CN106246259A - A kind of oil field based on semi-conductor condensation heat energy from waste gas dynamical system - Google Patents

A kind of oil field based on semi-conductor condensation heat energy from waste gas dynamical system Download PDF

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CN106246259A
CN106246259A CN201610760100.3A CN201610760100A CN106246259A CN 106246259 A CN106246259 A CN 106246259A CN 201610760100 A CN201610760100 A CN 201610760100A CN 106246259 A CN106246259 A CN 106246259A
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China
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waste gas
oil field
heat energy
semi
transformation efficiency
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郭远军
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K11/00—Plants characterised by the engines being structurally combined with boilers or condensers
    • F01K11/02—Plants characterised by the engines being structurally combined with boilers or condensers the engines being turbines
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K27/00—Plants for converting heat or fluid energy into mechanical energy, not otherwise provided for
    • F01K27/02—Plants modified to use their waste heat, other than that of exhaust, e.g. engine-friction heat

Abstract

The invention discloses a kind of oil field based on semi-conductor condensation heat energy from waste gas dynamical system, pass sequentially through circulating line including gasification installation, turbine, condensing unit and one-way hydraulic pump and realize circulation UNICOM, circulating line is contained within cycle fluid, heat collector is installed outside gasification installation, heat collector is linked with oil field waste gas burner, oil field waste gas burner includes waste gas inlet, oil field waste gas air-introduced machine, waste gas burning room, persistently leads firearm and steam discharge pipe, condensing unit includes condensing tube and heat emission fan, and condensing tube is made by thermo-electric generation sheet；Oil field based on semi-conductor condensation of the present invention heat energy from waste gas dynamical system has condensing rate faster, can reduce condensation row's energy, improve heat energy transformation efficiency, and stable, power adjustable.

Description

A kind of oil field based on semi-conductor condensation heat energy from waste gas dynamical system
Technical field
The invention belongs to utilization of energy apparatus field, a kind of oil field based on semi-conductor condensation heat energy from waste gas power 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.
On the other hand, in oil extraction process, oil well has a large amount of oil field waste gas containing methane and discharges, in order to prevent stone In oil waste gas, methane is discharged to the external world, ozone layer shines into pollution, and prevents the methane gas gathering of oilfield exploitation areas adjacent from containing Measuring too high initiation to explode, widespread practice is to arrange waste gas burner at oil well mouth, is fallen by incendivity gas firing in its waste gas, This processing mode causes bigger energy waste.
For above-mentioned energy waste problem, oil field, minority part land can use oil gas reclaimer by the waste gas of oil field Oil gas reclaim, but existing oil gas reclaimer requires to take up room big, installs more complicated, and running energy consumption Greatly, offshore oilfield is suitable for hardly.
Summary of the invention
The purpose that the present invention is to be realized is: comprehensive utilization oil field waste gas, reduces energy waste and environmental pollution, reduces The hot type amount of thermal hardware and thermal waste, improve heat energy transformation efficiency, stablize working medium gasification temperature and refrigerant flow rate, improve work Matter quality, prevents working medium from going bad, improves turbine structure, it is to avoid turbine is revealed and rotary speed unstabilization, improve condensing unit, add rapid cooling Solidifying speed；Existing for existing thermal hardware in the above-mentioned background technology of solution: waste gas energy waste in oil field is big, pollutes environment, The heat energy transformation efficiency of thermal hardware is low, and 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, easily there is refrigerant leakage in turbine, and secondary speed is unstable and easily occurs stuck, the heat energy of condensing unit Waste is big, condensing rate is 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 oil field based on semi-conductor condensation waste gas Dynamic system of heat energy, including heat collector, gasification installation, turbine, oil field waste gas burner, condensing unit, circulating line, Cycle fluid and one-way hydraulic pump, 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, and heat collector is arranged on outside gasification installation, working medium in gasification installation Biomass gasification boiler；
It is characterized in that: described oil field waste gas burner includes waste gas inlet, oil field waste gas air-introduced machine, waste gas burning room, holds Continue and lead firearm and steam discharge pipe, waste gas inlet, waste gas burning room and steam discharge pipe UNICOM successively, oil field waste gas air-introduced machine Being arranged on waste gas inlet, persistently lead firearm and be arranged on waste gas burning indoor, described firearm of persistently leading is continuous discharge spark plug Or heated filament net, steam discharge pipe is connected to heat collector；
Condensing unit includes condensing tube and heat emission fan, and condensing tube uniformly divides Multi-layers distributing, the mutual UNICOM of condensing tube, and heat emission fan is installed 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 system Becoming, thermo-electric generation sheet includes sheet metal, p-type semiconductor, n-type semiconductor, dielectric substrate layer and output electrode, and dielectric substrate layer is equal Even p-type semiconductor and the n-type semiconductor of being interspersed with, equally distributed p-type semiconductor and n-type semiconductor connected by sheet metal, p Type quasiconductor is connected output electrode respectively with the series connection end at the whole story of n-type semiconductor.
As optimizing further, between gasification installation and condensing unit, 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 optimizing further, heat collector includes upper cover and lower cover, offers heating gate, upper cover and lower cover position respectively in the middle part of lower cover Being heat collector cavity between upper and lower, upper cover and lower cover, the upper cover lower part of heat collector is furnished with multilamellar upper cover and dashes forward ring, heat collector Lower cover upper part be furnished with multilamellar lower cover and dash forward ring, upper cover ring and lower cover ring of dashing forward of dashing forward staggers, and gasification installation is positioned at heat collector cavity.
