CN106224025A - A kind of biofermentation dynamic system of heat energy based on centering type turbine - Google Patents

A kind of biofermentation dynamic system of heat energy based on centering type turbine Download PDF

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Publication number
CN106224025A
CN106224025A CN201610759066.8A CN201610759066A CN106224025A CN 106224025 A CN106224025 A CN 106224025A CN 201610759066 A CN201610759066 A CN 201610759066A CN 106224025 A CN106224025 A CN 106224025A
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heat energy
heat
biofermentation
turbine
centering type
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Chinese (zh)
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郭远军
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/16—Evaporating by spraying
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01C—ROTARY-PISTON OR OSCILLATING-PISTON MACHINES OR ENGINES
    • F01C1/00—Rotary-piston machines or engines
    • F01C1/30—Rotary-piston machines or engines having the characteristics covered by two or more groups F01C1/02, F01C1/08, F01C1/22, F01C1/24 or having the characteristics covered by one of these groups together with some other type of movement between co-operating members
    • F01C1/34—Rotary-piston machines or engines having the characteristics covered by two or more groups F01C1/02, F01C1/08, F01C1/22, F01C1/24 or having the characteristics covered by one of these groups together with some other type of movement between co-operating members having the movement defined in group F01C1/08 or F01C1/22 and relative reciprocation between the co-operating members
    • F01C1/344—Rotary-piston machines or engines having the characteristics covered by two or more groups F01C1/02, F01C1/08, F01C1/22, F01C1/24 or having the characteristics covered by one of these groups together with some other type of movement between co-operating members having the movement defined in group F01C1/08 or F01C1/22 and relative reciprocation between the co-operating members with vanes reciprocating with respect to the inner member
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K11/00—Plants characterised by the engines being structurally combined with boilers or condensers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K25/00—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
    • F01K25/08—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K25/00—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
    • F01K25/08—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours
    • F01K25/10—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours the vapours being cold, e.g. ammonia, carbon dioxide, ether
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28B—STEAM OR VAPOUR CONDENSERS
    • F28B1/00—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
    • F28B1/06—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using air or other gas as the cooling medium
    • H—ELECTRICITY
    • H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
    • H02N—ELECTRIC MACHINES NOT OTHERWISE PROVIDED FOR
    • H02N11/00—Generators or motors not provided for elsewhere; Alleged perpetua mobilia obtained by electric or magnetic means
    • H02N11/002—Generators

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

Abstract

The invention discloses a kind of biofermentation dynamic system of heat energy based on centering type turbine, including heat collector, gasification installation, turbine, condensing unit and one-way hydraulic pump pass sequentially through circulating line and realize circulation UNICOM, circulating line is contained within cycle fluid, heat collector and gasification installation is had to be arranged in biofermentation pond, condensing unit is arranged on outside biofermentation pond, centering type turbine includes turbine casing, revolving wormgear structure, air inlet and air vent, the rotating shaft of revolving wormgear structure is eccentrically mounted in turbine casing, air inlet and air vent are distributed in turbine casing radially opposite sides；The advantages such as it is high that biofermentation dynamic system of heat energy based on centering type turbine of the present invention has heat energy transformation efficiency, and turbine moment is big, power adjustable.

Description

A kind of biofermentation dynamic system of heat energy based on centering type turbine
Technical field
The invention belongs to utilization of energy apparatus field, a kind of biofermentation thermal power based on centering type turbine 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%, under the thermal source of 200 DEG C, Heat energy transformation efficiency average out to 18%；B. working medium gasification temperature is unstable, and working medium condensation effect is the best, and working medium is apt to deteriorate or goes out Existing impurity；C. the drive of turbine is little, and gasification working medium externally being done work, it is less to change into the efficiency of mechanical energy；D. secondary speed Instability, and stuck problem easily occurs；E. the Heat-collecting effect of heat collector is the best, and extraneous exhaust-heat absorption rate is little, and f. condenses dress The hot type amount put is relatively big, and thermal waste is big, slow by the condensation rate of natural condensation mode, and uses actively condensing mode (wind Machine is air-cooled or liquid pump water-cooled) need extra power consumption；G. existing equipment volume is bigger；F. turbine easily occurs leaking asking of working medium Topic.
