CN106437902A - Pressure-adjustable condensation heat energy power system using nuclear power plant hot drained water - Google Patents

Pressure-adjustable condensation heat energy power system using nuclear power plant hot drained water Download PDF

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CN106437902A
CN106437902A CN201610760127.2A CN201610760127A CN106437902A CN 106437902 A CN106437902 A CN 106437902A CN 201610760127 A CN201610760127 A CN 201610760127A CN 106437902 A CN106437902 A CN 106437902A
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heat
pressure
heat energy
nuclear power
power station
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郭远军
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K11/00—Plants characterised by the engines being structurally combined with boilers or condensers
    • 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
    • F01K27/00—Plants for converting heat or fluid energy into mechanical energy, not otherwise provided for
    • F01K27/02—Plants modified to use their waste heat, other than that of exhaust, e.g. engine-friction heat

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

Abstract

The invention discloses a pressure-adjustable condensation heat energy power system using nuclear power plant hot drained water. The system 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 nuclear power plant hot drainage way; the condensing device is mounted in a deep water low-temperature area; a working medium adjuster is mounted between the turbine and the condensing device, and includes a turbine current limiter and a pressure stabilizing and controlling machine; the pressure stabilizing and controlling machine includes a slow pressure current storage cylinder, a slow pressure piston and an air pressure adjuster; the top end of the slow pressure current storage cylinder is communicated with the circulating pipes, and the bottom end of the slow pressure current storage cylinder is communicated with the air pressure adjuster; and the flow pressure piston is mounted in the slow pressure current storage cylinder. The pressure-adjustable condensation heat energy power system using nuclear power plant hot drained water has such advantages as high heat energy conversion efficiency, stable operation and power adjustability.

Description

A kind of pressure-adjustable condensation dynamic system of heat energy of utilization nuclear power station heat drain
Technical field
The invention belongs to the pressure-adjustable condensation heat energy of utilization of energy apparatus field, especially a kind of utilization nuclear power station heat drain Dynamical 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, heat energy transformation efficiency generally 15% to 35%, under 200 DEG C of thermal source, Heat energy transformation efficiency average out to 18%；B. working medium gasification temperature is unstable, and working medium condensation effect is not good, the working medium in condensing units Easily there is temperature to be too high to condense and the too low big phenomenon of power consumption that heats up that causes to gasify of condensation temperature；C. turbine Drive little, by gasification working medium externally acting change into mechanical energy efficiency less；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 the hot discharge capacity of f. condensing units is larger, Thermal waste is big, slow by the condensation rate of natural condensation mode, and adopts active condensing mode（The air-cooled or liquid pump water of blower fan Cold）Need extra power consumption；G. working medium is apt to deteriorate or impurity occurs；F. easily there is the problem for leaking working medium in turbine.
On the other hand, as international energy supply conditions day is becoming tight, in order to meet the rapid growth and more of electricity needs Environmental protection well, nuclear energy power generation causes the interest of various countries again.Internal authority mechanism predicts, in future 25 years, the whole world will The reactor of 90 to 300 1600 megawatts is built, welcomes the new height phase of the construction of nuclear power station.
However, the development of nuclear power has also brought larger worry, because the construction of nuclear power station and use, except right Environment is shone into outside certain radioactive pollution, can also shine into high temperature pollution to closing on waters.Nuclear power station is needed with substantial amounts of water pair Reactor is cooled down, and nuclear power station water consumption per second reaches hundreds of tons, and Mare Frigoris water or river are flow back to after Factory Building heat exchange Marine, water temperature can be raised up to twenty or thirty degree, and nuclear power heat drain can cause to have an area of in 1 kilometer of waters from after discharge outlet discharge Water temperature rises up to 5 DEG C to 8 DEG C, when the temperature of summer Mare Frigoris water or river reaches 30 DEG C, and after absorbing nuclear power station heat extraction, temperature can Elevated 40 DEG C or so, general Fish and seaweed bio cannot be survived, while also bringing larger high temperature shadow to neighbouring resident Ring.
And for the heat energy in above-mentioned nuclear power station heat drain, due to heat drain and only 20 DEG C or so of the temperature difference of normal-temperature water The temperature difference, this kind of temperature difference is difficult to be utilized by existing thermal generating equipment.
Content of the invention
Present invention purpose to be realized is：The waste thermal energy of comprehensive utilization nuclear power station heat drain, stable working medium gasification temperature, Avoid the Temperature of Working in condensing units too high or too low, improve heat energy transformation efficiency；And increase the drive of turbine, improve Turbine efficiency, stable working medium gasification temperature and refrigerant flow rate, improve working medium quality, prevent working medium from going bad, improve turbine structure, Avoid turbine from revealing and rotary speed unstabilization, condensing units are improved, accelerate condensing rate；To solve existing heat in above-mentioned background technology Existing for energy 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 easily becomes Matter or there is impurity, refrigerant leakage easily occurs in turbine, and secondary speed is unstable and stuck, condensing units easily occurs The problems such as thermal waste is big, condensing rate slow or needs extra power consumption.
For solving its technical problem the technical solution adopted in the present invention it is：A kind of pressure-adjustable of utilization nuclear power station heat drain Condensation dynamic system of heat energy, including heat collector, gasification installation, turbine, nuclear power station heat drain road, condensing units, circulation pipe Road, cycle fluid and one-way hydraulic pump, heat collector, gasification installation, turbine, condensing units and one-way hydraulic pump are passed sequentially through Circulating line realizes circulation UNICOM, and circulating line is contained within cycle fluid, and condensing units include condensing tube,
It is characterized in that：The heat collector and gasification installation are in nuclear power station heat drain road, and the condensing units are arranged on Deep-water low-temperature area, the heat collector includes thermal-collecting tube and heat collecting sheet, and heat collecting sheet parallel interval is distributed, and thermal-collecting tube fold-type is distributed in In heat collecting sheet；Gasification installation includes gasify heat-absorbing chamber and gasification pressure controller, and gasification pressure controller is installed in gasification heat absorption intracavity, gasification Pressure controller is used for cycle fluid blood pressure lowering；Heat source temperature, high pressure liquid is reached after high-pressure liquid working medium is fully heated in thermal-collecting tube State working medium flows into gasification heat-absorbing chamber, and the gasification pressure controller of gasification heat absorption intracavity is controlled by pressure so as to liquid refrigerant heat absorption gas Change, the blood pressure lowering acting in the turbine of gasification working medium；This kind of structure can be prevented effectively from gasification work compared in thermal-collecting tube direct gasification Mixing in matter has liquid refrigerant, and working medium can be made to gasify evenly；
Working medium actuator is additionally provided between the turbine and condensing units, and working medium actuator includes turbine current limiter and pressure Voltage stabilizing pressure controller, turbine current limiter includes turbine structure and secondary speed controller, and pressure voltage stabilizing pressure controller includes slow pressure storage stream The gentle pressure piston of cylinder and barostat, delay the top UNICOM circulating line of pressure storage stream cylinder, delay the bottom UNICOM gas of pressure storage stream cylinder Pressure actuator, delays pressure piston in slow pressure storage stream cylinder.
Used as optimizing further, the pressure voltage stabilizing pressure controller also includes pressure transducer, temperature sensor and single-chip microcomputer, In single-chip microcomputer, storage working medium is in different pressure PiUnder condensation temperature Ti, pressure transducer and temperature sensor are evenly distributed on cold In solidifying pipe, pressure transducer and temperature sensor data connect single-chip microcomputer, and Single-chip Controlling connection barostat and turbine turn Fast controller；When the Temperature of Working in condensing tube afterbody and working medium liquefaction temperature required differ larger when, automatic adjustable pressure tune Section device or secondary speed controller, control pressure and flow velocity, make temperature in condensing tube be close to working medium liquefaction temperature required；The structure Interior energy of the cycle fluid in condensing tube can be reduced waste, so as to improve heat energy transformation efficiency.