As the further optimization of such scheme, gasification installation includes gasification chamber, and gasification chamber is working medium reality in gasification installation The cavity now gasified, gasification installation is positioned at heat collector cavity, and gasification chamber is tapered cavity.
As the further optimization of such scheme, described gasification installation also includes preheating cavity, and preheating cavity is connected with gasification chamber Logical, preheating cavity is positioned at gasification chamber front end, and preheating cavity is for the preheating of working medium.
As the further optimization of such scheme, described preheating cavity is spiral cast cavity, and gasification chamber is spherical cavity.
As the further optimization of such scheme, between described preheating cavity and gasification chamber, it is additionally provided with atomizing mouth, atomizing mouth For the liquid refrigerant in preheating cavity is atomized, spray in gasification chamber.
As the further optimization of such scheme, described gasification chamber is ellipse cavity.
As the further optimization of such scheme, described gasification chamber becomes tapered, and the horizontal cross-section of gasification chamber is that Rhizoma Nelumbinis is poroid.
As the further optimization of such scheme, described gasification chamber becomes polygon tapered, and the horizontal cross-section of gasification chamber is all in honeybee Socket bore shape.
As the further optimization of such scheme, described preheating cavity is spirally coiled in heat collector periphery, for absorbing sets The used heat of thermal periphery.
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 can use UNICOM's one-way hydraulic pump and gas Circulating line between gasifying device；Owing to the circulating line between one-way hydraulic pump and gasification installation needs heat absorption, and working medium is led Logical intraductal 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 pure water.
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 propanol or 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: oil field based on semi-conductor condensation heat energy from waste gas dynamical system described in this invention, during work, gasification dress Cycle fluid in putting flows to turbine from heat collector cavity endothermic gasification, gasification working medium, drives rotating turbine, simultaneously turbine band Dynamic generator rotation generating；After gasification working medium flows through turbine, due to externally acting, its Temperature of Working 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 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 zone Temperature conditions, regulation working medium condensing temperature or gasification temperature, it is thus possible to be effectively improved heat energy transformation efficiency；Condensing unit can be by Working medium liquefies completely；After liquefaction, working medium sequentially passes through contaminant filter pump and one-way hydraulic pump, and contaminant filter pump can be by miscellaneous in working medium Matter filters out, and working medium is carried out unidirectional pumping supercharging by one-way hydraulic pump；After liquefaction, working medium sequentially passes through contaminant filter pump and list After hydraulic pump, and it is again introduced into gasification installation, completes a circulation.
Condensing tube in oil field based on semi-conductor condensation heat energy from waste gas dynamical system 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: oil field based on semi-conductor condensation of the present invention heat energy from waste gas dynamical system, 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 fuel gas of oil field waste gas, reduce energy waste, and reduce oil field waste gas environmental pollution.
Accompanying drawing explanation
Fig. 1 is the Integral connection structure schematic diagram of the present invention program one；
Fig. 2 is the oil field waste gas burner structural representation of the present invention program one；
Fig. 3 is the condensing unit attachment structure schematic diagram of the present invention program one；
Fig. 4 is the condensing tube tube wall Structure of cross section schematic diagram of the present invention program one；
Fig. 5 is the gasification installation 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 installation mounting connection structure schematic diagram of the present invention program four；
Fig. 9 is the gasification installation mounting connection structure schematic diagram of the present invention program five；
Figure 10 is the gasification chamber cross section structure schematic diagram of the present invention program six；
Figure 11 is the gasification 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 for heat collector, 11 for upper cover, 111 for upper cover dash forward ring, 12 for lower cover, 121 for lower cover dash forward ring, 13 heating gates, 14 be collect Hot chamber；
2 be gasification installation, 21 be gasification chamber, 22 be preheating cavity, 23 for atomizing mouth；
3 be turbine, 36 for precondenser, 361 for working medium conduction pipe, 362 for condensation endothermic tube；
4 it is oil field waste gas burner, 41 is waste gas inlet, 42 is oil field waste gas air-introduced machine, 43 is waste gas burning room, 44 is Persistently lead firearm, 45 for steam discharge pipe；
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 oil field based on semi-conductor condensation heat energy from waste gas dynamical system, including thermal-arrest Device 1, gasification installation 2, turbine 3, oil field waste gas burner 4, condensing unit 5, circulating line 6, cycle fluid 7 and unidirectional Hydraulic pump 9, gasification installation 2, turbine 3, condensing unit 5 and one-way hydraulic pump 9 pass sequentially through circulating line 6 and realize circulation connection Logical, circulating line 6 is contained within cycle fluid 7, and it is outside that heat collector 1 is arranged on gasification installation 2, working medium in gasification installation 2 Biomass gasification boiler；
(as shown in Figure 2) oil field waste gas burner 4 includes waste gas inlet 41, oil field waste gas air-introduced machine 42, waste gas burning room 43, firearm 44 and steam discharge pipe 45, air inlet 41, waste gas burning room 43 and steam discharge pipe 45 UNICOM successively, oil are persistently led Field waste gas air-introduced machine 42 is arranged on air inlet 41, persistently leads firearm 44 and is arranged in waste gas burning room 43, described persistently leads firearm 44 is continuous discharge spark plug or heated filament net, steam discharge pipe 45 UNICOM
To heat collector 1；
(as shown in Figure 3) described condensing unit 5 includes condensing tube 51 and heat emission fan 52, and condensing tube 51 uniformly divides Multi-layers distributing, cold The solidifying mutual UNICOM of pipe 51, heat emission fan 52 is arranged on above or below condensing tube 51, and heat emission fan 52 is with convulsion mode or pressure wind mode Drive；
(as shown in Figure 4) described condensing tube 51 is made by thermo-electric generation sheet 511, and 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 worn Being inserted with p-type semiconductor 513 and n-type semiconductor 514, equally distributed p-type semiconductor 513 and n-type semiconductor 514 pass through sheet metal 512 series connection, p-type semiconductor 513 is connected output electrode 516 respectively with the series connection end at the whole story of n-type semiconductor 514；Thermo-electric generation sheet Output electrode 516 voltage of 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 gasification installation 2 and condensing unit 5, it is additionally provided with impurity Filter pump 8.