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, increases the drive of turbine, improves turbine efficiency, stablizes working medium gasification temperature and refrigerant flow rate, improve working medium quality, Prevent working medium from going bad, improve turbine structure, it is to avoid turbine is revealed and rotary speed unstabilization, improve condensing unit, accelerate condensing rate； Existing for existing thermal hardware in the above-mentioned background technology of solution: heat energy transformation efficiency is low, working medium gasification temperature is unstable, work Matter condensation effect is the best, and working medium is apt to deteriorate or impurity occurs, and refrigerant leakage easily occurs in turbine, secondary speed is unstable, And easily occurring 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 centering type turbine Dynamic system of heat energy, including heat collector, gasification installation, centering type turbine, biofermentation pond, condensing unit, circulating line, Cycle fluid and one-way hydraulic pump, gasification installation, centering type turbine, condensing unit and one-way hydraulic pump pass sequentially through circulation pipe Road realizes circulation UNICOM, and 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, gasification control Depressor is used for cycle fluid blood pressure lowering；Heat source temperature, high-pressure liquid is reached after high-pressure liquid working medium fully heats in thermal-collecting tube Working medium flows into gasification heat-absorbing chamber, and the gasification pressure controller in gasification heat-absorbing chamber is controlled by pressure so that it is liquid refrigerant endothermic gasification, The blood pressure lowering acting in turbine of gasification working medium；This kind of structure, compared in thermal-collecting tube direct gasification, can be prevented effectively from gasification working medium In mix and have liquid refrigerant, working medium can be made to gasify evenly, described centering type turbine includes that turbine casing, revolving wormgear are tied Structure, air inlet, air vent and sealing bearing, revolving wormgear structure by seal bearing be arranged in turbine casing, air inlet and Air vent is distributed in turbine casing radially opposite sides, and described revolving wormgear structure includes moving vane and grooved rotating shaft, grooved rotating shaft Axial plane on groove is distributed, moving vane is movably arranged in the groove of grooved rotating shaft by spring, and grooved rotating shaft is by close Envelope bearing is eccentrically mounted in turbine casing, and air inlet is relatively near away from eccentric shaft, air vent away from eccentric shaft farther out, adjacent activities blade Between constitute chamber, communicate with air inlet for expansion chamber, communicate with air vent for discharge chamber；Both sides blade due to expansion chamber Area is different, and expansion chamber trends towards volume and becomes general orientation rotation, and the turbine of this kind of structure has bigger thrust, can be more abundant Ground utilizes kinetic energy and the potential energy of gasification working medium, has preferable heat energy transformation efficiency.
As optimizing explanation further, the moving vane of described revolving wormgear structure comprises at least three.
Optimizing as the most concrete, the exhaust ports of described centering type turbine is provided with precondenser；Take this knot Structure can increase the pressure reduction of air inlet and air vent, improves the transformation efficiency of turbine.
Optimizing as the most concrete, described precondenser includes working medium conduction pipe and condensation endothermic tube, working medium conduction pipe For connecting air vent and circulating line, condensation endothermic tube is for absorbing the heat of working medium conducting intraductal working medium, working medium conduction pipe With condensation endothermic tube spiral paratactic contact, it is heat recipient fluid in condensation endothermic tube, for increasing condensation efficiency, the flowing of heat recipient fluid Direction is contrary with the flow direction of working medium conducting intraductal working medium.
Optimizing as the most concrete, described condensation endothermic tube uses following between UNICOM's one-way hydraulic pump and heat collector Endless tube road；Owing to the circulating line between one-way hydraulic pump and heat collector needs heat absorption, and working medium conducting intraductal working medium needs Heat extraction, this structure recycles working medium heat in circulating line largely, increases thermal transition efficiency.
As the further optimization of such scheme, the gasification heat-absorbing chamber of gasification installation is Taper Pipe type cavity.
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 optimizing explanation further, between described condensing unit and heat collector, it is additionally provided with contaminant filter pump.
As optimizing explanation further, described condensing unit includes condensing tube and heat emission fan, and a condensing tube uniformly point multilamellar is divided Cloth, the mutual UNICOM of condensing tube, heat emission fan is arranged on above or below condensing tube, and heat emission fan is driven with convulsion mode or pressure wind mode Dynamic.
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 work between described centering type turbine and condensing unit Matter actuator, described working medium actuator includes turbine current limiter and pressure voltage stabilizing pressure controller, and turbine current limiter includes turbine structure With secondary speed controller, pressure voltage stabilizing pressure controller includes slow pressure storage stream cylinder gentle pressure piston and barostat, slow pressure storage stream The top UNICOM circulating line of cylinder, the bottom UNICOM barostat of slow pressure storage stream cylinder, slow pressure piston is arranged on slow pressure storage stream cylinder In；When in circulating line, the pressure of working medium or flow velocity change, turbine current limiter can be by limiting the rotation of turbine structure And realizing the restriction of flow velocity, part working medium can be postponed and be pressed storage stream cylinder to flow out or flow into expansion or the compression realizing volume simultaneously, from And realize stablizing the effect of pressure.