As explanation is optimized further, contaminant filter pump between the condensing units and heat collector, is additionally provided with.
Used as explanation is optimized further, the heat collecting sheet of the heat collector is plane or curved surface lamellar, or is interspersed；
Used as the optimization further of such scheme, the gasification heat-absorbing chamber of gasification installation is in cast, Rhizoma Nelumbinis type or honeycomb type.
As the optimization further of such scheme, gasification pressure controller between the heat collector and one-way hydraulic pump, is provided with, Gasification pressure controller is used for the preheating of working medium.
As the optimization further of such scheme, between the gasification heat-absorbing chamber and thermal-collecting tube, atomizing mouth is additionally provided with.
Used as the optimization further of such scheme, the horizontal cross-section of the gasification heat-absorbing chamber is poroid in Rhizoma Nelumbinis.
Used as the optimization further of such scheme, the horizontal cross-section of the gasification heat-absorbing chamber is all poroid in honeycomb.
Used as the optimization further of such scheme, the gasification heat-absorbing chamber is located at the upstream in nuclear power station heat drain road, thermal-arrest Device is located at the downstream in nuclear power station heat drain road.
Concrete further as such scheme optimizes, and the turbine includes turbine casing, revolving wormgear structure, air inlet Mouth, air vent and sealed bearings, revolving wormgear structure is by sealed bearings in turbine casing, and air inlet and air vent divide Cloth is in turbine casing radially opposite sides, and the revolving wormgear structure includes moving vane and grooved rotating shaft, on the axial plane of grooved rotating shaft Distribution is fluted, and moving vane is movably arranged on by spring in the groove of grooved rotating shaft, and grooved rotating shaft is inclined by sealed bearings Feel at ease and be mounted in turbine casing, air inlet is nearer away from eccentric shaft, air vent constitutes chamber away from eccentric shaft farther out, between adjacent activities blade Room, communicate with air inlet for expansion chamber, communicate with air vent for discharge chamber；Due to expansion chamber both sides blade area not With expansion chamber is intended to volume and becomes general orientation rotation, and the turbine of this kind of structure has larger thrust, more fully hereinafter can utilize The kinetic energy of gasification working medium and potential energy, with preferable heat energy transformation efficiency.
Used as explanation is optimized further, the moving vane of the revolving wormgear structure includes at least three.
Optimize as concrete further, the exhaust ports of the turbine are provided with precondenser；Take the structure increase Big air inlet and the pressure reduction of air vent, improve the transformation efficiency of turbine.
Optimize as concrete further, the precondenser includes working medium conduction pipe and condensation endothermic tube, working medium conduction pipe For connecting air vent and circulating line, condensing endothermic tube is used for absorbing the heat that working medium turns on intraductal working medium, working medium conduction pipe With condensation endothermic tube spiral paratactic contact, it is heat recipient fluid in condensation endothermic tube, is to increase condensation efficiency, the flowing of heat recipient fluid Direction is contrary with the flow direction of working medium conducting intraductal working medium.
Optimize as concrete further, the condensation endothermic tube is using following between UNICOM's one-way hydraulic pump and heat collector Endless tube road；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, the structure largely recycles working medium heat in circulating line, increases thermal transition efficiency.
Used as explanation is optimized further, the condensing units include condensing tube and heat emission fan, and condensing tube uniformly divide by a point multilamellar Cloth, the mutual UNICOM of condensing tube, heat emission fan is above or below condensing tube, and heat emission fan is driven with convulsion mode or pressure wind mode Dynamic.
Concrete further as such scheme optimizes, and the condensing tube becomes oblique type to be distributed.
Concrete further as such scheme optimizes, and the condensing tube becomes horizontal or vertical distribution.
Concrete further as such scheme optimizes, and when the condensing tube becomes horizontal distribution, upper and lower layer condensing tube is mutual Stagger.
Concrete further as such scheme optimizes, and the condensing tube is copper metal tube or stability alloying metal Pipe.
Concrete further as such scheme optimizes, and in order to accelerate the liquefaction of working medium, reduces the thermal discharge of condensation process, The condensing units also have additional booster pump, and booster pump is arranged on condensing tube middle-end.
Concrete further as such scheme optimizes, in order to reduce the compression energy consumption of working medium in condensing units, described cold In solidifying device, compress mode takes staged to compress, and is provided with multiple booster pumps in condensing units, and booster pump is evenly distributed on cold In solidifying pipe；The structure is taken, compared to single booster pump is adopted, fractional condensaion can be preferably realized, largely improve pressure Poor by force, and reduce energy consumption needed for supercharging.
Concrete further as such scheme optimizes, in order to avoid the working medium entrance of uncooled liquefaction in condensing tube is unidirectional Hydraulic pump, condensing tube tail end is provided with catch box.
Concrete further as such scheme optimizes, and in order to accelerate radiating, condensing units are additionally provided with fin.
Concrete further as such scheme optimizes, and the booster pump adopts turbocharging, and multiple booster pumps are by dynamic Force transmission mechanism is driven by same motor.
Concrete further as such scheme optimizes, and the cycle fluid adopts propanol.
Concrete further as such scheme optimizes, and the cycle fluid adopts methanol.
Concrete further as such scheme optimizes, and the cycle fluid adopts ethanol.
Concrete further as such scheme optimizes, and the cycle fluid adopts isopropanol.
Concrete further as such scheme optimizes, and the cycle fluid adopts liquefied ammonia.
Concrete further as such scheme optimizes, and the cycle fluid is using conventional freon.
Operation principle：The pressure-adjustable condensation dynamic system of heat energy of the invention utilization nuclear power station heat drain, during work, follows Ring working medium is absorbed heat the heat source temperature that reaches a high temperature in heat collector, then flows in gasification installation, makes its gas by the blood pressure lowering of a small amount of Changing heat absorption, turbine is flowed after working medium gasification, drive rotating turbine；After gasification working medium flows through turbine, due to externally doing work, Its Temperature of Working and air pressure can all reduce, and cause part working medium liquefaction；After gasification working medium flows through turbine, working medium flows successively Working medium actuator and condensing units；Working medium actuator is used for controlling 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, working medium condensing temperature or gasification temperature is adjusted, 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, contaminant filter pump can by contaminant filter in working medium out, and one-way hydraulic pump carries out unidirectional pumping supercharging to working medium；Work after liquefaction After matter sequentially passes through contaminant filter pump and one-way hydraulic pump, and gasification installation is again introduced into, completes a circulation.
Beneficial effect：The pressure-adjustable condensation dynamic system of heat energy of utilization nuclear power station heat drain of the present invention, with respect to existing The heat energy machine having in technology, have the advantages that following several respects and progress：1. the pressure by setting up working medium actuator, to working medium It is controlled with flow, gasification efficiency and condensation efficiency, and stable working medium gasification temperature and refrigerant flow rate can be effectively improved, is prevented Sealing member deformation is larger, it is to avoid the unstable and working medium leakage problem of secondary speed；2. by setting up precondenser, it is possible to increase turbine The pressure reduction of middle air inlet and air vent, 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, and reduces thermal waste and cooling power consumption；3. by setting up contaminant filter pump and one-way hydraulic pump, Can effectively prevent working medium rotten and more impurity occur, and prevent working medium from flowing back；4. by setting up supercharging in condensing units Pump, can largely improve condensing rate, reduce condensation power consumption；5., by adopting turbine, whirlpool largely can be increased Turbine turn power, and improve turbine efficiency；6. nuclear power station thermal wastewater is fully utilized, has certain cooling to thermal wastewater, protection Environment.