As further illustrating of above-mentioned embodiment, (as shown in Figure 5) described gasification installation 2 includes gasification chamber 21, gas Changing chamber 21 be that working medium is realizing the cavity that gasifies in gasification installation 2, and gasification installation 2 is positioned at heat collector cavity 14, and gasification chamber 21 is in cone Type cavity.
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 pure water.
By oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment one is tested, to Oil field waste gas burner 4 introduces oil field waste gas, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is according to oil field based on semi-conductor condensation heat energy from waste gas power The operation stability of system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat energy Transformation efficiency is about 19%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 22%, oil field Ignition temperature in waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 27%, the combustion in oil field waste gas burner 4 Burning temperature is 250 DEG C, and heat energy transformation efficiency is about 32%, when the ignition temperature in oil field waste gas burner 4 is about 300 DEG C, Heat energy transformation efficiency is about 38%, and when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy transformation efficiency is about It is 44%；In the present embodiment one, the heat energy transformation efficiency of oil field based on semi-conductor condensation heat energy from waste gas dynamical system is than routine Thermal energy power machine (when 200 DEG C, average out to 18%) is compared, oil field based on the semi-conductor condensation heat energy from waste gas power of the present embodiment The energy transformation efficiency of system is higher by 9% than the heat energy transformation efficiency of conventional heat energy machine, and it is about 50% that efficiency improves ratio；Meanwhile, originally Embodiment oil field based on semi-conductor condensation heat energy from waste gas dynamical system cooldown rate is fast, and hot driving is little, runs noise little, runs Good stability, can realize power output regulation simultaneously.
Embodiment two (as shown in Fig. 6): be with embodiment one difference: heat collector 1 includes upper cover 11 and lower cover 12, offer heating gate 13, upper cover 11 and lower cover 12 in the middle part of lower cover 12 and lay respectively at upper and lower, for collection between upper cover 11 and lower cover 12 Hot chamber 14, upper cover 11 lower part of heat collector 1 is furnished with two-layer upper cover and dashes forward ring 111, and lower cover 12 upper part of heat collector 1 is furnished with Two-layer lower cover is dashed forward ring 121, and upper cover ring 111 and lower cover ring 121 of dashing forward of dashing forward staggers.
By oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment two is tested, to Oil field waste gas burner 4 introduces oil field waste gas, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is according to oil field based on semi-conductor condensation heat energy from waste gas power The operation stability of system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat energy Transformation efficiency is about 19.5%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 23%, oil Ignition temperature in field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 28%, in oil field waste gas burner 4 Ignition temperature is 250 DEG C, and heat energy transformation efficiency is about 33%, and the ignition temperature in oil field waste gas burner 4 is about 300 DEG C Time, heat energy transformation efficiency is about 39%, and when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy converts effect Rate is about 45%；In the present embodiment two, the heat energy transformation efficiency of oil field based on semi-conductor condensation heat energy from waste gas dynamical system is than often The thermal energy power machine (when 200 DEG C, average out to 18%) of rule is compared, oil field based on the semi-conductor condensation heat energy from waste gas of the present embodiment The energy transformation efficiency of dynamical system is higher by 9.8% than the heat energy transformation efficiency of conventional heat energy machine, and it is about 54% that efficiency improves ratio.
Embodiment three (shown in Fig. 7): be with embodiment one difference: as described in upper cover 11 bottom of heat collector 1 Three layer upper cover being distributed dash forward ring 111, lower cover 12 upper part of heat collector 1 is furnished with three layers of lower cover and dashes forward ring 121, and upper cover is dashed forward ring 111 Stagger with lower cover ring 121 of dashing forward.
By oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment three is tested, to Oil field waste gas burner 4 introduces oil field waste gas, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is according to oil field based on semi-conductor condensation heat energy from waste gas power The operation stability of system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat energy Transformation efficiency is about 19.5%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 23.5%, Ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 28.5%, oil field waste gas burner 4 Interior ignition temperature is 250 DEG C, and heat energy transformation efficiency is about 33.5%, and the ignition temperature in oil field waste gas burner 4 is 300 Time about DEG C, heat energy transformation efficiency is about 39.5%, when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, and heat 45.5% can be about by transformation efficiency；In the present embodiment three, the heat energy of oil field based on semi-conductor condensation heat energy from waste gas dynamical system turns Change efficiency to compare than conventional thermal energy power machine (when 200 DEG C, average out to 18%), the oil based on semi-conductor condensation of the present embodiment The energy transformation efficiency of field heat energy from waste gas dynamical system is higher by 10.2% than the heat energy transformation efficiency of conventional heat energy machine, and efficiency improves ratio It is about 56%.
