure-adjustable voltage stabilizing condensation
CN106224042A (en) A kind of supercharging condensation dynamic system of heat energy utilizing nuclear power station heat drain
CN106224063A (en) A kind of exhaust dynamic system of heat energy based on supercharging condensation
CN106246273A (en) A kind of biofermentation dynamic system of heat energy based on semi-conductor condensation
CN106246272A (en) A kind of multi-stage booster condensation dynamic system of heat energy utilizing nuclear power station heat drain
CN106246258A (en) A kind of exhaust dynamic system of heat energy based on working medium circulation condensation
CN106224030A (en) A kind of working medium circulation condensation dynamic system of heat energy utilizing nuclear power station heat drain
CN106437902A (en) Pressure-adjustable condensation heat energy power system using nuclear power plant hot drained water
CN106246256A (en) A kind of oil field heat energy from waste gas dynamical system based on working medium circulation 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: 20161221