Description of the drawings
Fig. 1 is the Integral connection structure schematic diagram of the present invention program one；
Fig. 2 is the nuclear power station heat drain road structural representation of the present invention program one；
Fig. 3 is the working medium controller structure schematic diagram of the present invention program one；
Fig. 4 is the automatic control circuit principle schematic of the working medium actuator of the present invention program one；
Fig. 5 is the heat collector structural representation of the present invention program one；
Fig. 6 is the gasification heat-absorbing chamber structural representation of the present invention program one；
Fig. 7 is the condensing units vertical cross section structural representation of the present invention program one；
Fig. 8 is the condensing units horizontal cross-sectional structural representation of the present invention program one；
Fig. 9 is the heat collector structural representation of the present invention program two；
Figure 10 is the heat collector structural representation of the present invention program three；
Figure 11 is the gasification pressure controller attachment structure schematic diagram of the present invention program four；
Figure 12 is the atomizing mouth attachment structure schematic diagram of the present invention program five；
Figure 13 is the gasification heat-absorbing chamber cross section structure schematic diagram of the present invention program six；
Figure 14 is the gasification heat-absorbing chamber cross section structure schematic diagram of the present invention program seven；
Figure 15 is the precondenser structural representation of the present invention program eight；
Figure 16 is the precondenser attachment structure schematic diagram of the present invention program nine；
Figure 17 is the condensing units vertical cross section structural representation of the present invention program ten；
Figure 18 is the condensing units vertical cross section structural representation of the present invention program 11；
Figure 19 is the condensing units vertical cross section structural representation of the present invention program 12；
Figure 20 is the turbine structure schematic diagram of the present invention program 13；
Figure 21 is the turbine grooved pivot structure schematic diagram of the present invention program 13；
Figure 22 is the condensing units structural representation of the present invention program 14；
Figure 23 is the condensing units structural representation of the present invention program 15；
In figure：
1 is heat collector, 11 is thermal-collecting tube, 12 is heat collecting sheet；
2 is gasification installation, 21 is gasification heat-absorbing chamber, 22 is gasification pressure controller, 221 is differential pressure control valve, 222 is gasification pressure sense It is atomizing mouth to answer device, 23；
3 is turbine, 31 is turbine casing, 32 is revolving wormgear structure, 321 is moving vane, 322 is grooved rotating shaft, 323 are Groove, 324 be spring, 33 air inlets, 34 be air vent, 35 be sealed bearings, 36 be precondenser, 361 be working medium conduction pipe, 362 is condensation endothermic tube, 331 is expansion chamber, 341 is discharge chamber；
4 is nuclear power station heat drain road；
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 pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch 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be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan, 53 be booster pump, 54 catch boxssssssssssssssssssssssssssssssssssssssssssssssssssssssssssssss heat emission fan；
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 be slow pressure piston, 107 be barostat, 108 be pressure transducer, 109 is temperature sensor, 1010 is single-chip microcomputer.
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 pressure-adjustable condensation dynamic system of heat energy of utilization nuclear power station heat drain, including Heat collector 1, gasification installation 2, turbine 3, nuclear power station heat drain road 4, condensing units 5, circulating line 6, cycle fluid 7 and list To 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 Circulation UNICOM is realized, circulating line 6 is contained within cycle fluid 7；
（As shown in Figure 2）The heat collector 1 and gasification installation 2 are arranged in nuclear power station heat drain road 4, the condensing units 5 Installed in deep-water low-temperature area, the heat collector 1 includes thermal-collecting tube 11 and heat collecting sheet 12, and 12 parallel interval of heat collecting sheet is distributed, collection 11 fold-type of heat pipe is distributed in heat collecting sheet 12；Gasification installation 2 includes gasify heat-absorbing chamber 21 and gasification pressure controller 22, and gasify pressure controller 22 in gasification heat-absorbing chamber 21, and gasification pressure controller 22 is used for liquid refrigerant blood pressure lowering；When high-pressure liquid working medium is in thermal-collecting tube 11 Heat source temperature is reached after interior abundant heating, high-pressure liquid working medium flows into gasification heat-absorbing chamber 21, the gasification control that gasifies in heat-absorbing chamber 21 Depressor 22 is controlled by pressure so as to liquid refrigerant endothermic gasification, the blood pressure lowering acting in the turbine 3 of gasification working medium；This kind of structure There is liquid refrigerant compared in 11 direct gasification of thermal-collecting tube, being prevented effectively to mix in gasification working medium, working medium gasification can be made more equal Even；
（As shown in Figure 3, Figure 4）, working medium actuator 10 is additionally provided between the turbine 3 and condensing units 5, the working medium is adjusted Section device 10 includes turbine current limiter 101 and pressure voltage stabilizing pressure controller 102, and turbine current limiter 101 includes turbine structure 103 and turbine Rotational speed governor 104, pressure voltage stabilizing pressure controller 102 includes the gentle pressure piston 106 of slow pressure storage stream cylinder 105 and barostat 107, The top UNICOM circulating line 6 of slow pressure storage stream cylinder 105, delays the bottom UNICOM barostat 107 of pressure storage stream cylinder 105, delays pressure and live Plug 106 is in slow pressure storage stream cylinder 105；The pressure voltage stabilizing pressure controller 102 also includes pressure transducer 108, temperature sensing Device 109 and single-chip microcomputer 1010, in single-chip microcomputer 1010, storage working medium is in different pressure PiUnder condensation temperature Ti, pressure transducer 108 It is evenly distributed in condensing units 5 with temperature sensor 109, pressure transducer 108 and 109 data cube computation monolithic of temperature sensor Machine 1010, the control of single-chip microcomputer 1010 connection barostat 107 and secondary speed controller 104.
Optimization further as the above-mentioned embodiment of this enforcement is illustrated, the turbine 3 is common blade formula turbine.
Optimization further as the above-mentioned embodiment of this enforcement is illustrated, between the condensing units 5 and heat collector 1 also It is provided with contaminant filter pump 8.
Optimization further as the above-mentioned embodiment of this enforcement is illustrated,（As shown in Figure 5）Heat collecting sheet 12 is in planar sheet；
Optimization further as the above-mentioned embodiment of this enforcement is illustrated,（As shown in Figure 6）The gasification heat-absorbing chamber 21 is by multiple Body is formed side by side.
Optimization further as the above-mentioned embodiment of this enforcement is illustrated,（As shown in Figure 7, Figure 8）The condensing units 5 are wrapped Condensing tube 51 and heat emission fan 52 is included, condensing tube 51 uniformly divides Multi-layers distributing, the mutual UNICOM of condensing tube 51, heat emission fan 52 is installed in cold Above or below solidifying pipe 51, heat emission fan 52 is driven with convulsion mode or pressure wind mode；The condensing tube 51 be copper metal tube or Alloying metal pipe, condensing tube 51 is in horizontal distribution.
Optimization further as the above-mentioned embodiment of this enforcement illustrates, 51 tail end of condensing tube is provided with catch box 54.
Optimization further as the above-mentioned embodiment of this enforcement illustrates, condensing units 5 are additionally provided with fin 55.
Optimization further as the above-mentioned embodiment of this enforcement illustrates, the cycle fluid 7 adopts liquefied ammonia.
The pressure-adjustable condensation dynamic system of heat energy of the utilization nuclear power station heat drain described in the present embodiment, its working medium actuator 10 In single-chip microcomputer 1010 by the temperature sensor T of real-time C.T induction apparatuss 109WhenWith the sensing pressure according to pressure induction apparatuss PWhenThe temperature required T of the liquefaction that calculatedi, real-time control is realized, so that the working medium in condensing units is liquefied with perfect condition.
