CN106246273A - A kind of biofermentation dynamic system of heat energy based on semi-conductor condensation - Google Patents

A kind of biofermentation dynamic system of heat energy based on semi-conductor condensation Download PDF

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Publication number
CN106246273A
CN106246273A CN201610760163.9A CN201610760163A CN106246273A CN 106246273 A CN106246273 A CN 106246273A CN 201610760163 A CN201610760163 A CN 201610760163A CN 106246273 A CN106246273 A CN 106246273A
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heat energy
heat
biofermentation
temperature
semi
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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
    • F01K13/00—General layout or general methods of operation of complete plants
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K13/00—General layout or general methods of operation of complete plants
    • F01K13/006—Auxiliaries or details not otherwise provided for
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K13/00—General layout or general methods of operation of complete plants
    • F01K13/02—Controlling, e.g. stopping or starting
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • 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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K9/00—Plants characterised by condensers arranged or modified to co-operate with the engines

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

The invention discloses a kind of biofermentation dynamic system of heat energy based on semi-conductor condensation, pass sequentially through circulating line including heat collector, gasification installation, turbine, condensing unit and one-way hydraulic pump and realize circulation UNICOM, circulating line is contained within cycle fluid, heat collector and gasification installation is had to be arranged in biofermentation pond, condensing unit is arranged on outside biofermentation pond, condensing unit includes condensing tube and heat emission fan, and condensing tube is made by thermo-electric generation sheet；Biofermentation dynamic system of heat energy based on semi-conductor condensation of the present invention has condensing rate faster, can reduce condensation row's energy, improve heat energy transformation efficiency, and stable, power adjustable.

Description

A kind of biofermentation dynamic system of heat energy based on semi-conductor condensation
Technical field
The invention belongs to utilization of energy apparatus field, a kind of biofermentation thermal power based on semi-conductor condensation System.
Background technology
The energy is the important substance basis that human society is depended on for existence and development.Make a general survey of the history of human social development, people The major progress each time of class civilization is all along with improvement and the replacement of the energy.The exploitation of the energy greatly advance the world Economy and the development of human society.
But along with the consumption that is continuously developed of the energy, the non-renewable energy resources such as oil, colliery, natural gas progressively tighten, energy The saving in source and recycling progressively is taken seriously.The substance of the energy strategy of current China is: adheres to economization at first, base oneself upon Domestic, diverse development, depend on science and technology, protect environment, strengthen international mutual beneficial co-operation, make great efforts to construct stable, economical, cleaning, safety Energy supply system, support the sustainable development of economic society with the sustainable development of the energy.
China implements the measure of energy conservation comprehensively: push structure adjusts, and accelerates the upgrading and optimization of industrial structure, sends out energetically Exhibition new high-tech industry and service trade, strictly limit highly energy-consuming, high consumptive material, highly water intensive industry development, eliminate the backward production facilities, and promotes The right-about of Economic Development Mode, accelerates to build energy-saving industrial system.Strengthen industrial energy saving, accelerate technological transformation, improve Management level, reduce energy resource consumption.Implement energy conservation project, encourage the popularization and application of energy-efficient product, greatly develop energy-saving Ground type building, improves efficiency of energy utilization, accelerates energy-saving monitoring and technical service system construction, strengthens energy-saving monitoring, innovation clothes Business platform.Strengthen management energy-conservation, actively push forward preferentially to purchase energy-conservation (including water saving) product, study and define and encourage energy-conservation property tax Policy.Advocate social energy conservation, conduct vigorous propaganda the significance saving the energy, constantly strengthen whole people's resource awareness of unexpected development and save meaning Know.
For response national energy-saving strategy, increasing enterprise starts research and development, uses energy-saving equipment, and strengthens discarded product Can thing, the utilization of waste heat energy.Wherein, utilize aspect at waste heat, mainly realize surplus energy utility by thermal generating equipment.Existing Some thermal generating equipments include plurality of classes, but can be divided mainly into two classes, and a class is to utilize turbine that heat energy is changed into machine Tool energy, then changes mechanical energy is become electric energy, the generating equipment of this kind of principle classification is the most ripe, and kind is many；Another kind of is to utilize Pyroelectric effect principle, is directly translated into electric potential energy by thermoelectric conversion element by heat energy, but due to for generation technology aspect not Maturation, electrical power is little, and manufacturing cost is high, and thermoelectric conversion efficiency is low, is mainly used in microelectronic.
Present stage, most enterprises is big due to complementary energy eliminating amount, in the utilization of waste heat, the most also needs to rely on above-mentioned first Class thermal generating equipment, changes into heat energy mechanical energy by turbine, then changes mechanical energy is become electric energy.Such heat existing Generating equipment can mainly include cycle fluid, heat collector, gasification installation, turbine, electromotor and condensing unit；During work, Cycle fluid first passes through gasification installation in circulating line, working medium is gasified and promotes turbine to rotate, and turbine drives to be sent out Electric power generation, the working medium after gasification, when by turbine, externally does work, and temperature and air pressure can reduce, and pass through condensing unit It is cooled to liquid refrigerant.
But, existing thermal generating equipment common problem is: a. is high to the temperature requirement of high temperature heat source, one As more than 200 DEG C, and heat energy transformation efficiency is on the low side, and heat energy transformation efficiency is generally 15% to 35%；B. the hot type of condensing unit Amount is relatively big, and thermal waste is big, slow by the condensation rate of natural condensation mode, and use actively condensing mode (blower fan air-cooled or Liquid pump water-cooled) need extra power consumption；C. the problem that turbine easily occurs leaking working medium；D. secondary speed is unstable, and easily goes out Existing stuck problem；E. the Heat-collecting effect of heat collector is the best, and extraneous exhaust-heat absorption rate is little, and f. working medium gasification temperature is unstable, work Matter condensation effect is the best, and working medium is apt to deteriorate or impurity occurs；G. existing equipment volume is bigger.
Biofermentation is widely used in the production of industrial chemicals, biological medicine, and biological fermentation process can produce substantial amounts of Heat, the temperature of fermentation heap may be up to 70-75 DEG C, in process of production, in order to the temperature preventing fermentation heap is too high, need to often stir Move and dispel the heat；This kind of radiating mode fails to utilize heat of fermentation, there is the waste of the energy, dispelled the heat at this meanwhile Journey needs to run blender, and energy consumption is bigger.
Summary of the invention
The purpose that the present invention is to be realized is: comprehensive utilization biofermentation heat energy, and the heat energy improving thermal hardware converts effect Rate, the hot type amount of reduction and thermal waste, stablize working medium gasification temperature and refrigerant flow rate, improve working medium quality, prevent working medium from becoming Matter, improves turbine structure, it is to avoid turbine is revealed and rotary speed unstabilization, improves condensing unit, accelerates condensing rate；Above-mentioned to solve In background technology existing for existing thermal hardware: heat energy transformation efficiency is low, working medium gasification temperature is unstable, working medium condensation effect The best, working medium is apt to deteriorate or impurity occurs, and refrigerant leakage easily occurs in turbine, and secondary speed is unstable and easily goes out Existing stuck, the thermal waste of condensing unit is big, condensing rate slow or needs the problems such as extra power consumption.