Operation principle: biofermentation dynamic system of heat energy based on centering type turbine 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 centering type turbine after working medium gasification, drives centering type rotating turbine, and centering type turbine drives electromotor simultaneously Rotate generating；After gasification working medium flows through centering type turbine, due to externally acting, its Temperature of Working and air pressure all can reduce, and Part working medium is caused to liquefy；After gasification working medium flows through centering type turbine, working medium flows to working medium actuator and condensing unit successively； Working medium actuator is for controlling the pressure of working medium, flow velocity in circulating line, and working medium actuator can be according to heat absorption district of the external world and heat release The temperature conditions in district, regulation working medium condensing temperature or gasification temperature, it is thus possible to be effectively improved heat energy transformation efficiency；Condensing unit Working medium can be liquefied completely；After liquefaction, working medium sequentially passes through contaminant filter pump and one-way hydraulic pump, and contaminant filter pump can be by working medium Out, working medium is carried out unidirectional pumping supercharging interior contaminant filter by one-way hydraulic pump；After liquefaction, working medium sequentially passes through contaminant filter pump After one-way hydraulic pump, and it is again introduced into gasification installation, completes a circulation.
Centering type turbine in biofermentation dynamic system of heat energy based on centering type turbine described in this invention, is importing During gases at high pressure, owing to the both sides blade area of its expansion chamber is different, expansion chamber trends towards volume and becomes general orientation rotation, this acting Process is static pressure acting, reveals without volume, has and promotes the feature that moment of torsion is big, air work transformation efficiency is high；Simultaneously as it is swollen Swollen chamber stress in rotation is more uniform, the conventional cylinder formula steam turbine of ratio, has power output evenly.
Beneficial effect: biofermentation dynamic system of heat energy based on centering type turbine of the present invention, the most existing skill Heat energy machine in art, has advantage and the progress of following several respects: 1. by using centering type turbine, can be largely Increase turbine turns power, and improves turbine efficiency, and has output power evenly；2. by setting up precondenser, Air inlet and the pressure reduction of air vent in centering type turbine can be increased, and the heat energy of working medium can be recycled, it is achieved to circulation industrial Heat absorption and the heat rejection process of matter difference section comprehensively utilize, and reduce thermal waste and cooling power consumption；3. by setting up impurity Filter pump and one-way hydraulic pump, can effectively prevent working medium rotten and more impurity occur, and preventing working medium from refluxing；4. pass through Condensing unit is set up booster pump, condensing rate can be improved largely, reduce condensation power consumption；5. by setting up working medium tune Joint device, pressure and flow to working medium are controlled, and can be effectively improved gasification usefulness and condensation efficiency, and stablize working medium gasification temperature Degree and refrigerant flow rate, prevent sealing member deformation bigger, it is to avoid secondary speed shakiness and working medium leakage problem；6. fully utilize life The heat energy of thing sweat, 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 is the biofermentation pool structure schematic diagram of the present invention program one；
Fig. 3 is the centering type turbine structure schematic diagram of the present invention program one；
Fig. 4 is the grooved pivot structure schematic diagram of the centering type turbine 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 installation structural representation of the present invention program one；
Fig. 7 is the condensing unit vertical cross section structural representation of the present invention program one；
Fig. 8 is the condensing unit 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 installation mounting connection structure schematic diagram of the present invention program four；
Figure 12 is the gasification installation mounting connection 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 unit vertical cross section structural representation of the present invention program ten；
Figure 18 is the condensing unit vertical cross section structural representation of the present invention program 11；
Figure 19 is the condensing unit vertical cross section structural representation of the present invention program 12；
Figure 20 is the Integral connection structure schematic diagram of the present invention program 13；