Temperature of Working T in 51 afterbody of condensing tubeWhenT temperature required more than working medium liquefactioniWhen, working medium cannot be condensed, single Piece machine 1010 controls barostat 107 and secondary speed controller 104 to increase sender matter pressure respectively and reduce refrigerant flow rate, when When pressure becomes big, working medium condensing temperature is uprised, meanwhile, when refrigerant flow rate is reduced, working medium cooling increases, so as to progressively make condensation In pipe 51, Temperature of Working is close to condensation temperature, reality condensation；
When the Temperature of Working in 51 afterbody of condensing tube is temperature required less than working medium liquefaction, single-chip microcomputer 1010 controls barostat 107 and secondary speed controller 104 reduce respectively sender matter pressure and accelerate refrigerant flow rate, when pressure become hour, working medium liquefaction temperature Degree step-down, meanwhile, when big refrigerant flow rate is subtracted, working medium cooling reduces, cold so as to progressively be close to Temperature of Working in condensing tube 51 Solidifying temperature, it is to avoid continuing cooling after working fluid condensate causes thermal waste, so as to improve heat energy transformation efficiency.
By dynamic system of heat energy being condensed to the pressure-adjustable using nuclear power station heat drain in above-described embodiment one carry out reality Testing, the hot water of different temperatures being entered to heat collector 1 and gasification installation 2, it is 3000L/s that sink temperature is 10 DEG C, drainage rates, In circulation pipe, refrigerant flow rate is carried out according to the operation stability of the pressure-adjustable condensation dynamic system of heat energy using nuclear power station heat drain Adjustment；Experiment effect is：When hot water temperature is 40 DEG C or so, heat energy transformation efficiency is about 5.5%, and hot water temperature is 45 DEG C or so When, heat energy transformation efficiency is about 8.4%, and when hot water temperature is 50 DEG C or so, heat energy transformation efficiency is about 10%, and hot water temperature is 55 DEG C or so when, heat energy transformation efficiency is about 11.6%, hot water temperature be 60 DEG C or so when, heat energy transformation efficiency is about 14%, passes through Data are analyzed, the pressure-adjustable of the utilization nuclear power station heat drain of the present embodiment condenses dynamic system of heat energy and conventional heat energy machine Heat energy transformation efficiency（Conventional heat energy machine, under 40-60 DEG C of low-temperature heat source, heat energy efficiency is very low, and efficiency is less than 3%, heat More difficult can be utilized）Compare, the pressure-adjustable of the utilization nuclear power station heat drain of the present embodiment condenses converting for dynamic system of heat energy Efficiency is higher than the heat energy transformation efficiency of conventional heat energy machine by 7% or so；Meanwhile, the present embodiment is using the pressure-adjustable of nuclear power station heat drain The operation noise of condensation dynamic system of heat energy is little, good operation stability, while can achieve power output regulation.
Embodiment two（As shown in Figure 9）：It is with one difference of embodiment：The heat collecting sheet 12 of the heat collector 1 is in Curved surface lamellar.
By dynamic system of heat energy being condensed to the pressure-adjustable using nuclear power station heat drain in above-described embodiment two carry out reality Testing, the hot water of different temperatures being entered to heat collector 1 and gasification installation 2, it is 3000L/s that sink temperature is 10 DEG C, drainage rates, In circulation pipe, refrigerant flow rate is carried out according to the operation stability of the pressure-adjustable condensation dynamic system of heat energy using nuclear power station heat drain Adjustment；Experiment effect is：When hot water temperature is 40 DEG C or so, heat energy transformation efficiency is about 6.2%, and hot water temperature is 45 DEG C or so When, heat energy transformation efficiency is about 11.8%, and when hot water temperature is 50 DEG C or so, heat energy transformation efficiency is about 10.8%, hot water temperature During for 55 DEG C or so, heat energy transformation efficiency is about 30.2%, and when hot water temperature is 60 DEG C or so, heat energy transformation efficiency is about 14.6%；By being analyzed to data, the pressure-adjustable condensation dynamic system of heat energy of the utilization nuclear power station heat drain of the present embodiment two Heat energy transformation efficiency with conventional heat energy machine（Conventional heat energy machine, under 40-60 DEG C of low-temperature heat source, heat energy efficiency is very low, effect Rate is less than 3%, and heat energy is more difficult to be utilized）Compare, the pressure-adjustable condensation thermal power system of the utilization nuclear power station heat drain of the present embodiment The energy transformation efficiency of system is higher than the heat energy transformation efficiency of conventional heat energy machine by 7.9% or so.
Embodiment three（As shown in Figure 10）：It is with one difference of embodiment：The heat collecting sheet 12 of the heat collector 1 is in It is in staggered distribution.
By dynamic system of heat energy being condensed to the pressure-adjustable using nuclear power station heat drain in above-described embodiment three carry out reality Testing, the hot water of different temperatures being entered to heat collector 1 and gasification installation 2, it is 3000L/s that sink temperature is 10 DEG C, drainage rates, In circulation pipe, refrigerant flow rate is carried out according to the operation stability of the pressure-adjustable condensation dynamic system of heat energy using nuclear power station heat drain Adjustment；Experiment effect is：When hot water temperature is 40 DEG C or so, heat energy transformation efficiency is about 5.7%, and hot water temperature is 45 DEG C or so When, heat energy transformation efficiency is about 8.8%, and when hot water temperature is 50 DEG C or so, heat energy transformation efficiency is about 10.8%, and hot water temperature is When 55 DEG C or so, heat energy transformation efficiency is about 12.4%, and when hot water temperature is 60 DEG C or so, heat energy transformation efficiency is about 16.2%； By being analyzed to data, the pressure-adjustable of the utilization nuclear power station heat drain of the present embodiment three condenses dynamic system of heat energy and routine The heat energy transformation efficiency of heat energy machine（Conventional heat energy machine, under 40-60 DEG C of low-temperature heat source, heat energy efficiency is very low, and efficiency is less than 3%, heat energy is more difficult to be utilized）Compare, the energy of the pressure-adjustable condensation dynamic system of heat energy of the utilization nuclear power station heat drain of the present embodiment Transformation efficiency is higher than the heat energy transformation efficiency of conventional heat energy machine by 6.4% or so.
Example IV（As shown in figure 11）：It is with one difference of embodiment：The gasification pressure controller 22 includes pressure reduction Control valve 221 and gasification pressure induction apparatuss 222, differential pressure control valve 221 is located at the front end of gasification heat-absorbing chamber 21, gasification pressure sensing Device 222 is located at gasification 21 rear end of heat-absorbing chamber；Differential pressure control valve 221 is used for adjusting pressure reduction, and gasification pressure induction apparatuss 222 are used for sensing In gasification heat-absorbing chamber 21, the pressure of working medium, when pressure is larger, increases the pressure reduction of differential pressure control valve 221, when pressure is compared with hour, subtracts The pressure reduction of small pressure difference control valve 221, so as to realize the pressure control to the heat-absorbing chamber 21 that gasifies.
By dynamic system of heat energy being condensed to the pressure-adjustable using nuclear power station heat drain in above-described embodiment four carry out reality Testing, the hot water of different temperatures being entered to heat collector 1 and gasification installation 2, it is 3000L/s that sink temperature is 10 DEG C, drainage rates, In circulation pipe, refrigerant flow rate is carried out according to the operation stability of the pressure-adjustable condensation dynamic system of heat energy using nuclear power station heat drain Adjustment；Experiment effect is：When hot water temperature is 40 DEG C or so, heat energy transformation efficiency is about 6%, when hot water temperature is 45 DEG C or so, Heat energy transformation efficiency is about 8.7%, and when hot water temperature is 50 DEG C or so, heat energy transformation efficiency is about 10.6%, and hot water temperature is 55 DEG C or so when, heat energy transformation efficiency is about 12.8%, hot water temperature be 60 DEG C or so when, heat energy transformation efficiency is about 16.2%, lead to Cross and data are analyzed, the pressure-adjustable of the utilization nuclear power station heat drain of the present embodiment four condenses dynamic system of heat energy and conventional heat The heat energy transformation efficiency of energy machine（Conventional heat energy machine, under 40-60 DEG C of low-temperature heat source, heat energy efficiency is very low, and efficiency is less than 3%, heat energy is more difficult to be utilized）Compare, the energy of the pressure-adjustable condensation dynamic system of heat energy of the utilization nuclear power station heat drain of the present embodiment Transformation efficiency is higher than the heat energy transformation efficiency of conventional heat energy machine by 6.8% or so.