Embodiment four (as shown in Figure 8): be with embodiment one difference: described gasification installation 2 also includes preheating cavity 22, preheating cavity 22 is connected with gasification chamber 21, and preheating cavity 22 is positioned at gasification chamber 21 front end, and preheating cavity 22 is for the preheating of working medium.
Optimizing explanation further as above-described embodiment, described preheating cavity 22 is spiral cast cavity, and gasification chamber 21 is Spherical cavity.
As the further optimization of such scheme, described preheating cavity 22 is spirally coiled in heat collector 1 periphery, is used for absorbing The used heat of heat collector 1 periphery.
By oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment four is tested, to Oil field waste gas burner 4 introduces oil field waste gas, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is according to oil field based on semi-conductor condensation heat energy from waste gas power The operation stability of system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat energy Transformation efficiency is about 20%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 24%, oil field Ignition temperature in waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 29%, the combustion in oil field waste gas burner 4 Burning temperature is 250 DEG C, and heat energy transformation efficiency is about 35%, when the ignition temperature in oil field waste gas burner 4 is about 300 DEG C, Heat energy transformation efficiency is about 41%, and when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy transformation efficiency is about It is 47%；In the present embodiment four, the heat energy transformation efficiency of oil field based on semi-conductor condensation heat energy from waste gas dynamical system is than routine Thermal energy power machine (when 200 DEG C, average out to 18%) is compared, oil field based on the semi-conductor condensation heat energy from waste gas power of the present embodiment The energy transformation efficiency of system is higher by 11.5% than the heat energy transformation efficiency of conventional heat energy machine, and it is about 64% that efficiency improves ratio.
Embodiment five (as shown in Figure 9): and embodiment four difference is: between described preheating cavity 22 and gasification chamber 21 Being additionally provided with atomizing mouth 23, atomizing mouth 23, for being atomized by the liquid refrigerant in preheating cavity 22, sprays in gasification chamber 21.
Optimizing explanation further as above-described embodiment, described gasification chamber 21 is ellipse cavity.
Tested, to oil field by oil field based on the semi-conductor condensation heat energy from waste gas dynamical system of above-described embodiment five Waste gas burner 4 introduces oil field waste gas, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is according to oil field based on semi-conductor condensation heat energy from waste gas dynamical system Operation stability be adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, and heat energy converts Efficiency is about 21%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 25%, oil field waste gas Ignition temperature in burner 4 is 200 DEG C, and heat energy transformation efficiency is about 30%, the burning temperature in oil field waste gas burner 4 Degree is 250 DEG C, and heat energy transformation efficiency is about 37%, when the ignition temperature in oil field waste gas burner 4 is about 300 DEG C, heat energy Transformation efficiency is about 43%, and when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy transformation efficiency is about 49%；In the present embodiment five, the heat energy transformation efficiency of oil field based on semi-conductor condensation heat energy from waste gas dynamical system is than conventional warm Motility machine (when 200 DEG C, average out to 18%) is compared, oil field based on the semi-conductor condensation heat energy from waste gas dynamical system of the present embodiment The energy transformation efficiency of system is higher by 13% than the heat energy transformation efficiency of conventional heat energy machine, and it is about 72% that efficiency improves ratio.
Embodiment six (as shown in Figure 10): be with embodiment five difference: described gasification chamber 21 becomes tapered, gasification chamber The horizontal cross-section of 21 is that Rhizoma Nelumbinis is poroid.
By oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment six is tested, to Oil field waste gas burner 4 introduces oil field waste gas, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is according to oil field based on semi-conductor condensation heat energy from waste gas power The operation stability of system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat energy Transformation efficiency is about 22%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 26%, oil field Ignition temperature in waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 32%, the combustion in oil field waste gas burner 4 Burning temperature is 250 DEG C, and heat energy transformation efficiency is about 39%, when the ignition temperature in oil field waste gas burner 4 is about 300 DEG C, Heat energy transformation efficiency is about 44%, and when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy transformation efficiency is about It is 50%；In the present embodiment six, the heat energy transformation efficiency of oil field based on semi-conductor condensation heat energy from waste gas dynamical system is than routine Thermal energy power machine (when 200 DEG C, average out to 18%) is compared, oil field based on the semi-conductor condensation heat energy from waste gas power of the present embodiment The energy transformation efficiency of system is higher by 14.3% than the heat energy transformation efficiency of conventional heat energy machine, and it is about 79.5% that efficiency improves ratio.
Embodiment seven (as shown in figure 11): be that described gasification chamber 21 becomes polygon tapered, in advance with embodiment five difference The horizontal cross-section of hot chamber 22 and gasification chamber 21 is all poroid in honeycomb.
By oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment seven is tested, to Oil field waste gas burner 4 introduces oil field waste gas, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is according to oil field based on semi-conductor condensation heat energy from waste gas power The operation stability of system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat energy Transformation efficiency is about 22.5%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 26.5%, Ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 32.5%, oil field waste gas burner 4 Interior ignition temperature is 250 DEG C, and heat energy transformation efficiency is about 40%, and the ignition temperature in oil field waste gas burner 4 is 300 DEG C During left and right, heat energy transformation efficiency is about 45%, and when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy turns Change efficiency and be about 51%；The heat energy transformation efficiency of oil field based on semi-conductor condensation heat energy from waste gas dynamical system in the present embodiment seven Compare than conventional thermal energy power machine (when 200 DEG C, average out to 18%), oil field based on the semi-conductor condensation waste gas of the present embodiment The energy transformation efficiency of dynamic system of heat energy is higher by 15% than the heat energy transformation efficiency of conventional heat energy machine, and it is 83.3% left side that efficiency improves ratio Right.