Figure 21 is the working medium controller structure schematic diagram of the present invention program 13；
Figure 22 is the condensing unit structural representation of the present invention program 14；
Figure 23 is the condensing unit structural representation of the present invention program 15；
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 it is centering type turbine, 31 is turbine casing, 32 is revolving wormgear structure, 321 is moving vane, 322 turns for grooved Axle, 323 be groove, 324 be spring, 33 air inlets, 34 be air vent, 35 for seal bearing, 36 be precondenser, 361 for work Matter conduction pipe, 362 for condensation endothermic tube, 331 be expansion chamber, 341 be discharge chamber；
4 is biological fermentation vat；
5 be condensing unit, 51 be condensing tube, 52 be heat emission fan, 53 be booster pump, 54 for catch box；
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 centering type turbine, including thermal-arrest Device 1, gasification installation 2, centering type turbine 3, biofermentation pond 4, condensing unit 5, circulating line 6, cycle fluid 7 and unidirectional Hydraulic pump 9, heat collector 1, gasification installation 2, centering type turbine 3, condensing unit 5 and one-way hydraulic pump 9 pass sequentially through circulation Pipeline 6 realizes circulation UNICOM, and 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；
(as shown in Figure 3, Figure 4) described centering type turbine 3 includes turbine casing 31, revolving wormgear structure 32, air inlet 33, row QI KOU 34 and sealing bearing 35, revolving wormgear structure 32 is arranged in turbine casing 31 by sealing bearing 35, air inlet 33 He Air vent 34 is distributed in turbine casing 31 radially opposite sides, and described revolving wormgear structure 32 includes moving vane 321 and grooved rotating shaft 322, groove 323 is distributed on the axial plane of grooved rotating shaft 322, moving vane 321 is movably arranged on grooved rotating shaft by spring 324 In the groove 323 of 322, grooved rotating shaft 322 is eccentrically mounted in turbine casing 31 by sealing bearing 35, and air inlet 33 is away from bias Axle is relatively near, and air vent 34 away from eccentric shaft farther out, constitutes chamber between adjacent activities blade 321, communicate with air inlet 33 for expanding Chamber 331, communicate with air vent 34 for discharge chamber 341；Owing to the both sides blade area of expansion chamber is different, expansion chamber trends towards body The long-pending general orientation that becomes rotates, and the turbine of this kind of structure has bigger thrust, can more fully hereinafter utilize gasification working medium kinetic energy and Potential energy, has preferable heat energy transformation efficiency.
Explanation, the moving vane of described revolving wormgear structure 32 is optimized further as the above-mentioned embodiment of this enforcement 321 comprise four.
Optimize explanation further, as the above-mentioned embodiment of this enforcement between described condensing unit 5 and heat collector 1 also It is provided with contaminant filter pump 8.
Optimize explanation further as the above-mentioned embodiment of this enforcement, (as shown in Figure 5) described gasification heat-absorbing chamber 21 by Multiple bodys are formed side by side.
As further illustrating of above-mentioned embodiment, (as shown in Figure 6) described gasification pressure controller 22 by with atmospheric pressure Strong holding amount pressure reduction realizes pressure control；
Optimizing explanation further as the above-mentioned embodiment of this enforcement, (as shown in Figure 7, Figure 8) described condensing unit 5 includes cold Solidifying pipe 51 and 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 condensing tube Above or below in the of 51, heat emission fan 52 drives with convulsion mode or pressure wind mode；Described condensing tube 51 is copper metal tube or alloy Metal tube, condensing tube 51 is in horizontal distribution.
Optimizing explanation further as the above-mentioned embodiment of this enforcement, condensing tube 51 tail end is provided with catch box 54.
Optimizing explanation further as the above-mentioned embodiment of this enforcement, condensing unit 5 is additionally provided with fin 55.
Optimizing explanation further as the above-mentioned embodiment of this enforcement, described cycle fluid 7 uses liquefied ammonia.
The centering type turbine of the present embodiment structure, owing to the both sides blade area of expansion chamber is different, expansion chamber trends towards Volume becomes general orientation and rotates, so that blade rotates；The vane stress of this kind of turbine is that gas-static is the poorest, and work distance Relatively big, compare the rotating vane turbine (produce pressure by fluid flowing to drive, namely gas-kinetic pressure is poor) of routine, have bigger Thrust, can more fully hereinafter utilize the gasification kinetic energy of working medium and potential energy, there is preferable heat energy transformation efficiency.