For solving its technical problem the technical solution adopted in the present invention it is: a kind of biofermentation based on semi-conductor condensation Dynamic system of heat energy, including heat collector, gasification installation, turbine, biofermentation pond, condensing unit, circulating line, circulation industrial Matter and one-way hydraulic pump, heat collector, gasification installation, turbine, condensing unit and one-way hydraulic pump pass sequentially through circulating line Realizing circulation UNICOM, circulating line is contained within cycle fluid；
It is characterized in that: described heat collector and gasification installation are arranged in biofermentation pond, and described condensing unit is arranged on biology Outside fermentation vat, described 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 collection In backing；
Gasification installation includes gasify heat-absorbing chamber and gasification pressure controller, and gasification pressure controller is arranged in gasification heat-absorbing chamber, and gasify pressure control Device is used for cycle fluid blood pressure lowering；Heat source temperature, high-pressure liquid work is reached after high-pressure liquid working medium fully heats in thermal-collecting tube Mass flow enters the heat-absorbing chamber that gasifies, and the gasification pressure controller in gasification heat-absorbing chamber is controlled by pressure so that it is liquid refrigerant endothermic gasification, gas Chemical industry matter is blood pressure lowering acting in turbine；This kind of structure, compared in thermal-collecting tube direct gasification, can be prevented effectively from gasification working medium Mix and have liquid refrigerant, working medium can be made to gasify evenly.
Described condensing unit is arranged on low temperature environment (in normal temperature air or in liquid).
Condensing unit includes condensing tube and heat emission fan, and condensing tube uniformly divides Multi-layers distributing, the mutual UNICOM of condensing tube, heat emission fan Being arranged on above or below condensing tube, heat emission fan drives with convulsion mode or pressure wind mode；Described condensing tube passes through thermo-electric generation Sheet is made, and thermo-electric generation sheet includes sheet metal, p-type semiconductor, n-type semiconductor, dielectric substrate layer and output electrode, dielectric substrate Layer is uniformly interspersed with p-type semiconductor and n-type semiconductor, equally distributed p-type semiconductor and n-type semiconductor by sheet metal string Connection, p-type semiconductor is connected output electrode respectively with the series connection end at the whole story of n-type semiconductor.
As optimizing further, between condensing unit and heat collector, it is additionally provided with contaminant filter pump.
As optimizing further, the output electrode end of described thermo-electric generation sheet be connected with in turn manostat, booster transformer, Accumulator, accumulator is used for heat emission fan or the power supply of one-way hydraulic pump.
As the further optimization of such scheme, between described gasification heat-absorbing chamber and thermal-collecting tube, it is additionally provided with atomizing mouth.
As the further optimization of such scheme, the horizontal cross-section of described gasification heat-absorbing chamber is that Rhizoma Nelumbinis is poroid.
As the further optimization of such scheme, the horizontal cross-section of described gasification heat-absorbing chamber is all poroid in honeycomb.
As the further optimization of such scheme, described gasification heat-absorbing chamber is positioned at the upstream in biofermentation pond, heat collector It is positioned at the downstream in biofermentation pond.
As the further optimization of such scheme, described heat collecting sheet is planar sheet or curved surface lamellar or is in staggered distribution.
The most concrete as such scheme optimizes, and turbine is conventional steam turbine.
The most concrete as such scheme optimizes, and turbine is the steam turbine comprising multistage blade.
The most concrete as such scheme optimizes, and turbine is tesla's turbine.
The most concrete as such scheme optimizes, and turbine is radial outward flow turbine.
The most concrete as such scheme optimizes, and the exhaust ports of described turbine is provided with precondenser；Take This structure can increase the pressure reduction of air inlet and air vent, improves the transformation efficiency of turbine.
The most concrete as such scheme optimizes, and described precondenser includes working medium conduction pipe and condensation endothermic tube, Working medium conduction pipe is used for connecting air vent and circulating line, and condensation endothermic tube turns on the heat of intraductal working medium for absorbing working medium, Working medium conduction pipe and condensation endothermic tube spiral paratactic contact, be heat recipient fluid in condensation endothermic tube, for increasing condensation efficiency, and heat absorption The flow direction of fluid is contrary with the flow direction of working medium conducting intraductal working medium.
The most concrete as such scheme optimizes, and described condensation endothermic tube uses UNICOM's one-way hydraulic pump and collection hot charging Circulating line between putting；Owing to the circulating line between one-way hydraulic pump and heat collector needs to absorb heat, and working medium conduction pipe Interior working medium needs heat extraction, and this structure recycles working medium heat in circulating line largely, increases thermal transition efficiency.
The most concrete as such scheme optimizes, and described condensing tube becomes oblique type to be distributed.
The most concrete as such scheme optimizes, and described condensing tube becomes horizontal or vertical distribution.
The most concrete as such scheme optimizes, and when described condensing tube becomes horizontal distribution, upper and lower layer condensing tube is mutual Stagger.
The most concrete as such scheme optimizes, and described condensing tube is copper metal tube or stability alloying metal Pipe.
The most concrete as such scheme optimizes, and in order to accelerate the liquefaction of working medium, reduces the thermal discharge of condensation process, Described condensing unit also has additional booster pump, and booster pump is arranged on condensing tube middle-end.
The most concrete as such scheme optimizes, in order to reduce the compression energy consumption of working medium in condensing unit, described cold In solidifying device, compress mode takes staged to compress, and is provided with multiple booster pump in condensing unit, and booster pump is evenly distributed on cold In solidifying pipe；Take this structure, compared to using single booster pump, can preferably realize fractional condensaion, improve pressure largely The poorest, and reduce energy consumption needed for supercharging.
The most concrete as such scheme optimizes, in order to avoid the working medium of liquefaction uncooled in condensing tube enters unidirectional Hydraulic pump, condensing tube tail end is provided with catch box.
The most concrete as such scheme optimizes, and in order to accelerate heat radiation, condensing unit is additionally provided with fin.
The most concrete as such scheme optimizes, and described booster pump uses turbocharging, and multiple booster pumps are by dynamic Force transmission mechanism is driven by same motor.
The most concrete as such scheme optimizes, and described cycle fluid uses propanol.
The most concrete as such scheme optimizes, and described cycle fluid uses methanol.
The most concrete as such scheme optimizes, and described cycle fluid uses ethanol.
The most concrete as such scheme optimizes, and described cycle fluid uses isopropanol.
The most concrete as such scheme optimizes, and described cycle fluid uses liquefied ammonia.
The most concrete as such scheme optimizes, and described cycle fluid uses conventional freon.