Embodiment five（As shown in figure 12）：It is with example IV difference：The gasification heat-absorbing chamber 21 and thermal-collecting tube Atomizing mouth 23 is additionally provided between 11.
Dynamic system of heat energy is condensed by the pressure-adjustable using nuclear power station heat drain of above-described embodiment five to be tested, to Heat collector 1 and gasification installation 2 enter the hot water of different temperatures, and it is 3000L/s that sink temperature is 10 DEG C, drainage rates, circulation Intraductal working medium flow velocity is adjusted according to the operation stability of the pressure-adjustable condensation dynamic system of heat energy using nuclear power station heat drain； Experiment effect is：When hot water temperature is 40 DEG C or so, heat energy transformation efficiency is about 7%, when hot water temperature is 45 DEG C or so, heat energy Transformation efficiency is about 9.2%, and when hot water temperature is 50 DEG C or so, heat energy transformation efficiency is about 11.2%, and hot water temperature is 55 DEG C of left sides When right, heat energy transformation efficiency is about 13.6%, and when hot water temperature is 60 DEG C or so, heat energy transformation efficiency is about 16.6%, by right Data are analyzed, and the pressure-adjustable of the utilization nuclear power station heat drain of the present embodiment five condenses dynamic system of heat energy and conventional heat energy machine Heat energy transformation efficiency（Conventional heat energy machine, under 40-60 DEG C of low-temperature heat source, heat energy efficiency is very low, and efficiency is less than 3%, heat More difficult can be utilized）Compare, the pressure-adjustable of the utilization nuclear power station heat drain of the present embodiment condenses converting for dynamic system of heat energy Efficiency is higher than the heat energy transformation efficiency of conventional heat energy machine by 7% or so.
Embodiment six（As shown in figure 13）：It is with five difference of embodiment：The level of the gasification heat-absorbing chamber 21 is cut Face is poroid in Rhizoma Nelumbinis.
By dynamic system of heat energy being condensed to the pressure-adjustable using nuclear power station heat drain in above-described embodiment six carry out reality Testing, the hot water of different temperatures being entered to heat collector 1 and gasification installation 2, it is 3000L/s that sink temperature is 10 DEG C, drainage rates, In circulation pipe, refrigerant flow rate is carried out according to the operation stability of the pressure-adjustable condensation dynamic system of heat energy using nuclear power station heat drain Adjustment；Experiment effect is：When hot water temperature is 40 DEG C or so, heat energy transformation efficiency is about 8%, when hot water temperature is 45 DEG C or so, Heat energy transformation efficiency is about 10%, and when hot water temperature is 50 DEG C or so, heat energy transformation efficiency is about 12%, and hot water temperature is 55 DEG C of left sides When right, heat energy transformation efficiency is about 14.8%, and when hot water temperature is 60 DEG C or so, heat energy transformation efficiency is about 17.4%, by right Data are analyzed, and the pressure-adjustable of the utilization nuclear power station heat drain of the present embodiment six condenses dynamic system of heat energy and conventional heat energy machine Heat energy transformation efficiency（Conventional heat energy machine, under 40-60 DEG C of low-temperature heat source, heat energy efficiency is very low, and efficiency is less than 3%, heat More difficult can be utilized）Compare, the pressure-adjustable of the utilization nuclear power station heat drain of the present embodiment condenses converting for dynamic system of heat energy Efficiency is higher than the heat energy transformation efficiency of conventional heat energy machine by 9% or so.
Embodiment seven（As shown in figure 14）：It is with five difference of embodiment：The level of the gasification heat-absorbing chamber 21 is cut Face is all poroid in honeycomb.
By dynamic system of heat energy being condensed to the pressure-adjustable using nuclear power station heat drain in above-described embodiment seven carry out reality Testing, the hot water of different temperatures being entered to heat collector 1 and gasification installation 2, it is 3000L/s that sink temperature is 10 DEG C, drainage rates, In circulation pipe, refrigerant flow rate is carried out according to the operation stability of the pressure-adjustable condensation dynamic system of heat energy using nuclear power station heat drain Adjustment；Experiment effect is：When hot water temperature is 40 DEG C or so, heat energy transformation efficiency is about 8%, when hot water temperature is 45 DEG C or so, Heat energy transformation efficiency is about 10%, and when hot water temperature is 50 DEG C or so, heat energy transformation efficiency is about 12.4%, and hot water temperature is 55 DEG C During left and right, heat energy transformation efficiency is about 15.5%, and when hot water temperature is 60 DEG C or so, heat energy transformation efficiency is about 17.8%；Pass through Data are analyzed, the pressure-adjustable of the utilization nuclear power station heat drain of the present embodiment seven condenses dynamic system of heat energy and conventional heat energy The heat energy transformation efficiency of machine（Conventional heat energy machine, under 40-60 DEG C of low-temperature heat source, heat energy efficiency is very low, and efficiency is less than 3%, Heat energy is more difficult to be utilized）Compare, the energy of the pressure-adjustable condensation dynamic system of heat energy of the utilization nuclear power station heat drain of the present embodiment turns Change efficiency higher than the heat energy transformation efficiency of conventional heat energy machine by 9.6% or so.
Embodiment eight（As shown in figure 15）：It is with seven difference of embodiment：In order to increase turbine air inlet 33 with The pressure reduction of air vent 34, is additionally provided with precondenser 36 at the air vent 34 of the turbine 3.
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 34 and circulating line 6, and condensation endothermic tube 362 is used for absorbing working medium The heat of working medium in conduction pipe 361, working medium conduction pipe 361 and condensation 362 spiral paratactic contact of endothermic tube, condense endothermic tube 362 Interior for heat recipient fluid.
Being further elaborated with as above-described embodiment, is to increase condensation efficiency, the flow direction of heat recipient fluid and work In matter conduction pipe 361, the flow direction of working medium is contrary.
By dynamic system of heat energy being condensed to the pressure-adjustable using nuclear power station heat drain in above-described embodiment eight carry out reality Testing, the hot water of different temperatures being entered to heat collector 1 and gasification installation 2, it is 3000L/s that sink temperature is 10 DEG C, drainage rates, In circulation pipe, refrigerant flow rate is carried out according to the operation stability of the pressure-adjustable condensation dynamic system of heat energy using nuclear power station heat drain Adjustment；Experiment effect is：When hot water temperature is 40 DEG C or so, heat energy transformation efficiency is about 8.4%, and hot water temperature is 45 DEG C or so When, heat energy transformation efficiency is about 10.4%, and when hot water temperature is 50 DEG C or so, heat energy transformation efficiency is about 12.8%, hot water temperature During for 55 DEG C or so, heat energy transformation efficiency is about 16.2%, and when hot water temperature is 60 DEG C or so, heat energy transformation efficiency is about 18%, By being analyzed to data, the pressure-adjustable of the utilization nuclear power station heat drain of the present embodiment eight condenses dynamic system of heat energy and routine The heat energy transformation efficiency of heat energy machine（Conventional heat energy machine, under 40-60 DEG C of low-temperature heat source, heat energy efficiency is very low, and efficiency is less than 3%, heat energy is more difficult to be utilized）Compare, the pressure-adjustable condensation dynamic system of heat energy of the utilization nuclear power station heat drain of the present embodiment eight Energy transformation efficiency is higher than the heat energy transformation efficiency of conventional heat energy machine by 9.4% or so.
Embodiment nine（As Figure 16）：It is with eight difference of embodiment：The condensation endothermic tube 362 is unidirectional using UNICOM Circulating line 6 between hydraulic pump 9 and heat collector 1；As the circulating line 6 between one-way hydraulic pump 9 and heat collector is needed Absorb heat, and in working medium conduction pipe 361, working medium needs heat extraction, the structure largely recycles working medium in circulating line 6 Heat, increases thermal transition efficiency.