By the biofermentation dynamic system of heat energy based on centering type turbine 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 centering type turbine 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 5%, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 8%, and in fermentation vat, temperature is 58 DEG C of left sides Time right, heat energy transformation efficiency is about 10%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 11.6%, fermentation When in pond, temperature is about 68 DEG C, heat energy transformation efficiency is about 14%, by data are analyzed, the present embodiment based on partially (conventional heat energy machine, at 40-60 DEG C for the biofermentation dynamic system of heat energy of core type turbine and the heat energy transformation efficiency of conventional heat energy machine 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 bias The heat energy transformation efficiency of the biofermentation dynamic system of heat energy of formula turbine is higher by about 7% than the heat energy transformation efficiency of conventional heat energy machine； Meanwhile, the operation noise of the present embodiment biofermentation based on centering type turbine dynamic system of heat energy is little, good operation stability, with Time can realize power output regulation.
Embodiment two (as shown in Figure 9): be with embodiment one difference: the heat collecting sheet 12 of described heat collector 1 in Curved surface lamellar.
By the biofermentation dynamic system of heat energy based on centering type turbine 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 centering type turbine 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 5.5%, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 8.4%, and in fermentation vat, temperature is 58 Time about DEG C, heat energy transformation efficiency is about 10.2%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 12%, When in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 14.4%, by data are analyzed, and the present embodiment two Biofermentation dynamic system of heat energy based on centering type turbine and the heat energy transformation efficiency of conventional heat energy 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 Biofermentation dynamic system of heat energy based on centering type turbine heat energy transformation efficiency than conventional heat energy machine heat energy convert effect Rate is high by about 7.6%.
Embodiment three (as shown in Figure 10): be with embodiment one difference: the heat collecting sheet 12 of described heat collector 1 in It is in staggered distribution.
By the biofermentation dynamic system of heat energy based on centering type turbine 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 centering type turbine 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 5.5%, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 8.4%, and in fermentation vat, temperature is 58 Time about DEG C, heat energy transformation efficiency is about 10.2%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 12.2%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 15%, by data are analyzed, and this enforcement The biofermentation dynamic system of heat energy based on centering type turbine of example three and the heat energy transformation efficiency of conventional heat energy 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, this enforcement The heat energy transformation efficiency of the biofermentation dynamic system of heat energy based on centering type turbine of example converts than the heat energy of conventional heat energy machine Efficiency is high by about 7.8%.
Embodiment four (as shown in figure 11): be with embodiment one difference: described gasification pressure controller 22 includes pressure reduction Control valve 221 and gasification pressure induction apparatus 222, differential pressure control valve 221 is positioned at the front end of gasification heat-absorbing chamber 21, gasification pressure sensing Device 222 is 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 The pressure of working medium in gasification heat-absorbing chamber 21, when pressure is bigger, increases the pressure reduction of differential pressure control valve 221, when pressure is less, subtracts The pressure reduction of small pressure difference 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 centering type turbine 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 centering type turbine 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 10.6%, 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 16.2%, by data are analyzed, and the present embodiment four Biofermentation dynamic system of heat energy based on centering type turbine and the heat energy transformation efficiency of conventional heat energy 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 Biofermentation dynamic system of heat energy based on centering type turbine heat energy transformation efficiency than conventional heat energy machine heat energy convert effect Rate is high by about 6.8%.
Embodiment five (as shown in figure 12): be with embodiment four difference: gasification heat-absorbing chamber 21 and thermal-collecting tube 11 it Between be additionally provided with atomizing mouth 23；Atomizing mouth 23, for being atomized by the liquid refrigerant in thermal-collecting tube 11, sprays into gasification heat-absorbing chamber In 21.
Tested by the biofermentation dynamic system of heat energy based on centering type turbine 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 centering type turbine 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 7%, and 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 DEG C of left sides Time right, 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 13.6%, sends out When in ferment pond, temperature is about 68 DEG C, heat energy transformation efficiency is about 16.6%, by data are analyzed, the present embodiment five Biofermentation dynamic system of heat energy based on centering type turbine and the heat energy transformation efficiency of conventional heat energy 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 centering type turbine is than the heat energy transformation efficiency of conventional heat energy machine High by about 7%.
Embodiment six (as shown in figure 13): 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 centering type turbine 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 centering type turbine 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%, 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 During left and 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%, sends out When in ferment pond, temperature is about 68 DEG C, heat energy transformation efficiency is about 17.5%, by data are analyzed, the present embodiment six Biofermentation dynamic system of heat energy based on centering type turbine and the heat energy transformation efficiency of conventional heat energy 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 centering type turbine is than the heat energy transformation efficiency of conventional heat energy machine High by about 9%.