Embodiment eight: be with embodiment seven difference: described turbine 3 is the steamturbine comprising multistage blade Machine.
By oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment eight is tested, to Oil field waste gas burner 4 introduces oil field waste gas, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is according to oil field based on semi-conductor condensation heat energy from waste gas power The operation stability of system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat energy Transformation efficiency is about 24%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 28%, oil field Ignition temperature in waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 34%, the combustion in oil field waste gas burner 4 Burning temperature is 250 DEG C, and heat energy transformation efficiency is about 42%, when the ignition temperature in oil field waste gas burner 4 is about 300 DEG C, Heat energy transformation efficiency is about 47%, and when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy transformation efficiency is about It is 53%；In the present embodiment eight, the heat energy transformation efficiency of oil field based on semi-conductor condensation heat energy from waste gas dynamical system is than routine Thermal energy power machine (when 200 DEG C, average out to 18%) is compared, oil field based on the semi-conductor condensation heat energy from waste gas power of the present embodiment The energy transformation efficiency of system is higher by 16.8% than the heat energy transformation efficiency of conventional heat energy machine, and it is about 93.3% that efficiency improves ratio.
Embodiment nine: be with embodiment seven difference: described turbine 3 is tesla's turbine.
By oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment nine is tested, to Oil field waste gas burner 4 introduces oil field waste gas, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is according to oil field based on semi-conductor condensation heat energy from waste gas power The operation stability of system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat energy Transformation efficiency is about 24.5%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 28.5%, Ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 34.5%, oil field waste gas burner 4 Interior ignition temperature is 250 DEG C, and heat energy transformation efficiency is about 42.5%, and the ignition temperature in oil field waste gas burner 4 is 300 Time about DEG C, heat energy transformation efficiency is about 48%, when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy Transformation efficiency is about 54%；In the present embodiment nine, the heat energy of oil field based on semi-conductor condensation heat energy from waste gas dynamical system converts effect Rate is compared than conventional thermal energy power machine (when 200 DEG C, average out to 18%), gives up in the oil field based on semi-conductor condensation of the present embodiment The energy transformation efficiency of gas dynamic system of heat energy is higher by 17.4% than the heat energy transformation efficiency of conventional heat energy machine, and efficiency improves ratio and is About 96.5%.
Embodiment ten: be with embodiment one difference: described turbine 3 is radial outward flow turbine.
By oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment ten is tested, to Oil field waste gas burner 4 introduces oil field waste gas, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is according to oil field based on semi-conductor condensation heat energy from waste gas power The operation stability of system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat energy Transformation efficiency is about 24%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 28%, oil field Ignition temperature in waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 34%, the combustion in oil field waste gas burner 4 Burning temperature is 250 DEG C, and heat energy transformation efficiency is about 42.5%, and the ignition temperature in oil field waste gas burner 4 is about 300 DEG C Time, heat energy transformation efficiency is about 47.5%, and when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy converts Efficiency is about 53%；The heat energy transformation efficiency ratio of oil field based on semi-conductor condensation heat energy from waste gas dynamical system in the present embodiment ten Conventional thermal energy power machine (when 200 DEG C, average out to 18%) is compared, oil field based on the semi-conductor condensation waste gas heat of the present embodiment The energy transformation efficiency of motility system is higher by 17% than the heat energy transformation efficiency of conventional heat energy machine, and it is 94.5% left side that efficiency improves ratio 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 oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment 11 is tested, Introduce oil field waste gas to oil field waste gas burner 4, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is active according to oil field based on semi-conductor condensation waste gas heat The operation stability of Force system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat Can be about 24.5% by transformation efficiency, the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 28.5%, the ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 35%, and oil field waste gas burning fills Putting the ignition temperature in 4 is 250 DEG C, and heat energy transformation efficiency is about 44%, and the ignition temperature in oil field waste gas burner 4 is 300 Time about DEG C, heat energy transformation efficiency is about 49%, when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy Transformation efficiency is about 54%；In the present embodiment ten, the heat energy of oil field based on semi-conductor condensation heat energy from waste gas dynamical system converts effect Rate is compared than conventional thermal energy power machine (when 200 DEG C, average out to 18%), gives up in the oil field based on semi-conductor condensation of the present embodiment The energy transformation efficiency of gas dynamic system of heat energy is higher by 17.6% than the heat energy transformation efficiency of conventional heat energy machine, and efficiency improves ratio and is About 97.5%.
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 oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment 12 is tested, Introduce oil field waste gas to oil field waste gas burner 4, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is active according to oil field based on semi-conductor condensation waste gas heat The operation stability of Force system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat Can be about 25% by transformation efficiency, the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 29%, oil Ignition temperature in field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 36%, in oil field waste gas burner 4 Ignition temperature is 250 DEG C, and heat energy transformation efficiency is about 45%, and the ignition temperature in oil field waste gas burner 4 is about 300 DEG C Time, heat energy transformation efficiency is about 50%, and when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy converts effect Rate is about 55%；In the present embodiment ten, the heat energy transformation efficiency of oil field based on semi-conductor condensation heat energy from waste gas dynamical system is than often The thermal energy power machine (when 200 DEG C, average out to 18%) of rule is compared, oil field based on the semi-conductor condensation heat energy from waste gas of the present embodiment The energy transformation efficiency of dynamical system is higher by 18.4% than the heat energy transformation efficiency of conventional heat energy machine, and it is about 102% that efficiency improves ratio.