By dynamic system of heat energy being condensed to the pressure-adjustable using nuclear power station heat drain in above-described embodiment nine carry out reality Testing, the hot water of different temperatures being entered to heat collector 1 and gasification installation 2, it is 3000L/s that sink temperature is 10 DEG C, drainage rates, In circulation pipe, refrigerant flow rate is carried out according to the operation stability of the pressure-adjustable condensation dynamic system of heat energy using nuclear power station heat drain Adjustment；Experiment effect is：When hot water temperature is 40 DEG C or so, heat energy transformation efficiency is about 9%, when hot water temperature is 45 DEG C or so, Heat energy transformation efficiency is about 10.8%, and when hot water temperature is 50 DEG C or so, heat energy transformation efficiency is about 13.4%, and hot water temperature is 55 DEG C or so when, heat energy transformation efficiency is about 17%, hot water temperature be 60 DEG C or so when, heat energy transformation efficiency is about 18%, by right Data are analyzed, and the pressure-adjustable of the utilization nuclear power station heat drain of the present embodiment nine condenses dynamic system of heat energy and conventional heat energy machine Heat energy transformation efficiency（Conventional heat energy machine, under 40-60 DEG C of low-temperature heat source, heat energy efficiency is very low, and efficiency is less than 3%, heat More difficult can be utilized）Compare, the energy of the pressure-adjustable condensation dynamic system of heat energy of the utilization nuclear power station heat drain of the present embodiment nine turns Change efficiency higher than the heat energy transformation efficiency of conventional heat energy machine by 11% or so.
Embodiment ten（As shown in figure 17）：It is with nine difference of embodiment：The oblique type distribution of 51 one-tenth of the condensing tube.
By dynamic system of heat energy being condensed to the pressure-adjustable using nuclear power station heat drain in above-described embodiment ten carry out reality Testing, the hot water of different temperatures being entered to heat collector 1 and gasification installation 2, it is 3000L/s that sink temperature is 10 DEG C, drainage rates, In circulation pipe, refrigerant flow rate is carried out according to the operation stability of the pressure-adjustable condensation dynamic system of heat energy using nuclear power station heat drain Adjustment；Experiment effect is：When hot water temperature is 40 DEG C or so, heat energy transformation efficiency is about 9%, when hot water temperature is 45 DEG C or so, Heat energy transformation efficiency is about 10.8%, and when hot water temperature is 50 DEG C or so, heat energy transformation efficiency is about 13.4%, and hot water temperature is 55 DEG C or so when, heat energy transformation efficiency is about 17.2%%, hot water temperature be 60 DEG C or so when, heat energy transformation efficiency is about 18.1%, lead to Cross and data are analyzed, the pressure-adjustable of the utilization nuclear power station heat drain of the present embodiment ten condenses dynamic system of heat energy and conventional heat The heat energy transformation efficiency of energy machine（Conventional heat energy machine, under 40-60 DEG C of low-temperature heat source, heat energy efficiency is very low, and efficiency is less than 3%, heat energy is more difficult to be utilized）Compare, the energy of the pressure-adjustable condensation dynamic system of heat energy of the utilization nuclear power station heat drain of the present embodiment Transformation efficiency is higher than the heat energy transformation efficiency of conventional heat energy machine by 11.2% or so.
Embodiment 11（As shown in figure 18）：It is with nine difference of embodiment：51 one-tenth vertical distribution of the condensing tube.
Carried out by condensing dynamic system of heat energy to the pressure-adjustable using nuclear power station heat drain in above-described embodiment 11 Experiment, enters the hot water of different temperatures to heat collector 1 and gasification installation 2, and it is 3000L/ that sink temperature is 10 DEG C, drainage rates S, in circulation pipe, refrigerant flow rate enters according to the operation stability of the pressure-adjustable condensation dynamic system of heat energy using nuclear power station heat drain Row adjustment；Experiment effect is：When hot water temperature is 40 DEG C or so, heat energy transformation efficiency is about 8.7%, and hot water temperature is 45 DEG C of left sides When right, heat energy transformation efficiency is about 10.4%, and when hot water temperature is 50 DEG C or so, heat energy transformation efficiency is about 13.2%, hot water temperature When spending for 55 DEG C or so, heat energy transformation efficiency is about 17%, and when hot water temperature is 60 DEG C or so, heat energy transformation efficiency is about 18%, By being analyzed to data, the pressure-adjustable of the utilization nuclear power station heat drain of the present embodiment 11 condensation dynamic system of heat energy with normal The heat energy transformation efficiency of rule heat energy machine（Conventional heat energy machine, under 40-60 DEG C of low-temperature heat source, heat energy efficiency is very low, and efficiency is low In 3%, heat energy is more difficult to be utilized）Compare, the pressure-adjustable condensation dynamic system of heat energy of the utilization nuclear power station heat drain of the present embodiment eight Can transformation efficiency higher than the heat energy transformation efficiency of conventional heat energy machine by 10.6% or so.
Embodiment 12（As shown in figure 19）：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.
Carried out by condensing dynamic system of heat energy to the pressure-adjustable using nuclear power station heat drain in above-described embodiment 12 Experiment, enters the hot water of different temperatures to heat collector 1 and gasification installation 2, and it is 3000L/ that sink temperature is 10 DEG C, drainage rates S, in circulation pipe, refrigerant flow rate enters according to the operation stability of the pressure-adjustable condensation dynamic system of heat energy using nuclear power station heat drain Row adjustment；Experiment effect is：When hot water temperature is 40 DEG C or so, heat energy transformation efficiency is about 9%, and hot water temperature is 45 DEG C or so When, heat energy transformation efficiency is about 10.8%, and when hot water temperature is 50 DEG C or so, heat energy transformation efficiency is about 13.4%, hot water temperature During for 55 DEG C or so, heat energy transformation efficiency is about 17.2%%, and when hot water temperature is 60 DEG C or so, heat energy transformation efficiency is about 18.1%, by being analyzed to data, the pressure-adjustable condensation thermal power system of the utilization nuclear power station heat drain of the present embodiment 12 System and the heat energy transformation efficiency of conventional heat energy machine（Conventional heat energy machine, under 40-60 DEG C of low-temperature heat source, heat energy efficiency is very low, Efficiency is less than 3%, and heat energy is more difficult to be utilized）Compare, the pressure-adjustable condensation thermal power of the utilization nuclear power station heat drain of the present embodiment The energy transformation efficiency of system is higher than the heat energy transformation efficiency of conventional heat energy machine by 11.2% or so.
Embodiment 13（As shown in figs 20 and 21）：It is with 12 difference of embodiment：The turbine 3 includes whirlpool Wheel casing 31, revolving wormgear structure 32, air inlet 33, air vent 34 and sealed bearings 35, revolving wormgear structure 32 is by sealing Bearing 35 is in turbine casing 31, and air inlet 33 and air vent 34 are distributed in 31 radially opposite sides of turbine casing, the rotation Turbine structure 32 includes moving vane 321 and grooved rotating shaft 322, is distributed fluted 323, activity on the axial plane of grooved rotating shaft 322 Blade 321 is movably arranged in the groove 323 of grooved rotating shaft 322 by spring 324, and grooved rotating shaft 322 passes through sealed bearings 35 Be eccentrically mounted in turbine casing 31, air inlet 33 is nearer away from eccentric shaft, air vent 34 away from eccentric shaft farther out, adjacent activities blade Constitute chamber between 321, communicate with air inlet 33 for expansion chamber 331, communicate with air vent 34 for discharge chamber 341；Due to swollen The both sides blade areas difference in swollen chamber, expansion chamber is intended to volume and becomes general orientation rotation, and the turbine of this kind of structure has larger Thrust, can be more fully hereinafter using the gasification kinetic energy of working medium and potential energy, with preferable heat energy transformation efficiency.