Embodiment seven (as shown in figure 14): 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 centering type turbine 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 centering type turbine 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%, 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 During left and right, heat energy transformation efficiency is about 12.4%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 15.5%, When in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 17.8%；By data are analyzed, the present embodiment seven Biofermentation dynamic system of heat energy based on centering type turbine and the heat energy transformation efficiency of conventional heat energy 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 Biofermentation dynamic system of heat energy based on centering type turbine heat energy transformation efficiency than conventional heat energy machine heat energy convert effect Rate is high by about 9.6%.
Embodiment eight (as shown in figure 15): be with embodiment seven difference: 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 described centering type turbine 3.
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 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 endothermic tube 362 spiral paratactic contact, condense endothermic tube 362 Interior is heat recipient fluid.
Being further elaborated with as above-described embodiment, for increasing 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 the biofermentation dynamic system of heat energy based on centering type turbine 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 centering type turbine 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 8.4%, 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%, by data are analyzed, and this enforcement The biofermentation dynamic system of heat energy based on centering type turbine of example eight and the heat energy transformation efficiency of conventional heat energy 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, this enforcement The heat energy transformation efficiency of the biofermentation dynamic system of heat energy based on centering type turbine of example eight turns than the heat energy of conventional heat energy machine Change efficiency high by about 9.4%.
Embodiment nine (such as Figure 16): be with embodiment eight difference: as described in condensation endothermic tube 362 use UNICOM unidirectional Circulating line 6 between hydraulic pump 9 and heat collector 1；Owing to the circulating line 6 between one-way hydraulic pump 9 and heat collector needs Absorbing heat, and in working medium conduction pipe 361, working medium needs heat extraction, this structure recycles working medium in circulating line 6 largely Heat, increases thermal transition efficiency.
By the biofermentation dynamic system of heat energy based on centering type turbine 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 centering type turbine 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 10.8%, and in fermentation vat, temperature is 58 Time about DEG C, heat energy transformation efficiency is about 13.4%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 17%, When in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 18%, by data are analyzed, the present embodiment nine Biofermentation dynamic system of heat energy based on centering type turbine and the heat energy transformation efficiency of conventional heat energy 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 nine Biofermentation dynamic system of heat energy based on centering type turbine heat energy transformation efficiency than conventional heat energy machine heat energy convert effect Rate is high by about 11%.
Embodiment ten (as shown in figure 17): be with embodiment nine difference: described condensing tube 51 becomes oblique type to be distributed.
By the biofermentation dynamic system of heat energy based on centering type turbine 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 centering type turbine 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 10.8%, and in fermentation vat, temperature is 58 Time about DEG C, heat energy transformation efficiency is about 13.4%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 17.2%%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 18.1%, by data are analyzed, and this reality Execute biofermentation dynamic system of heat energy based on centering type turbine and the heat energy transformation efficiency of conventional heat energy machine (the conventional heat of example ten 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, this reality The heat energy transformation efficiency of the biofermentation dynamic system of heat energy based on centering type turbine executing example turns than the heat energy of conventional heat energy machine Change efficiency high by about 11.2%.
Embodiment 11 (as shown in figure 18): be with embodiment nine difference: described condensing tube 51 becomes vertical distribution.
By the biofermentation dynamic system of heat energy based on centering type turbine 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 centering type turbine 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 8.7% by transformation efficiency, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 10.4%, temperature in fermentation vat When degree is about 58 DEG C, heat energy transformation efficiency is about 13.2%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about Being 17%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 18%, by data are analyzed, and this enforcement The biofermentation dynamic system of heat energy based on centering type turbine of example 11 and the heat energy transformation efficiency of conventional heat energy 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, this reality Execute the heat energy transformation efficiency of biofermentation dynamic system of heat energy based on centering type turbine of example eight than the heat energy of conventional heat energy machine Transformation efficiency is high by about 10.6%.
Embodiment 12 (as shown in figure 19): 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 centering type turbine 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 centering type turbine 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% by transformation efficiency, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 10.8%, temperature in fermentation vat When being about 58 DEG C, heat energy transformation efficiency is about 13.4%, and when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 17.2%%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 18.1%, by data are analyzed, and this reality The biofermentation dynamic system of heat energy based on centering type turbine executing example 12 is (conventional with the heat energy transformation efficiency of conventional heat energy machine 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, this The heat energy transformation efficiency of the biofermentation dynamic system of heat energy based on centering type turbine of embodiment is than the heat energy of conventional heat energy machine Transformation efficiency is high by about 11.2%.