The most concrete as such scheme optimizes, and is additionally provided with working medium actuator between turbine and condensing unit, Described working medium actuator includes turbine current limiter and pressure voltage stabilizing pressure controller, and turbine current limiter includes turbine structure and secondary speed Controller, pressure voltage stabilizing pressure controller includes slow pressure storage stream cylinder gentle pressure piston and barostat, the top connection of slow pressure storage stream cylinder Logical circulating line, the bottom UNICOM barostat of slow pressure storage stream cylinder, slow pressure piston is arranged in slow pressure storage stream cylinder；Work as circulation pipe When in road, the pressure of working medium or flow velocity change, turbine current limiter can realize flow velocity by limiting the rotation of turbine structure Limiting, part working medium can be postponed and pressed storage stream cylinder outflow or flow into expansion or the compression realizing volume simultaneously, thus the stable pressure of realization Strong effect.
Operation principle: biofermentation dynamic system of heat energy based on semi-conductor condensation described in this invention, during work, circulation industrial Matter is absorbed heat the heat source temperature that reaches a high temperature in heat collector, then flows in gasification installation, is vaporized suction by blood pressure lowering in a small amount Heat, flows to turbine after working medium gasification, drives rotating turbine；After gasification working medium flows through turbine, owing to externally doing work, its work Matter temperature and air pressure all can reduce, and cause part working medium to liquefy；After gasification working medium flows through turbine, working medium flows to working medium successively Actuator and condensing unit；Working medium actuator for controlling the pressure of working medium, flow velocity in circulating line, working medium actuator energy according to Extraneous heat absorption district and the temperature conditions of heat release zone, regulation working medium condensing temperature or gasification temperature, it is thus possible to be effectively improved heat energy Transformation efficiency；Working medium can be liquefied by condensing unit completely；After liquefaction, working medium sequentially passes through contaminant filter pump and one-way hydraulic pump, miscellaneous Matter filter pump can by contaminant filter in working medium out, and working medium is carried out unidirectional pumping supercharging by one-way hydraulic pump；After liquefaction, working medium depends on Secondary after contaminant filter pump and one-way hydraulic pump, and it is again introduced into gasification installation, complete a circulation.
Condensing tube in biofermentation dynamic system of heat energy based on semi-conductor condensation described in this invention uses thermo-electric generation Sheet is made, and the p-type semiconductor of thermo-electric generation sheet and n-type semiconductor can produce electromotive force when producing the temperature difference at two ends, p-type semiconductor Heat source side and low-temperature receiver end are respectively low potential end and high potential end, and heat source side and the low-temperature receiver end of n-type semiconductor are respectively high potential End and low potential end, when p-type semiconductor and n-type semiconductor can realize voltage superposition when connecting, thus realize generating；Therefore, temperature Its partial heat, while transmission heat, can be changed into electromotive force by difference generating sheet.
Beneficial effect: biofermentation dynamic system of heat energy based on semi-conductor condensation of the present invention, the most existing skill Heat energy machine in art, has advantage and a progress of following several respects: 1. pressure and the stream by setting up working medium actuator, to working medium Amount is controlled, and can be effectively improved gasification usefulness and condensation efficiency, and stablize working medium gasification temperature and refrigerant flow rate, prevents from sealing Part deformation is bigger, it is to avoid secondary speed shakiness and working medium leakage problem；2. by setting up precondenser, it is possible to increase turbine enters QI KOU and the pressure reduction of air vent, and the heat energy of working medium can be recycled, it is achieved heat absorption and the heat extraction to cycle fluid difference section Process comprehensively utilizes, and reduces thermal waste and cooling power consumption；3., by setting up contaminant filter pump and one-way hydraulic pump, can have Effect prevents working medium rotten and more impurity occurs, and prevents working medium from refluxing；4. by setting up booster pump, energy in condensing unit Improve condensing rate largely, reduce condensation power consumption；5. condensing tube uses thermo-electric generation sheet make, utilization condensation can be divided The temperature difference calorific potential of process, improves heat energy transformation efficiency, and utilizes the interior electric current produced of thermo-electric generation sheet to accelerate thermal energy conduction speed； 6. fully utilize the heat energy of biological fermentation process, and the temperature of fermentation vat can be stablized.
Accompanying drawing explanation
Fig. 1 is the Integral connection structure schematic diagram of the present invention program one；
Fig. 2 be the present invention program one biofermentation pond in mounting structure schematic diagram；
Fig. 3 is the condensing unit attachment structure schematic diagram of the present invention program one；
Fig. 4 is the condensing tube tube wall Structure of cross section schematic diagram of the present invention program one；
Fig. 5 is the gasification heat-absorbing chamber structural representation of the present invention program one；
Fig. 6 is the heat collector structural representation of the present invention program two；
Fig. 7 is the heat collector structural representation of the present invention program three；
Fig. 8 is the gasification pressure controller structural representation of the present invention program four；
Fig. 9 is the atomizing mouth mounting connection structure schematic diagram of the present invention program five；
Figure 10 is the gasification heat-absorbing chamber cross section structure schematic diagram of the present invention program six；
Figure 11 is the gasification heat-absorbing chamber cross section structure schematic diagram of the present invention program seven；
Figure 12 is the Integral connection structure schematic diagram of the present invention program 11；
Figure 13 is the working medium controller structure schematic diagram of the present invention program 11；
Figure 14 is the precondenser structural representation of the present invention program 12；
Figure 15 is the precondenser attachment structure schematic diagram of the present invention program 13；
Figure 16 is the condensing unit vertical cross section structural representation of the present invention program 14；
Figure 17 is the condensing unit vertical cross section structural representation of the present invention program 15；
Figure 18 is the condensing unit vertical cross section structural representation of the present invention program 16；
Figure 19 is the condensing unit structural representation of the present invention program 17；
Figure 20 is the condensing unit structural representation of the present invention program 18；
In figure:
1 be heat collector, 11 be thermal-collecting tube, 12 for heat collecting sheet；
2 be gasification installation, 21 for gasification heat-absorbing chamber, 22 for gasification pressure controller, 221 for differential pressure control valve, 222 for gasification pressure sense Answer device, 23 for atomizing mouth；
3 be turbine, 36 for precondenser, 361 for working medium conduction pipe, 362 for condensation endothermic tube；
4 is biological fermentation vat；
5 be condensing unit, 51 be condensing tube, 511 be thermo-electric generation sheet, 512 be sheet metal, 513 be p-type semiconductor, 514 for n Type quasiconductor, 515 be dielectric substrate layer, 516 be output electrode, 517 be manostat, 518 be booster transformer, 519 for electric power storage Pond, 52 be heat emission fan, 53 be booster pump, 54 be catch box, 55 for fin；
6 is circulating line；
7 is cycle fluid；
8 is contaminant filter pump；
9 is one-way hydraulic pump；
10 be working medium actuator, 101 be turbine current limiter, 102 be pressure voltage stabilizing pressure controller, 103 be turbine structure, 104 for whirlpool Wheel speed controller, 105 be slow pressure storage stream cylinder, 106 be slow pressure piston, 107 be barostat.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete Describe wholely；Obviously, described embodiment is only a part of embodiment of the present invention rather than whole embodiments.Based on Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under not making creative work premise Embodiment, broadly falls into the scope of protection of the invention.