Carried out by condensing dynamic system of heat energy to the pressure-adjustable using nuclear power station heat drain in above-described embodiment 13 Experiment, enters the hot water of different temperatures to heat collector 1 and gasification installation 2, and it is 3000L/ that sink temperature is 10 DEG C, drainage rates S, in circulation pipe, refrigerant flow rate enters according to the operation stability of the pressure-adjustable condensation dynamic system of heat energy using nuclear power station heat drain Row adjustment；Experiment effect is：When hot water temperature is 40 DEG C or so, heat energy transformation efficiency is about 9.2%, and hot water temperature is 45 DEG C of left sides When right, heat energy transformation efficiency is about 11%, and when hot water temperature is 50 DEG C or so, heat energy transformation efficiency is about 13.6%, hot water temperature During for 55 DEG C or so, heat energy transformation efficiency is about 17.4%, and when hot water temperature is 60 DEG C or so, heat energy transformation efficiency is about 18.4%, by being analyzed to data, the pressure-adjustable condensation thermal power system of the utilization nuclear power station heat drain of the present embodiment 13 System and the heat energy transformation efficiency of conventional heat energy machine（Conventional heat energy machine, under 40-60 DEG C of low-temperature heat source, heat energy efficiency is very low, Efficiency is less than 3%, and heat energy is more difficult to be utilized）Compare, the pressure-adjustable condensation thermal power of the utilization nuclear power station heat drain of the present embodiment The energy transformation efficiency of system is higher than the heat energy transformation efficiency of conventional heat energy machine by 11.8% or so.
Embodiment 14（As shown in figure 22）：It is with 13 difference of embodiment：The condensing units 5 also have additional One booster pump 53, booster pump 53 is arranged on 51 middle-end of condensing tube；The structure is taken, the liquefaction of working medium can be accelerated, increase turbine Machine air inlet and the pressure reduction of air vent, reduce the gas temperature of gas turbine exhaust mouth.
Carried out by condensing dynamic system of heat energy to the pressure-adjustable using nuclear power station heat drain in above-described embodiment 14 Experiment, enters the hot water of different temperatures to heat collector 1 and gasification installation 2, and it is 3000L/ that sink temperature is 10 DEG C, drainage rates S, in circulation pipe, refrigerant flow rate enters according to the operation stability of the pressure-adjustable condensation dynamic system of heat energy using nuclear power station heat drain Row adjustment；Experiment effect is：When hot water temperature is 40 DEG C or so, heat energy transformation efficiency is about 9.8%, and hot water temperature is 45 DEG C of left sides When right, heat energy transformation efficiency is about 11.6%, and when hot water temperature is 50 DEG C or so, heat energy transformation efficiency is about 14.4%, hot water temperature When spending for 55 DEG C or so, heat energy transformation efficiency is about 18%, and when hot water temperature is 60 DEG C or so, heat energy transformation efficiency is about 19%, By being analyzed to data, the pressure-adjustable of the utilization nuclear power station heat drain of the present embodiment 14 condensation dynamic system of heat energy with normal The heat energy transformation efficiency of rule heat energy machine（Conventional heat energy machine, under 40-60 DEG C of low-temperature heat source, heat energy efficiency is very low, and efficiency is low In 3%, heat energy is more difficult to be utilized）Compare, the pressure-adjustable condensation dynamic system of heat energy of the utilization nuclear power station heat drain of the present embodiment Energy transformation efficiency is higher than the heat energy transformation efficiency of conventional heat energy machine by 11.8% or so.
Embodiment 15（As shown in figure 23）：It is with 13 difference of embodiment：The condensing units 5 have additional many Individual booster pump 53, booster pump 53 is evenly distributed in condensing tube 51, is stated booster pump 53 and is adopted turbocharging, and multiple booster pumps 53 lead to Cross power drive mechanism to be driven by same motor；Take the structure, can accelerate the liquefaction of working medium, increase turbine air inlet with The pressure reduction of air vent, reduces the gas temperature of gas turbine exhaust mouth.
Carried out by condensing dynamic system of heat energy to the pressure-adjustable using nuclear power station heat drain in above-described embodiment 15 Experiment, enters the hot water of different temperatures to heat collector 1 and gasification installation 2, and it is 3000L/ that sink temperature is 10 DEG C, drainage rates S, in circulation pipe, refrigerant flow rate enters according to the operation stability of the pressure-adjustable condensation dynamic system of heat energy using nuclear power station heat drain Row adjustment；Experiment effect is：When hot water temperature is 40 DEG C or so, heat energy transformation efficiency is about 10%, and hot water temperature is 45 DEG C or so When, heat energy transformation efficiency is about 11.8%, and when hot water temperature is 50 DEG C or so, heat energy transformation efficiency is about 14.6%, hot water temperature During for 55 DEG C or so, heat energy transformation efficiency is about 18%, and when hot water temperature is 60 DEG C or so, heat energy transformation efficiency is about 19.3%, By being analyzed to data, the pressure-adjustable of the utilization nuclear power station heat drain of the present embodiment 15 condensation dynamic system of heat energy with normal The heat energy transformation efficiency of rule heat energy machine（Conventional heat energy machine, under 40-60 DEG C of low-temperature heat source, heat energy efficiency is very low, and efficiency is low In 3%, heat energy is more difficult to be utilized）Compare, the pressure-adjustable condensation dynamic system of heat energy of the utilization nuclear power station heat drain of the present embodiment Energy transformation efficiency is higher by 12.6% than the heat energy transformation efficiency of conventional heat energy machine.
Embodiment 16：It is with 15 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.
Carried out by condensing dynamic system of heat energy to the pressure-adjustable using nuclear power station heat drain in above-described embodiment 16 Experiment, enters the hot water of different temperatures to heat collector 1 and gasification installation 2, and it is 3000L/ that sink temperature is 10 DEG C, drainage rates S, heightens the pressure of working medium in condensing units 5, while heighten sender matter pressure in gasification installation 2, in circulation pipe refrigerant flow rate according to It is adjusted using the operation stability of the pressure-adjustable condensation dynamic system of heat energy of nuclear power station heat drain；Experiment effect is：Hot water When temperature is 40 DEG C or so, heat energy transformation efficiency is about 9.2%, and when hot water temperature is 45 DEG C or so, heat energy transformation efficiency is about 10.8%, when hot water temperature is 50 DEG C or so, heat energy transformation efficiency is about 14%, and when hot water temperature is 55 DEG C or so, heat energy is converted Efficiency is about 17.8%, and when hot water temperature is 60 DEG C or so, heat energy transformation efficiency is about 47%, by being analyzed to data, this The pressure-adjustable condensation dynamic system of heat energy of the utilization nuclear power station heat drain of embodiment 16 and the heat energy conversion effect of conventional heat energy machine Rate（Conventional heat energy machine, under 40-60 DEG C of low-temperature heat source, heat energy efficiency is very low, and efficiency is less than 3%, and heat energy is more difficult to be utilized） Compare, the energy transformation efficiency of the pressure-adjustable condensation dynamic system of heat energy of the utilization nuclear power station heat drain of the present embodiment is than conventional heat energy The heat energy transformation efficiency of machine is high by 11.8% or so.
Embodiment 17：It is with 15 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.