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 gasification installation 2；Due to following between one-way hydraulic pump 9 and gasification installation 2 Endless tube road 6 needs heat absorption, and in working medium conduction pipe 361, working medium needs heat extraction, and this structure recycles circulation pipe largely Working medium heat in road 6, increases thermal transition efficiency.
By oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment 13 is tested, Introduce oil field waste gas to oil field waste gas burner 4, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is active according to oil field based on semi-conductor condensation waste gas heat The operation stability of Force system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat Can be about 25.5% by transformation efficiency, the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 29.5%, the ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 36.5%, oil field waste gas burning Ignition temperature in device 4 is 250 DEG C, and heat energy transformation efficiency is about 45.5%, the ignition temperature in oil field waste gas burner 4 When being about 300 DEG C, heat energy transformation efficiency is about 50.5%, and the ignition temperature in oil field waste gas burner 4 is about 400 DEG C Time, heat energy transformation efficiency is about 55.5%；The heat of oil field based on semi-conductor condensation heat energy from waste gas dynamical system in the present embodiment ten Can compare than conventional thermal energy power machine (when 200 DEG C, average out to 18%) by transformation efficiency, the present embodiment based on semi-conductor condensation Oil field heat energy from waste gas dynamical system can transformation efficiency high by 18.9% than the heat energy transformation efficiency of conventional heat energy machine, efficiency raising Ratio is about 105%.
Embodiment 14 (as shown in figure 16): be with embodiment 13 difference: described condensing tube 51 becomes oblique type to divide Cloth.
By oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment 14 is tested, Introduce oil field waste gas to oil field waste gas burner 4, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is active according to oil field based on semi-conductor condensation waste gas heat The operation stability of Force system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat Can be about 25.5% by transformation efficiency, the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 30%, Ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 37%, in oil field waste gas burner 4 Ignition temperature be 250 DEG C, heat energy transformation efficiency is about 46%, and the ignition temperature in oil field waste gas burner 4 is 300 DEG C of left sides Time right, heat energy transformation efficiency is about 51%, and when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy converts Efficiency is about 56%；The heat energy transformation efficiency of oil field based on semi-conductor condensation heat energy from waste gas dynamical system in the present embodiment 14 Compare than conventional thermal energy power machine (when 200 DEG C, average out to 18%), oil field based on the semi-conductor condensation waste gas of the present embodiment The energy transformation efficiency of dynamic system of heat energy is higher by 19.3% than the heat energy transformation efficiency of conventional heat energy machine, and it is 108% that efficiency improves ratio Left and right.
Embodiment 15 (as shown in figure 17): be with embodiment one difference: described condensing tube 51 becomes vertical distribution.
By oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment 15 is tested, Introduce oil field waste gas to oil field waste gas burner 4, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is active according to oil field based on semi-conductor condensation waste gas heat The operation stability of Force system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat Can be about 25.5% by transformation efficiency, the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 30%, Ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 37.5%, oil field waste gas burner 4 Interior ignition temperature is 250 DEG C, and heat energy transformation efficiency is about 46.5%, and the ignition temperature in oil field waste gas burner 4 is 300 Time about DEG C, heat energy transformation efficiency is about 51.5%, when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, and heat 56.5% can be about by transformation efficiency；The heat energy of oil field based on semi-conductor condensation heat energy from waste gas dynamical system in the present embodiment 15 Transformation efficiency is compared than conventional thermal energy power machine (when 200 DEG C, average out to 18%), the present embodiment based on semi-conductor condensation The energy transformation efficiency of oil field heat energy from waste gas dynamical system is higher by 19.7% than the heat energy transformation efficiency of conventional heat energy machine, and efficiency improves ratio Rate is about 112%.
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 oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment 16 is tested, Introduce oil field waste gas to oil field waste gas burner 4, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is active according to oil field based on semi-conductor condensation waste gas heat The operation stability of Force system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat Can be about 25.5% by transformation efficiency, the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 30%, Ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 37%, in oil field waste gas burner 4 Ignition temperature be 250 DEG C, heat energy transformation efficiency is about 46%, and the ignition temperature in oil field waste gas burner 4 is 300 DEG C of left sides Time right, heat energy transformation efficiency is about 51%, and when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy converts Efficiency is about 56%；The heat energy transformation efficiency of oil field based on semi-conductor condensation heat energy from waste gas dynamical system in the present embodiment 16 Compare than conventional thermal energy power machine (when 200 DEG C, average out to 18%), oil field based on the semi-conductor condensation waste gas of the present embodiment The energy transformation efficiency of dynamic system of heat energy is higher by 19.3% than the heat energy transformation efficiency of conventional heat energy machine, and it is 108% that efficiency improves ratio Left and right.
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 oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment 17 is tested, Introduce oil field waste gas to oil field waste gas burner 4, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is active according to oil field based on semi-conductor condensation waste gas heat The operation stability of Force system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat Can be about 26.5% by transformation efficiency, the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 31.5%, the ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 38.5%, oil field waste gas burning Ignition temperature in device 4 is 250 DEG C, and heat energy transformation efficiency is about 47.5%, the ignition temperature in oil field waste gas burner 4 When being about 300 DEG C, heat energy transformation efficiency is about 52.5%, and the ignition temperature in oil field waste gas burner 4 is about 400 DEG C Time, heat energy transformation efficiency is about 57.5%；Oil field based on semi-conductor condensation heat energy from waste gas dynamical system in the present embodiment 17 Heat energy transformation efficiency is compared than conventional thermal energy power machine (when 200 DEG C, average out to 18%), the present embodiment based on semiconductor cooling The energy transformation efficiency of solidifying oil field heat energy from waste gas dynamical system is higher by 19.8% than the heat energy transformation efficiency of conventional heat energy machine, and efficiency carries Height ratio is about 110%.