Embodiment one (as shown in Figure 1): a kind of biofermentation dynamic system of heat energy based on semi-conductor condensation, including thermal-arrest Device 1, gasification installation 2, turbine 3, biofermentation pond 4, condensing unit 5, circulating line 6, cycle fluid 7 and one-way hydraulic pump 9, heat collector 1, gasification installation 2, turbine 3, condensing unit 5 and one-way hydraulic pump 9 pass sequentially through circulating line 6 and realize circulation UNICOM, circulating line 6 is contained within cycle fluid 7；
(as shown in Figure 2) described heat collector 1 and gasification installation 2 are arranged in biofermentation pond 4, and described condensing unit 5 is installed Outside biofermentation pond 4, described heat collector 1 includes thermal-collecting tube 11 and heat collecting sheet 12, and heat collecting sheet 12 parallel interval is distributed, thermal-arrest Pipe 11 fold-type 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 Being arranged in gasification heat-absorbing chamber 21, gasification pressure controller 22 is for liquid refrigerant blood pressure lowering；When high-pressure liquid working medium is in thermal-collecting tube 11 Fully reaching heat source temperature after heating, high-pressure liquid working medium flows into gasification heat-absorbing chamber 21, the gasification pressure control in gasification heat-absorbing chamber 21 Device 22 is controlled by pressure so that it is liquid refrigerant endothermic gasification, the blood pressure lowering acting in turbine 3 of gasification working medium；This kind of structure phase Than in thermal-collecting tube 11 direct gasification, can be prevented effectively from gasification working medium to mix has liquid refrigerant, and working medium can be made to gasify evenly.
Having explanation further as above-mentioned embodiment, described condensing unit 5 is arranged on low temperature environment (normal temperature air In or liquid in).
Having explanation further as above-mentioned embodiment, heat collecting sheet 12 is in planar sheet.
Having explanation further as above-mentioned embodiment, (as shown in Figure 3) described condensing unit 5 includes condensing tube 51 With heat emission fan 52, condensing tube 51 uniformly divides Multi-layers distributing, and the mutual UNICOM of condensing tube 51, heat emission fan 52 is arranged on above condensing tube 51 Or lower section, heat emission fan 52 drives with convulsion mode or pressure wind mode；
Having explanation further as above-mentioned embodiment, (as shown in Figure 4) described condensing tube 51 is by thermo-electric generation sheet 511 Making, described thermo-electric generation sheet 511 includes sheet metal 512, p-type semiconductor 513, n-type semiconductor 514, dielectric substrate layer 515 and Output electrode 516, dielectric substrate layer 515 is uniformly interspersed with p-type semiconductor 513 and n-type semiconductor 514, equally distributed p-type half Conductor 513 and n-type semiconductor 514 are connected by sheet metal 512, the end at the whole story of connecting of p-type semiconductor 513 and n-type semiconductor 514 Connect output electrode 516 respectively；Output electrode 516 voltage of thermo-electric generation sheet 511 reaches more than 3V.
Having explanation further as above-mentioned embodiment, output electrode 516 end of described thermo-electric generation sheet 511 is successively Connecting and have manostat 517, booster transformer 518, accumulator 519, accumulator 519 is for heat emission fan 52, the confession of one-way hydraulic pump 9 Electricity.
As further illustrating of above-mentioned embodiment, between described condensing unit 5 and heat collector 1, it is additionally provided with impurity Filter pump 8.
As further illustrating of above-mentioned embodiment, (as shown in Figure 5) described gasification heat-absorbing chamber 21 is by multiple bodys also Row are formed.
As further illustrating of above-mentioned embodiment, described gasification pressure controller 22 is by keeping amount pressure with atmospheric pressure Difference realizes pressure control.
As further illustrating of above-mentioned embodiment, described turbine 3 is conventional vane type steam turbine.
As further illustrating of above-mentioned embodiment, described condensing tube 51 tail end is provided with catch box 54.
As further illustrating of above-mentioned embodiment, described condensing unit 5 is additionally provided with fin 55.
As further illustrating of above-mentioned embodiment, described cycle fluid 7 uses liquefied ammonia.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment one is tested, logical Cross and select multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is sent out according to biology based on semi-conductor condensation The operation stability of ferment dynamic system of heat energy is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, heat energy turns Changing efficiency and be about 6%, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 8.7%, and in fermentation vat, temperature is 58 DEG C During left and right, heat energy transformation efficiency is about 10.8%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 12.8%, When in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 15.5%, life based on semi-conductor condensation in the present embodiment one (conventional heat energy machine, at the low temperature of 40-60 DEG C than conventional thermal energy power machine for the heat energy transformation efficiency of thing heat of fermentation dynamical system Under thermal source, heat energy efficiency is the lowest, efficiency be less than 3%, heat energy is more difficult to be utilized) compare, the present embodiment based on semi-conductor condensation The heat energy transformation efficiency of biofermentation dynamic system of heat energy higher by about 7% than the heat energy transformation efficiency of conventional heat energy machine；Meanwhile, The present embodiment biofermentation based on semi-conductor condensation dynamic system of heat energy cooldown rate is fast, and hot driving is little, runs noise little, fortune Line stabilization is good, can realize power output regulation simultaneously.
Embodiment two (shown in Fig. 6): be with embodiment one difference: as described in heat collector 1 heat collecting sheet 12 in Curved surface lamellar.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment two is tested, logical Cross and select multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is sent out according to biology based on semi-conductor condensation The operation stability of ferment dynamic system of heat energy is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, heat energy turns Changing efficiency and be about 6.5%, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 9.2%, and in fermentation vat, temperature is 58 Time about DEG C, heat energy transformation efficiency is about 11.2%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 13.2%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 16.2%, based on semiconductor cooling in the present embodiment two (conventional heat energy machine, at 40-60 DEG C than conventional thermal energy power machine for the heat energy transformation efficiency of solidifying biofermentation dynamic system of heat energy Low-temperature heat source under, heat energy efficiency is the lowest, efficiency be less than 3%, heat energy is more difficult to be utilized) compare, the present embodiment based on partly leading The heat energy transformation efficiency higher than the heat energy transformation efficiency of conventional heat energy machine 7.8% of the biofermentation dynamic system of heat energy of body condensation is left Right.
Embodiment three (shown in Fig. 7): be with embodiment one difference: as described in heat collector 1 heat collecting sheet 12 in It is in staggered distribution.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment three is tested, logical Cross and select multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is sent out according to biology based on semi-conductor condensation The operation stability of ferment dynamic system of heat energy is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, heat energy turns Changing efficiency and be about 6.5%, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 9.4%, and in fermentation vat, temperature is 58 Time about DEG C, heat energy transformation efficiency is about 11.4%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 13.4%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 16.4%, based on semiconductor cooling in the present embodiment three (conventional heat energy machine, at 40-60 DEG C than conventional thermal energy power machine for the heat energy transformation efficiency of solidifying biofermentation dynamic system of heat energy Low-temperature heat source under, heat energy efficiency is the lowest, efficiency be less than 3%, heat energy is more difficult to be utilized) compare, the present embodiment based on partly leading The heat energy transformation efficiency higher than the heat energy transformation efficiency of conventional heat energy machine 7.2% of the biofermentation dynamic system of heat energy of body condensation is left Right.