Embodiment 13 (as shown in figs 20 and 21): be with embodiment 12 difference: centering type turbine 3 is with cold It is additionally provided with working medium actuator 10 between solidifying device 5；Described working medium actuator 10 includes turbine current limiter 101 and pressure voltage stabilizing control Depressor 102, turbine current limiter 101 includes that turbine structure 103 and secondary speed controller 104, pressure voltage stabilizing pressure controller 102 include Slow pressure storage stream cylinder 105 gentle pressure piston 106 and barostat 107, the top UNICOM circulating line 6 of slow pressure storage stream cylinder 105, slow The bottom UNICOM barostat 107 of pressure storage stream cylinder 105, slow pressure piston 106 is arranged in slow pressure storage stream cylinder 105；Work as circulation pipe When in road 6, the pressure of working medium or flow velocity change, turbine current limiter 101 can be by limiting the rotation of turbine structure 103 and reality The restriction of existing flow velocity, part working medium can be postponed and be pressed storage stream cylinder 105 to flow out or flow into expansion or the compression realizing volume simultaneously, thus Realize stablizing the effect of pressure.
By the biofermentation dynamic system of heat energy based on centering type turbine 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 centering type turbine 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 9.2% by transformation efficiency, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 11%, temperature in fermentation vat When being 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 17.5%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 18.4%, by data are analyzed, and this reality The biofermentation dynamic system of heat energy based on centering type turbine executing example 13 is (conventional with the heat energy transformation efficiency of conventional heat energy machine 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, this The heat energy transformation efficiency of the biofermentation dynamic system of heat energy based on centering type turbine of embodiment is than the heat energy of conventional heat energy machine Transformation efficiency is high by about 11.8%.
Embodiment 14 (as shown in figure 22): be with embodiment 13 difference: described condensing unit 5 also has additional One booster pump 53, booster pump 53 is arranged on condensing tube 51 middle-end；Take this structure, 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.
By the biofermentation dynamic system of heat energy based on centering type turbine 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 centering type turbine 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 11.6%, temperature in fermentation vat When degree is 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 Being 18%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 19%, by data are analyzed, and this enforcement The biofermentation dynamic system of heat energy based on centering type turbine of example 14 and the heat energy transformation efficiency of conventional heat energy 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, this reality The heat energy transformation efficiency of the biofermentation dynamic system of heat energy based on centering type turbine executing example turns than the heat energy of conventional heat energy machine Change efficiency high by about 11.8%.
Embodiment 15 (as shown in figure 23): be with embodiment 13 difference: described condensing unit 5 has additional many Individual booster pump 53, booster pump 53 is evenly distributed in condensing tube 51, states booster pump 53 and uses turbocharging, multiple booster pumps 53 to lead to Cross power drive mechanism to be driven by same motor；Take this 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.
By the biofermentation dynamic system of heat energy based on centering type turbine 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 centering type turbine 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 11.8%, temperature in fermentation vat When being 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 18%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 19.3%, by data are analyzed, and this enforcement The biofermentation dynamic system of heat energy based on centering type turbine of example 15 and the heat energy transformation efficiency of conventional heat energy 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, this reality The heat energy transformation efficiency of the biofermentation dynamic system of heat energy based on centering type turbine executing example turns than the heat energy of conventional heat energy machine Change efficiency high by 12.6%.
Embodiment 16: be with embodiment 15 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 centering type turbine 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, 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 centering type turbine Line stabilization is adjusted；Experiment effect is: when in fermentation vat, temperature is about 48 DEG C, and heat energy transformation efficiency is about 9.2%, sends out When in ferment pond, temperature is about 53 DEG C, heat energy transformation efficiency is about 10.8%, and when in fermentation vat, temperature is about 58 DEG C, heat energy turns Changing efficiency and be about 14%, when in fermentation vat, temperature is about 63 DEG C, heat energy transformation efficiency is about 17.8%, and in fermentation vat, temperature is 68 Time about DEG C, heat energy transformation efficiency is about 47%, by data are analyzed, the present embodiment 16 based on centering type turbine Biofermentation dynamic system of heat energy (conventional heat energy machine, at the Low Temperature Thermal of 40-60 DEG C with the heat energy transformation efficiency of conventional heat energy machine 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 centering type turbine The heat energy transformation efficiency of biofermentation dynamic system of heat energy is higher by about 11.8% than the heat energy transformation efficiency of conventional heat energy machine.