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 oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment 18 is tested, Introduce oil field waste gas to oil field waste gas burner 4, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is active according to oil field based on semi-conductor condensation waste gas heat The operation stability of Force system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat Can be about 27% by transformation efficiency, the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 32%, oil Ignition temperature in field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 39%, in oil field waste gas burner 4 Ignition temperature is 250 DEG C, and heat energy transformation efficiency is about 48%, and the ignition temperature in oil field waste gas burner 4 is about 300 DEG C Time, heat energy transformation efficiency is about 53%, and when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy converts effect Rate is about 58%；The heat energy transformation efficiency ratio of oil field based on semi-conductor condensation heat energy from waste gas dynamical system in the present embodiment 18 Conventional thermal energy power machine (when 200 DEG C, average out to 18%) is compared, oil field based on the semi-conductor condensation waste gas heat of the present embodiment The energy transformation efficiency of motility system is higher by 20.3% than the heat energy transformation efficiency of conventional heat energy machine, and it is 113% left side that efficiency improves ratio Right.
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 oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment 19 is tested, Introduce oil field waste gas to oil field waste gas burner 4, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, heighten the pressure of working medium in condensing unit 5, heighten working medium in gasification installation 2 simultaneously Pressure, in circulation pipe, refrigerant flow rate is carried out according to the operation stability of oil field based on semi-conductor condensation heat energy from waste gas dynamical system Adjust；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, and heat energy transformation efficiency is about 25%, oil field Ignition temperature in waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 30%, the combustion in oil field waste gas burner 4 Burning temperature is 200 DEG C, and heat energy transformation efficiency is about 37%, and the ignition temperature in oil field waste gas burner 4 is 250 DEG C, and heat energy turns Changing efficiency and be about 46%, when the ignition temperature in oil field waste gas burner 4 is about 300 DEG C, heat energy transformation efficiency is about 51%, When ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy transformation efficiency is about 56%；In the present embodiment 19 The heat energy transformation efficiency of oil field based on semi-conductor condensation heat energy from waste gas dynamical system than conventional thermal energy power machine (when 200 DEG C, Average out to 18%) to compare, the energy transformation efficiency of oil field based on the semi-conductor condensation heat energy from waste gas dynamical system of the present embodiment is than often The heat energy transformation efficiency of rule heat energy machine is high by 18.2%, and it is about 101% that efficiency improves ratio.
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 oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment 20 is tested, Introduce oil field waste gas to oil field waste gas burner 4, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is active according to oil field based on semi-conductor condensation waste gas heat The operation stability of Force system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat Can be about 25.5% by transformation efficiency, the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 30.5%, the ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 37.5%, oil field waste gas burning Ignition temperature in device 4 is 250 DEG C, and heat energy transformation efficiency is about 46.5%, the ignition temperature in oil field waste gas burner 4 When being about 300 DEG C, heat energy transformation efficiency is about 51.5%, and the ignition temperature in oil field waste gas burner 4 is about 400 DEG C Time, heat energy transformation efficiency is about 56.5%；Oil field based on semi-conductor condensation heat energy from waste gas dynamical system in the present embodiment 20 Heat energy transformation efficiency is compared than conventional thermal energy power machine (when 200 DEG C, average out to 18%), the present embodiment based on semiconductor cooling The energy transformation efficiency of solidifying oil field heat energy from waste gas dynamical system is higher by 18.7% than the heat energy transformation efficiency of conventional heat energy machine, and efficiency carries Height ratio is about 104%.
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 oil field based on the semi-conductor condensation heat energy from waste gas dynamical system in above-described embodiment 21 is carried out reality Test, introduce oil field waste gas to oil field waste gas burner 4, the ignition temperature in oil field waste gas burner 4 be respectively 120 DEG C, 150 DEG C, 200 DEG C, 250 DEG C, 300 DEG C, 400 DEG C, in circulation pipe, refrigerant flow rate is according to oil field based on semi-conductor condensation waste gas heat The operation stability of motility system is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, heat energy transformation efficiency is about 26%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 31%, the ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 38%, oil field waste gas burner Ignition temperature in 4 is 250 DEG C, and heat energy transformation efficiency is about 47%, and the ignition temperature in oil field waste gas burner 4 is 300 DEG C During left and right, heat energy transformation efficiency is about 52%, and when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy turns Change efficiency and be about 57%；In the present embodiment 21, the heat energy of oil field based on semi-conductor condensation heat energy from waste gas dynamical system converts Efficiency is compared than conventional thermal energy power machine (when 200 DEG C, average out to 18%), the oil field based on semi-conductor condensation of the present embodiment The energy transformation efficiency of heat energy from waste gas dynamical system is higher by 19.2% than the heat energy transformation efficiency of conventional heat energy machine, and efficiency improves ratio and is About 106.5%.