Embodiment four (as shown in Figure 8): be with embodiment one difference: described gasification pressure controller 22 includes pressure reduction control Valve 221 processed and gasification pressure induction apparatus 222, differential pressure control valve 221 is positioned at the front end of gasification heat-absorbing chamber 21, and gasify pressure induction apparatus 222 are positioned at gasification heat-absorbing chamber 21 rear end；Differential pressure control valve 221 is used for regulating pressure reduction, and gasification pressure induction apparatus 222 is used for sensing gas The pressure of working medium in change heat-absorbing chamber 21, when pressure is bigger, increases the pressure reduction of differential pressure control valve 221, when pressure is less, reduces The pressure reduction of differential pressure control valve 221, thus realize the pressure of gasification heat-absorbing chamber 21 is controlled.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment four is tested, logical Cross and select multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is sent out according to biology based on semi-conductor condensation The operation stability of ferment dynamic system of heat energy is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, heat energy turns Changing efficiency and be about 7%, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 9.6%, and in fermentation vat, temperature is 58 DEG C During left and right, heat energy transformation efficiency is about 11.6%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 14%, sends out When in ferment pond, temperature is about 68 DEG C, heat energy transformation efficiency is about 17%, and in the present embodiment four, biology based on semi-conductor condensation is sent out (conventional heat energy machine, at the low-temperature heat source of 40-60 DEG C than conventional thermal energy power machine for the heat energy transformation efficiency of ferment dynamic system of heat energy Under, heat energy efficiency is the lowest, and efficiency is less than 3%, and heat energy is more difficult to be utilized) compare, the life based on semi-conductor condensation of the present embodiment The heat energy transformation efficiency of thing heat of fermentation dynamical system is higher by about 8.5% than the heat energy transformation efficiency of conventional heat energy machine.
Embodiment five (as shown in Figure 9): be with embodiment four difference: described gasification heat-absorbing chamber 21 and thermal-collecting tube 11 Between be additionally provided with atomizing mouth 23.
Tested by the biofermentation dynamic system of heat energy based on semi-conductor condensation of above-described embodiment five, by choosing Select multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is according to biofermentation based on semi-conductor condensation The operation stability of dynamic system of heat energy is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, and heat energy converts Efficiency is about 8%, and when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 10%, and in fermentation vat, temperature is 58 DEG C of left sides Time right, heat energy transformation efficiency is about 12%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 14.8%, fermentation When in pond, temperature is about 68 DEG C, heat energy transformation efficiency is about 17.8%, and in the present embodiment five, biology based on semi-conductor condensation is sent out (conventional heat energy machine, at the low-temperature heat source of 40-60 DEG C than conventional thermal energy power machine for the heat energy transformation efficiency of ferment dynamic system of heat energy Under, heat energy efficiency is the lowest, and efficiency is less than 3%, and heat energy is more difficult to be utilized) compare, the life based on semi-conductor condensation of the present embodiment The heat energy transformation efficiency of thing heat of fermentation dynamical system is higher by about 9% than the heat energy transformation efficiency of conventional heat energy machine.
Embodiment six (as shown in Figure 10): be with embodiment five difference: the level of described gasification heat-absorbing chamber 21 is cut Face is that Rhizoma Nelumbinis is poroid.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment six is tested, logical Cross and select multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is sent out according to biology based on semi-conductor condensation The operation stability of ferment dynamic system of heat energy is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, heat energy turns Changing efficiency and be about 8.7%, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 10.4%, and in fermentation vat, temperature is When about 58 DEG C, heat energy transformation efficiency is about 12.8%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 16.2%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 18%, based on semi-conductor condensation in the present embodiment six The heat energy transformation efficiency of biofermentation dynamic system of heat energy than conventional thermal energy power machine, (conventional heat energy machine, at 40-60 DEG C Under low-temperature heat source, heat energy efficiency is the lowest, efficiency be less than 3%, heat energy is more difficult to be utilized) compare, the present embodiment based on quasiconductor The heat energy transformation efficiency of the biofermentation dynamic system of heat energy of condensation is higher by about 9.3% than the heat energy transformation efficiency of conventional heat energy machine.
Embodiment seven (as shown in figure 11): be with embodiment five difference: the level of described gasification heat-absorbing chamber 21 is cut Face is all poroid in honeycomb.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment seven is tested, logical Cross and select multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is sent out according to biology based on semi-conductor condensation The operation stability of ferment dynamic system of heat energy is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, heat energy turns Changing efficiency and be about 9%, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 10.6%, and in fermentation vat, temperature is 58 Time about DEG C, heat energy transformation efficiency is about 13%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 16.6%, When in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 18%, biology based on semi-conductor condensation in the present embodiment seven (conventional heat energy machine, at the Low Temperature Thermal of 40-60 DEG C than conventional thermal energy power machine for the heat energy transformation efficiency of heat of fermentation dynamical system Under source, heat energy efficiency is the lowest, and efficiency is less than 3%, and heat energy is more difficult to be utilized) compare, the present embodiment based on semi-conductor condensation The heat energy transformation efficiency of biofermentation dynamic system of heat energy is higher by about 10% than the heat energy transformation efficiency of conventional heat energy machine.
Embodiment eight: be with embodiment seven difference: described turbine 3 is the steamturbine comprising multistage blade Machine.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment eight is tested, logical Cross and select multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is sent out according to biology based on semi-conductor condensation The operation stability of ferment dynamic system of heat energy is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, heat energy turns Changing efficiency and be about 9.6%, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 11.2%, and in fermentation vat, temperature is When about 58 DEG C, heat energy transformation efficiency is about 13.6%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 17.4%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 47%, based on semi-conductor condensation in the present embodiment eight The heat energy transformation efficiency of biofermentation dynamic system of heat energy than conventional thermal energy power machine, (conventional heat energy machine, at 40-60 DEG C Under low-temperature heat source, heat energy efficiency is the lowest, efficiency be less than 3%, heat energy is more difficult to be utilized) compare, the present embodiment based on quasiconductor The heat energy transformation efficiency higher than the heat energy transformation efficiency of conventional heat energy machine 10.8% of the biofermentation dynamic system of heat energy of condensation is left Right.
Embodiment nine: be with embodiment seven difference: described turbine 3 is tesla's turbine.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment nine is tested, logical Cross and select multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is sent out according to biology based on semi-conductor condensation The operation stability of ferment dynamic system of heat energy is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, heat energy turns Changing efficiency and be about 9.8%, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 11.4%, and in fermentation vat, temperature is When about 58 DEG C, heat energy transformation efficiency is about 13.8%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 17.6%%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 19%, based on semiconductor cooling in the present embodiment nine (conventional heat energy machine, at 40-60 DEG C than conventional thermal energy power machine for the heat energy transformation efficiency of solidifying biofermentation dynamic system of heat energy Low-temperature heat source under, heat energy efficiency is the lowest, efficiency be less than 3%, heat energy is more difficult to be utilized) compare, the present embodiment based on partly leading The heat energy transformation efficiency higher than the heat energy transformation efficiency of conventional heat energy machine 10.4% of the biofermentation dynamic system of heat energy of body condensation is left Right.