Embodiment 17: be with embodiment 15 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 centering type turbine 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 centering type turbine 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 9.4% by transformation efficiency, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 11%, 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%, by data are analyzed, and the present embodiment The biofermentation dynamic system of heat energy based on centering type turbine of 17 and the heat energy transformation efficiency of conventional heat energy 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, this enforcement The heat energy transformation efficiency of the biofermentation dynamic system of heat energy based on centering type turbine of example converts than the heat energy of conventional heat energy machine Efficiency is high by about 11.6%.
Embodiment 18: be with embodiment 15 difference: described cycle fluid 7 uses ethanol；This kind of working medium Boiling point at normal temperatures is 78.15 DEG C, and easily gasify incendivity, relatively low to the temperature requirement of high temperature heat source, can be used for being less than The low temperature heat resource power generation of 100 DEG C, but high to the sealing requirements of circulating line.
By the biofermentation dynamic system of heat energy based on centering type turbine 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 centering type turbine 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 9.4% by transformation efficiency, when in fermentation vat, temperature is about 53 DEG C, heat energy transformation efficiency is about 11.2%, temperature in fermentation vat When degree is 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 Being 18%, when in fermentation vat, temperature is about 68 DEG C, heat energy transformation efficiency is about 19%, by data are analyzed, and this enforcement The biofermentation dynamic system of heat energy based on centering type turbine of example 16 and the heat energy transformation efficiency of conventional heat energy 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, this reality The heat energy transformation efficiency of the biofermentation dynamic system of heat energy based on centering type turbine executing example turns than the heat energy of conventional heat energy machine Change efficiency high by about 11.7%.
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 centering type turbine, including heat collector (1), gasification installation (2), partially Core type 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 circulation Pipe (6) road realizes circulation UNICOM, and circulating line (6) is contained within cycle fluid (7), it is characterized in that: described heat collector (1) is gentle Gasifying device (2) is arranged in biofermentation pond (4), and described condensing unit (5) is arranged on biofermentation pond (4) outward, described thermal-arrest Device (1) includes thermal-collecting tube (11) and heat collecting sheet (12), and heat collecting sheet (12) parallel interval is distributed, and thermal-collecting tube (11) fold-type is distributed in In heat collecting sheet (12), gasification installation (2) includes gasify heat-absorbing chamber (21) and gasification pressure controller (22), and gasification pressure controller (22) is installed In gasification heat-absorbing chamber (21), gasification pressure controller (22) is for cycle fluid pressure control, and described centering type turbine (3) includes turbine Casing (31), revolving wormgear structure (32), air inlet (33), air vent (34) and sealing bearing (35), revolving wormgear structure (32) being arranged in turbine casing (31) by sealing bearing (35), air inlet (33) and air vent (34) are distributed in turbine casing (31) radially opposite sides, described revolving wormgear structure (32) includes moving vane (321) and grooved rotating shaft (322), grooved rotating shaft (322) groove (323) is distributed on axial plane, and moving vane (321) is movably arranged on grooved rotating shaft by spring (324) (322), in groove (323), grooved rotating shaft (322) is eccentrically mounted in turbine casing (31) by sealing bearing (35), air inlet Mouth (33) is relatively near away from eccentric shaft, and air vent (34) away from eccentric shaft farther out, constitutes chamber, with air inlet between adjacent activities blade (321) Mouthful (33) communicate for expansion chamber 331, communicate with air vent (34) for discharge chamber (341).
Biofermentation dynamic system of heat energy based on centering type turbine the most according to claim 1, is characterized in that: described rotation The moving vane (321) of rotating turbine structure (32) comprises at least three.
Biofermentation dynamic system of heat energy based on centering type turbine 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 centering type turbine 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 centering type turbine 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 centering type turbine 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 centering type turbine 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 centering type turbine 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 centering type turbine 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 centering type turbine the most according to claim 1, is characterized in that: condensation Device (5) includes condensing tube (51) and heat emission fan (52), and condensing tube (51) uniformly divides Multi-layers distributing, condensing tube (51) to interconnect mutually Logical, heat emission fan (52) is arranged on above or below condensing tube (51), and heat emission fan (52) drives with convulsion mode or pressure wind mode.
CN201610759066.8A 2016-08-30 2016-08-30 A kind of biofermentation dynamic system of heat energy based on centering type turbine Withdrawn CN106224025A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111248295A (en) * 2020-02-20 2020-06-09 北京嘉瑞富德食品科技有限公司 Production process of quark sweet food and stirring device thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111248295A (en) * 2020-02-20 2020-06-09 北京嘉瑞富德食品科技有限公司 Production process of quark sweet food and stirring device thereof

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Application publication date: 20161214