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. oil field based on a semi-conductor condensation heat energy from waste gas dynamical system, including heat collector (1), gasification installation (2), Turbine (3), oil field waste gas burner (4), condensing unit (5), circulating line (6), cycle fluid (7) and one-way hydraulic pump (9), gasification installation (2), turbine (3), condensing unit (5) and one-way hydraulic pump (9) pass sequentially through circulating line (6) realize follow Ring UNICOM, circulating line (6) is contained within cycle fluid (7), and it is outside that heat collector (1) is arranged on gasification installation (2), is used for gasifying The biomass gasification boiler of device (2) interior working medium, is characterized in that: oil field waste gas burner (4) includes giving up in waste gas inlet (41), oil field Gas air-introduced machine (42), waste gas burning room (43), persistently lead firearm (44) and steam discharge pipe (45), air inlet (41), waste gas fire Burning room (43) and steam discharge pipe (45) UNICOM successively, oil field waste gas air-introduced machine (42) is arranged on air inlet (41), persistently leads fire Device (44) is arranged in waste gas burning room (43), and described firearm (44) of persistently leading is continuous discharge spark plug or heated filament net, steam Discharge pipe (45) is connected to heat collector (1), and condensing unit (5) includes condensing tube (51) and heat emission fan (52), condensing tube (51) Uniformly point Multi-layers distributing, condensing tube (51) mutually UNICOM, heat emission fan (52) is arranged on above or below condensing tube (51), heat emission fan (52) driving with convulsion mode or pressure wind mode, described condensing tube (51) is made by thermo-electric generation sheet (511), thermo-electric generation sheet (511) sheet metal (512), p-type semiconductor (513), n-type semiconductor (514), dielectric substrate layer (515) and output electrode are included (516), dielectric substrate layer (515) is uniformly interspersed with p-type semiconductor (513) and n-type semiconductor (514), equally distributed p-type Quasiconductor (513) and n-type semiconductor (514) are connected by sheet metal (512), p-type semiconductor (513) and n-type semiconductor (514) Series connection end at the whole story connect output electrode (516) respectively, be additionally provided with impurity mistake between condensing unit (5) and gasification installation (2) Filter pump (8).
Oil field based on semi-conductor condensation the most according to claim 1 heat energy from waste gas dynamical system, 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).
Oil field based on semi-conductor condensation the most according to claim 1 heat energy from waste gas dynamical system, is characterized in that: described collection Thermal (1) includes that upper cover (11) and lower cover (12), lower cover (12) middle part offer heating gate (13), upper cover (11) and lower cover (12) Laying respectively at upper and lower, be heat collector cavity (14) between upper cover (11) and lower cover (12), gasification installation (2) is positioned at heat collector cavity (14), Upper cover (11) lower part of described heat collector (1) is furnished with multilamellar upper cover and dashes forward ring (111), in the lower cover (12) of heat collector (1) Part is furnished with multilamellar lower cover and dashes forward ring (121), and upper cover ring (111) and lower cover ring (121) of dashing forward of dashing forward staggers.
Oil field based on semi-conductor condensation the most according to claim 1 heat energy from waste gas dynamical system, is characterized in that: described gas Gasifying device (2) includes gasification chamber (21) and preheating cavity (22), and gasification chamber (21) is the sky that gasification installation (2) interior working medium realizes gasification Chamber, preheating cavity (22) is connected with gasification chamber (21), and preheating cavity (22) is positioned at gasification chamber (21) front end, and preheating cavity (22) is used for work The preheating of matter.
Oil field based on semi-conductor condensation the most according to claim 4 heat energy from waste gas dynamical system, is characterized in that: described pre- Hot chamber (22) is spiral cast cavity, and gasification chamber (21) is spherical cavity.
Oil field based on semi-conductor condensation the most according to claim 3 heat energy from waste gas dynamical system, is characterized in that: described pre- Being additionally provided with atomizing mouth (23) between hot chamber (22) and gasification chamber (21), atomizing mouth (23) is for by the liquid in preheating cavity (22) Working medium is atomized, and sprays in gasification chamber (21).
Oil field based on semi-conductor condensation the most according to claim 6 heat energy from waste gas dynamical system, is characterized in that: described gas Changing chamber (21) is ellipse cavity.
Oil field based on semi-conductor condensation the most according to claim 6 heat energy from waste gas dynamical system, is characterized in that: described gas Changing chamber (21) and become tapered, the horizontal cross-section of gasification chamber (21) is that Rhizoma Nelumbinis is poroid.
Oil field based on semi-conductor condensation the most according to claim 6 heat energy from waste gas dynamical system, is characterized in that: described gas Changing chamber (21) and become polygon tapered, the horizontal cross-section of gasification chamber (21) is that honeycomb is poroid.
Oil field based on semi-conductor condensation the most according to claim 1 heat energy from waste gas dynamical system, 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.
CN201610760100.3A 2016-08-30 2016-08-30 A kind of oil field based on semi-conductor condensation heat energy from waste gas dynamical system Withdrawn CN106246259A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106533265A (en) * 2017-01-12 2017-03-22 王赞 Energy-saving device and method for thermoelectric power generation based on heat distribution pipeline
CN108518249A (en) * 2018-06-12 2018-09-11 匡亚剑 One kind being vertically arranged formula steam turbine generator

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106533265A (en) * 2017-01-12 2017-03-22 王赞 Energy-saving device and method for thermoelectric power generation based on heat distribution pipeline
CN108518249A (en) * 2018-06-12 2018-09-11 匡亚剑 One kind being vertically arranged formula steam turbine generator
CN108518249B (en) * 2018-06-12 2023-12-12 匡亚剑 Vertical arrangement type steam turbine generator

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Application publication date: 20161221