Embodiment ten: be with embodiment one difference: described turbine 3 is radial outward flow turbine.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment ten is tested, logical Cross and select multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is sent out according to biology based on semi-conductor condensation The operation stability of ferment dynamic system of heat energy is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, heat energy turns Changing efficiency and be about 9.6%, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 11.2%, and in fermentation vat, temperature is When about 58 DEG C, heat energy transformation efficiency is about 13.6%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 17.6%%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 18.9%, based on quasiconductor in the present embodiment ten (conventional heat energy machine, at 40-60 than conventional thermal energy power machine for the heat energy transformation efficiency of the biofermentation dynamic system of heat energy of condensation DEG C low-temperature heat source under, heat energy efficiency is the lowest, and efficiency is less than 3%, and heat energy is more difficult to be utilized) compare, the present embodiment based on half The heat energy transformation efficiency higher than the heat energy transformation efficiency of conventional heat energy machine 10% of the biofermentation dynamic system of heat energy of conductor condensation is left Right.
Embodiment 11 (shown in Figure 12 and 13): be with embodiment ten difference: as described in turbine 3 be centrifugal Working medium actuator 10 it is additionally provided with between turbine 3 and condensing unit 5 described in formula turbine；Working medium actuator 10 includes that turbine limits Stream device 101 and pressure voltage stabilizing pressure controller 102, turbine current limiter 101 includes turbine structure 103 and secondary speed controller 104, pressure Strong voltage stabilizing pressure controller 102 includes slow pressure storage stream cylinder 105 gentle pressure piston 106 and barostat 107, slow pressure storage stream cylinder 105 Top UNICOM circulating line 6, the bottom UNICOM barostat 107 of slow pressure storage stream cylinder 105, slow pressure piston 106 is arranged on slow pressure In storage stream cylinder 105；When in circulating line 6, the pressure of working medium or flow velocity change, turbine current limiter 101 can be by limiting whirlpool The rotation of wheel construction 103 and realize the restriction of flow velocity, part working medium pressure storage stream cylinder 105 of can postponing flows out or flows into and realizes body simultaneously Long-pending expansion or compression, thus realize stablizing the effect of pressure.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment 11 is tested, By selecting multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is according to life based on semi-conductor condensation The operation stability of thing heat of fermentation dynamical system is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, heat Can be about 9.8% by transformation efficiency, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 11.4%, temperature in fermentation vat When degree is about 58 DEG C, heat energy transformation efficiency is about 14%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 18%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 19.3%, based on semi-conductor condensation in the present embodiment ten The heat energy transformation efficiency of biofermentation dynamic system of heat energy than conventional thermal energy power machine, (conventional heat energy machine, at 40-60 DEG C Under low-temperature heat source, heat energy efficiency is the lowest, efficiency be less than 3%, heat energy is more difficult to be utilized) compare, the present embodiment based on quasiconductor The heat energy transformation efficiency higher than the heat energy transformation efficiency of conventional heat energy machine 10.6% of the biofermentation dynamic system of heat energy of condensation is left Right.
Embodiment 12 (as shown in figure 14): be with embodiment 11 difference: in order to increase turbine air inlet With the pressure reduction of air vent, the exhaust ports of described turbine 3 is additionally provided with precondenser 36.
Being further elaborated with as above-described embodiment, described precondenser 36 includes working medium conduction pipe 361 and condensation Endothermic tube 362, working medium conduction pipe 361 is used for connecting air vent and circulating line 6, and condensation endothermic tube 362 is used for absorbing working medium leads The heat of working medium in siphunculus 361, working medium conduction pipe 361 and condensation endothermic tube 362 spiral paratactic contact, in condensation endothermic tube 362 For heat recipient fluid, for increasing condensation efficiency, the flow direction of heat recipient fluid and the flow direction phase of working medium in working medium conduction pipe 361 Instead.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment 12 is tested, By selecting multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is according to life based on semi-conductor condensation The operation stability of thing heat of fermentation dynamical system is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, heat Can be about 10% by transformation efficiency, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 11.6%, temperature in fermentation vat When being about 58 DEG C, heat energy transformation efficiency is about 14.4%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 18%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 19.5%, based on semi-conductor condensation in the present embodiment ten The heat energy transformation efficiency of biofermentation dynamic system of heat energy than conventional thermal energy power machine, (conventional heat energy machine, at 40-60 DEG C Under low-temperature heat source, heat energy efficiency is the lowest, efficiency be less than 3%, heat energy is more difficult to be utilized) compare, the present embodiment based on quasiconductor The heat energy transformation efficiency of the biofermentation dynamic system of heat energy of condensation is higher by 11.4% than the heat energy transformation efficiency of conventional heat energy machine.