Carried out by condensing dynamic system of heat energy to the pressure-adjustable using nuclear power station heat drain in above-described embodiment 17 Experiment, enters the hot water of different temperatures to heat collector 1 and gasification installation 2, and it is 3000L/ that sink temperature is 10 DEG C, drainage rates S, in circulation pipe, refrigerant flow rate enters according to the operation stability of the pressure-adjustable condensation dynamic system of heat energy using nuclear power station heat drain Row adjustment；Experiment effect is：When hot water temperature is 40 DEG C or so, heat energy transformation efficiency is about 9.4%, and hot water temperature is 45 DEG C of left sides When right, heat energy transformation efficiency is about 11%, and when hot water temperature is 50 DEG C or so, heat energy transformation efficiency is about 14.4%, hot water temperature During for 55 DEG C or so, heat energy is converted, and when hot water temperature is 60 DEG C or so, heat energy transformation efficiency is about 19%；By carrying out to data Analysis, the pressure-adjustable condensation dynamic system of heat energy of the utilization nuclear power station heat drain of the present embodiment 17 and the heat energy of conventional heat energy machine Transformation efficiency（Conventional heat energy machine, under 40-60 DEG C of low-temperature heat source, heat energy efficiency is very low, and efficiency is less than 3%, and heat energy is more difficult It is utilized）Compare, the energy transformation efficiency ratio of the pressure-adjustable condensation dynamic system of heat energy of the utilization nuclear power station heat drain of the present embodiment The heat energy transformation efficiency of conventional heat energy machine is high by 11.5% or so.
Embodiment 18：It is with 15 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.
Carried out by condensing dynamic system of heat energy to the pressure-adjustable using nuclear power station heat drain in above-described embodiment 18 Experiment, enters the hot water of different temperatures to heat collector 1 and gasification installation 2, and it is 3000L/ that sink temperature is 10 DEG C, drainage rates S, in circulation pipe, refrigerant flow rate enters according to the operation stability of the pressure-adjustable condensation dynamic system of heat energy using nuclear power station heat drain Row adjustment；Experiment effect is：When hot water temperature is 40 DEG C or so, heat energy transformation efficiency is about 9.6%, and hot water temperature is 45 DEG C of left sides When right, heat energy transformation efficiency is about 11.4%, and when hot water temperature is 50 DEG C or so, heat energy transformation efficiency is about 14.6%, hot water temperature When spending for 55 DEG C or so, heat energy transformation efficiency is about 18.1%, and when hot water temperature is 60 DEG C or so, heat energy transformation efficiency is about 19.1%；By being analyzed to data, the pressure-adjustable condensation thermal power system of the utilization nuclear power station heat drain of the present embodiment 16 System and the heat energy transformation efficiency of conventional heat energy machine（Conventional heat energy machine, under 40-60 DEG C of low-temperature heat source, heat energy efficiency is very low, Efficiency is less than 3%, and heat energy is more difficult to be utilized）Compare, the pressure-adjustable condensation thermal power of the utilization nuclear power station heat drain of the present embodiment The energy transformation efficiency of system is higher by 12.2% than the heat energy transformation efficiency of conventional heat energy machine.
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 pressure-adjustable of utilization nuclear power station heat drain condenses dynamic system of heat energy, including heat collector（1）, gasification installation （2）, turbine（3）, nuclear power station heat drain road（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）With one-way hydraulic pump（9）Pass sequentially through and follow Endless tube（6）Circulation UNICOM, circulating line are realized in road（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 nuclear power station heat drain road（4）Interior, the condensing units （5）Installed in deep-water low-temperature area, the heat collector（1）Including thermal-collecting tube（11）And heat collecting sheet（12）, heat collecting sheet（12）Parallel Spaced apart, thermal-collecting tube（11）Fold-type is distributed in heat collecting sheet（12）In, gasification installation（2）Including the heat-absorbing chamber that gasifies（21）And gasification Pressure controller（22）, gasify pressure controller（22）Installed in gasification heat-absorbing chamber（21）Interior, gasify pressure controller（22）For circulation industrial Quality Control Pressure, the turbine（3）With condensing units（5）Between be additionally provided with working medium actuator (10）, working medium actuator (10）Including whirlpool Wheel current limiter (101）With pressure voltage stabilizing pressure controller (102）, turbine current limiter (101）Including turbine structure (103）And secondary speed Controller (104）, pressure voltage stabilizing pressure controller (102）Including slow pressure storage stream cylinder (105）Gentle pressure piston (106）And barostat (107）, delay pressure storage stream cylinder (105）Top UNICOM circulating line（6）, delay pressure storage stream cylinder (105）Bottom UNICOM air pressure adjustment Device (107）, delay pressure piston (106）Installed in slow pressure storage stream cylinder (105）Interior.
2. the pressure-adjustable condensation dynamic system of heat energy of utilization nuclear power station heat drain according to claim 1, is characterized in that：Institute State pressure voltage stabilizing pressure controller (102）Also include pressure transducer (108）, temperature sensor (109）With single-chip microcomputer (1010）, monolithic Machine (1010）In be stored with cycle fluid（7）In different pressure PiUnder condensation temperature TiData, pressure transducer (108）And temperature Degree sensor (109）It is evenly distributed on condensing tube（51）Interior, pressure transducer (108）With temperature sensor (109）Data cube computation Single-chip microcomputer (1010）, single-chip microcomputer (1010）Control connection barostat (107）With secondary speed controller (104）.
3. the pressure-adjustable condensation dynamic system of heat energy of utilization nuclear power station heat drain according to claim 2, is characterized in that：Institute State gasification heat-absorbing chamber（21）With thermal-collecting tube（11）Between be additionally provided with atomizing mouth（23）.
4. the pressure-adjustable condensation dynamic system of heat energy of utilization nuclear power station heat drain according to claim 3, is characterized in that：Institute State gasification heat-absorbing chamber（21）Horizontal cross-section in Rhizoma Nelumbinis poroid.
5. the pressure-adjustable condensation dynamic system of heat energy of utilization nuclear power station heat drain according to claim 3, is characterized in that：Institute State gasification heat-absorbing chamber（21）Horizontal cross-section all poroid in honeycomb.
6. the pressure-adjustable condensation dynamic system of heat energy of utilization nuclear power station heat drain according to claim 3, is characterized in that：Institute State heat collecting sheet（12）In planar sheet.
7. the pressure-adjustable condensation dynamic system of heat energy of utilization nuclear power station heat drain according to claim 3, is characterized in that：Institute State heat collecting sheet（12）Lamellar in curved surface.
8. the pressure-adjustable condensation dynamic system of heat energy of utilization nuclear power station heat drain according to claim 3, is characterized in that：Institute State heat collecting sheet（12）It is in be in staggered distribution.
9. the pressure-adjustable condensation dynamic system of heat energy of utilization nuclear power station heat drain according to claim 3, is characterized in that：Institute State gasification heat-absorbing chamber（21）Positioned at nuclear power station heat drain road（4）Upstream, heat collector（1）Positioned at nuclear power station heat drain road（4） Downstream.
10. the pressure-adjustable condensation dynamic system of heat energy of utilization nuclear power station heat drain according to claim 7, is characterized in that： The turbine（3）Including turbine casing（31）, revolving wormgear structure（32）, air inlet（33）, air vent（34）And seal shaft Hold（35）, revolving wormgear structure（32）By sealed bearings（35）Installed in turbine casing（31）Interior, air inlet（33）And aerofluxuss Mouthful（34）It is distributed in turbine casing（31）Radially opposite sides, the revolving wormgear structure（32）Including moving vane（321）And grooved Rotating shaft（322）, grooved rotating shaft（322）Axial plane on be distributed fluted（323）, moving vane（321）By spring（324）Activity Installed in grooved rotating shaft（322）Groove（323）Interior, grooved rotating shaft（322）By sealed bearings（35）It is eccentrically mounted at turbine Casing（31）Interior, air inlet（33）Nearer away from eccentric shaft, air vent（34）Away from eccentric shaft farther out, adjacent activities blade（321）Between Chamber is constituted, with air inlet（33）Communicate for expansion chamber 331, with air vent（34）Communicate for discharge chamber（341）.
CN201610760127.2A 2016-08-30 2016-08-30 Pressure-adjustable condensation heat energy power system using nuclear power plant hot drained water Withdrawn CN106437902A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110671603A (en) * 2018-07-03 2020-01-10 山东恒昌圣诚化工股份有限公司 External heating type solid ammonia filling device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110671603A (en) * 2018-07-03 2020-01-10 山东恒昌圣诚化工股份有限公司 External heating type solid ammonia filling device

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