Embodiment 13 (as shown in figure 15): be with embodiment 12 difference: described condensation endothermic tube 362 uses Circulating line 6 between UNICOM's one-way hydraulic pump 9 and heat collector 1；Due to the circulation between one-way hydraulic pump 9 and heat collector Pipeline 6 needs heat absorption, and in working medium conduction pipe 361, working medium needs heat extraction, and this structure recycles circulating line 6 largely Interior working medium heat, increases thermal transition efficiency.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment 13 is tested, By selecting multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is according to life based on semi-conductor condensation The operation stability of thing heat of fermentation dynamical system is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, heat Can be about 10.2% by transformation efficiency, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 11.8%, temperature in fermentation vat When degree is about 58 DEG C, heat energy transformation efficiency is about 14.6%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about Being 18.1%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 19.5%；Based on quasiconductor in the present embodiment ten (conventional heat energy machine, at 40-60 than conventional thermal energy power machine for the heat energy transformation efficiency of the biofermentation dynamic system of heat energy of condensation DEG C low-temperature heat source under, heat energy efficiency is the lowest, and efficiency is less than 3%, and heat energy is more difficult to be utilized) compare, the present embodiment based on half The heat energy transformation efficiency of the biofermentation dynamic system of heat energy of conductor condensation is higher than the heat energy transformation efficiency of conventional heat energy machine 11.9%。
Embodiment 14 (as shown in figure 16): be with embodiment 13 difference: described condensing tube 51 becomes oblique type to divide Cloth.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment 14 is tested, By selecting multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is according to life based on semi-conductor condensation The operation stability of thing heat of fermentation dynamical system is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, heat Can be about 10.2% by transformation efficiency, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 12%, temperature in fermentation vat When being about 58 DEG C, heat energy transformation efficiency is about 14.8%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 18.4%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 19.5%, based on quasiconductor in the present embodiment 14 (conventional heat energy machine, at 40-60 than conventional thermal energy power machine for the heat energy transformation efficiency of the biofermentation dynamic system of heat energy of condensation DEG C low-temperature heat source under, heat energy efficiency is the lowest, and efficiency is less than 3%, and heat energy is more difficult to be utilized) compare, the present embodiment based on half The heat energy transformation efficiency of the biofermentation dynamic system of heat energy of conductor condensation is higher than the heat energy transformation efficiency of conventional heat energy machine 11.3%。
Embodiment 15 (as shown in figure 17): be with embodiment one difference: described condensing tube 51 becomes vertical distribution.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment 15 is tested, By selecting multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is according to life based on semi-conductor condensation The operation stability of thing heat of fermentation dynamical system is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, heat Can be about 10.2% by transformation efficiency, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 12%, temperature in fermentation vat When being about 58 DEG C, heat energy transformation efficiency is about 15%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 18.5%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 19.5%；Based on quasiconductor in the present embodiment 15 (conventional heat energy machine, at 40-60 than conventional thermal energy power machine for the heat energy transformation efficiency of the biofermentation dynamic system of heat energy of condensation DEG C low-temperature heat source under, heat energy efficiency is the lowest, and efficiency is less than 3%, and heat energy is more difficult to be utilized) compare, the present embodiment based on half The heat energy transformation efficiency of the biofermentation dynamic system of heat energy of conductor condensation is higher than the heat energy transformation efficiency of conventional heat energy machine 11.7%。
Embodiment 16 (as shown in figure 18): be with embodiment one difference: described condensing tube 51 becomes horizontal distribution Time, upper and lower layer condensing tube mutually staggers.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment 16 is tested, By selecting multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is according to life based on semi-conductor condensation The operation stability of thing heat of fermentation dynamical system is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, heat Can be about 10.2% by transformation efficiency, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 12%, temperature in fermentation vat When being about 58 DEG C, heat energy transformation efficiency is about 14.8%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 18.4%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 19.5%, based on quasiconductor in the present embodiment 16 (conventional heat energy machine, at 40-60 than conventional thermal energy power machine for the heat energy transformation efficiency of the biofermentation dynamic system of heat energy of condensation DEG C low-temperature heat source under, heat energy efficiency is the lowest, and efficiency is less than 3%, and heat energy is more difficult to be utilized) compare, the present embodiment based on half The heat energy transformation efficiency of the biofermentation dynamic system of heat energy of conductor condensation is higher than the heat energy transformation efficiency of conventional heat energy machine 13.3%。
Embodiment 17 (as shown in figure 19): be with embodiment 16 difference: in order to accelerate the liquefaction of working medium, institute Stating condensing unit 5 and also have additional a booster pump 53, booster pump 53 is arranged on condensing tube 51 middle-end.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment 17 is tested, By selecting multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is according to life based on semi-conductor condensation The operation stability of thing heat of fermentation dynamical system is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, heat Can be about 10.6% by transformation efficiency, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 12.6%, temperature in fermentation vat When degree is about 58 DEG C, heat energy transformation efficiency is about 16%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 18.9%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 19.5%；Based on quasiconductor in the present embodiment 17 (conventional heat energy machine, at 40-60 than conventional thermal energy power machine for the heat energy transformation efficiency of the biofermentation dynamic system of heat energy of condensation DEG C low-temperature heat source under, heat energy efficiency is the lowest, and efficiency is less than 3%, and heat energy is more difficult to be utilized) compare, the present embodiment based on half The heat energy transformation efficiency of the biofermentation dynamic system of heat energy of conductor condensation is higher than the heat energy transformation efficiency of conventional heat energy machine 12.8%。
Embodiment 18 (as shown in figure 20): be with embodiment 17 difference: in order to accelerate the liquefaction of working medium, subtract The thermal discharge of few condensation process, described condensing unit 5 also has additional multiple booster pump 53, and booster pump 53 is evenly distributed on condensing tube In 51；Described booster pump 53 uses turbocharging, multiple booster pumps 53 to be driven by same motor by power drive mechanism.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment 18 is tested, By selecting multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is according to life based on semi-conductor condensation The operation stability of thing heat of fermentation dynamical system is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, heat Can be about 10.8% by transformation efficiency, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 12.8%, temperature in fermentation vat When degree is about 58 DEG C, heat energy transformation efficiency is about 16.2%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about Being 19%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 19.5%, based on quasiconductor in the present embodiment 18 (conventional heat energy machine, at 40-60 than conventional thermal energy power machine for the heat energy transformation efficiency of the biofermentation dynamic system of heat energy of condensation DEG C low-temperature heat source under, heat energy efficiency is the lowest, and efficiency is less than 3%, and heat energy is more difficult to be utilized) compare, the present embodiment based on half The heat energy transformation efficiency of the biofermentation dynamic system of heat energy of conductor condensation is higher than the heat energy transformation efficiency of conventional heat energy machine 13.3%。
Embodiment 19: be with embodiment 18 difference: described cycle fluid 7 uses the freon of routine；Adopt With freon as working medium, can be used for the utilization of lower temperature thermal source, but owing to it needs the pressure in circulating line 6 higher, The processing technology of circulating line 6 and seal member is required higher by implementation process.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment 19 is tested, By selecting multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, heightens the pressure of working medium in condensing unit 5, heighten gasification simultaneously Sender matter pressure in device 2, in circulation pipe, refrigerant flow rate is according to the fortune of biofermentation dynamic system of heat energy based on semi-conductor condensation Line stabilization is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, and heat energy transformation efficiency is about 10%, fermentation When in pond, temperature is about 53 DEG C, heat energy transformation efficiency is about 12%, and when in fermentation vat, temperature is about 58 DEG C, heat energy converts effect Rate is about 14.8%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 18.4%, and in fermentation vat, temperature is 68 DEG C During left and right, heat energy transformation efficiency is about 19.5%, biofermentation of based on semi-conductor condensation thermal power system in the present embodiment 19 The heat energy transformation efficiency of system than conventional thermal energy power machine (conventional heat energy machine, under the low-temperature heat source of 40-60 DEG C, heat energy efficiency The lowest, efficiency is less than 3%, and heat energy is more difficult to be utilized) compare, the biofermentation heat energy based on semi-conductor condensation of the present embodiment The heat energy transformation efficiency of dynamical system is higher by 12.2% than the heat energy transformation efficiency of conventional heat energy machine.
Embodiment 20: be with embodiment 18 difference: described cycle fluid 7 uses methanol；This kind of working medium Boiling point at normal temperatures is 64.7 DEG C, easily gasifies, relatively low to the temperature requirement of high temperature heat source, can be used for the low temperature less than 100 DEG C Heat resource power generation, but belong to poisonous and harmful inflammable gas, high to the sealing requirements of circulating line.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment 20 is tested, By selecting multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is according to life based on semi-conductor condensation The operation stability of thing heat of fermentation dynamical system is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, heat Can be about 10.2% by transformation efficiency, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 12.2%, temperature in fermentation vat When degree is about 58 DEG C, heat energy transformation efficiency is about 15%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 18.5%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 19.5%；Based on quasiconductor in the present embodiment 20 (conventional heat energy machine, at 40-60 than conventional thermal energy power machine for the heat energy transformation efficiency of the biofermentation dynamic system of heat energy of condensation DEG C low-temperature heat source under, heat energy efficiency is the lowest, and efficiency is less than 3%, and heat energy is more difficult to be utilized) compare, the present embodiment based on half The heat energy transformation efficiency of the biofermentation dynamic system of heat energy of conductor condensation is higher than the heat energy transformation efficiency of conventional heat energy machine 12.7%。
Embodiment 21: be with embodiment 19 difference: described cycle fluid 7 uses ethanol；This kind of working medium Boiling point at normal temperatures be 78.15 DEG C, easily gasify incendivity, relatively low to the temperature requirement of high temperature heat source, can be used for little In the low temperature heat resource power generation of 100 DEG C, but high to the sealing requirements of circulating line.
By the biofermentation dynamic system of heat energy based on semi-conductor condensation in above-described embodiment 21 is carried out reality Test, by selecting multiple zymogenous bacteria classification, select different optimum fermentation temps；Its fermentation temperature be respectively 48 DEG C, 53 DEG C, 58 DEG C, 63 DEG C, 68 DEG C time, in the case of sink temperature is 15 DEG C, in circulation pipe, refrigerant flow rate is according to based on semi-conductor condensation The operation stability of biofermentation dynamic system of heat energy is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, Heat energy transformation efficiency is about 10.4%, and when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 12.4%, in fermentation vat When temperature is about 58 DEG C, heat energy transformation efficiency is about 15.5%, when in fermentation vat, temperature is about 63 DEG C, and heat energy transformation efficiency Being about 47%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 19.5%, based on half in the present embodiment 21 The heat energy transformation efficiency of the biofermentation dynamic system of heat energy of conductor condensation than conventional thermal energy power machine (conventional heat energy machine, Under the low-temperature heat source of 40-60 DEG C, heat energy efficiency is the lowest, and efficiency is less than 3%, and heat energy is more difficult to be utilized) compare, the present embodiment The heat energy transformation efficiency of biofermentation dynamic system of heat energy based on semi-conductor condensation is than the heat energy transformation efficiency of conventional heat energy machine High by 13.2%.
Finally it is noted that the foregoing is only the preferred embodiments of the present invention, it is not limited to the present invention, Although being described in detail the present invention with reference to previous embodiment, for a person skilled in the art, it still may be used So that the technical scheme described in foregoing embodiments to be modified, or wherein portion of techniques feature is carried out equivalent, All within the spirit and principles in the present invention, any modification, equivalent substitution and improvement etc. made, should be included in the present invention's Within protection domain.

Claims (10)

1. a biofermentation dynamic system of heat energy based on semi-conductor condensation, including heat collector (1), gasification installation (2), whirlpool Turbine (3), biofermentation pond (4), condensing unit (5), circulating line (6), cycle fluid (7) and one-way hydraulic pump (9), thermal-arrest It is real that device (1), gasification installation (2), turbine (3), condensing unit (5) and one-way hydraulic pump (9) pass sequentially through circulation pipe (6) road Now circulating UNICOM, circulating line (6) is contained within cycle fluid (7), it is characterized in that: described heat collector (1) and gasification installation (2) Being arranged in biofermentation pond (4), described condensing unit (5) is arranged on biofermentation pond (4) outward, and described heat collector (1) wraps Including thermal-collecting tube (11) and heat collecting sheet (12), heat collecting sheet (12) parallel interval is distributed, and thermal-collecting tube (11) fold-type is distributed in heat collecting sheet (12) in, gasification installation (2) includes gasify heat-absorbing chamber (21) and gasification pressure controller (22), and gasification pressure controller (22) is arranged on gasification In heat-absorbing chamber (21), gasification pressure controller (22) is for cycle fluid pressure control, and condensing unit (5) includes condensing tube (51) and heat emission fan (52), condensing tube (51) uniformly divides Multi-layers distributing, and condensing tube (51) mutually UNICOM, heat emission fan (52) is arranged on condensing tube (51) Side or lower section, heat emission fan (52) drives with convulsion mode or pressure wind mode, and described condensing tube (51) passes through thermo-electric generation sheet (511) Making, thermo-electric generation sheet (511) includes sheet metal (512), p-type semiconductor (513), n-type semiconductor (514), dielectric substrate layer And output electrode (516) (515), dielectric substrate layer (515) is uniformly interspersed with p-type semiconductor (513) and n-type semiconductor (514), Equally distributed p-type semiconductor (513) and n-type semiconductor (514) are connected by sheet metal (512), p-type semiconductor (513) and n The series connection end at the whole story of type quasiconductor (514) connects output electrode (516) respectively, between condensing unit (5) and gasification installation (2) also It is provided with contaminant filter pump (8).
Biofermentation dynamic system of heat energy based on semi-conductor condensation the most according to claim 1, is characterized in that: described temperature Output electrode (516) end of difference generating sheet (511) is connected with manostat (517), booster transformer (518) and accumulator in turn (519), accumulator (519) is used for heat emission fan (52), contaminant filter pump (8), the power supply of one-way hydraulic pump (9).
Biofermentation dynamic system of heat energy based on semi-conductor condensation the most according to claim 2, is characterized in that: described gas Change and be additionally provided with atomizing mouth (23) between heat-absorbing chamber (21) and thermal-collecting tube (11).
Biofermentation dynamic system of heat energy based on semi-conductor condensation the most according to claim 3, is characterized in that: described gas The horizontal cross-section changing heat-absorbing chamber (21) is that Rhizoma Nelumbinis is poroid.
Biofermentation dynamic system of heat energy based on semi-conductor condensation the most according to claim 3, is characterized in that: described gas The horizontal cross-section changing heat-absorbing chamber (21) is all poroid in honeycomb.
Biofermentation dynamic system of heat energy based on semi-conductor condensation the most according to claim 3, is characterized in that: described collection Backing (12) is in planar sheet.
Biofermentation dynamic system of heat energy based on semi-conductor condensation the most according to claim 3, is characterized in that: described collection Backing (12) lamellar in curved surface.
Biofermentation dynamic system of heat energy based on semi-conductor condensation the most according to claim 3, is characterized in that: described collection Backing (12) is in being in staggered distribution.
Biofermentation dynamic system of heat energy based on semi-conductor condensation the most according to claim 3, is characterized in that: described gas Changing heat-absorbing chamber (21) and be positioned at the upstream of biofermentation pond (4), heat collector (1) is positioned at the downstream of biofermentation pond (4).
Biofermentation dynamic system of heat energy based on semi-conductor condensation the most according to claim 1, is characterized in that: described Turbine (3) is any one in conventional steam turbine, multiple-stage steam turbine, tesla's turbine or radial outward flow turbine Kind.
CN201610760163.9A 2016-08-30 2016-08-30 A kind of biofermentation dynamic system of heat energy based on semi-conductor condensation Withdrawn CN106246273A (en)

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Application publication date: 20161221