CN106246253A - A kind of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation - Google Patents

A kind of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation Download PDF

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Publication number
CN106246253A
CN106246253A CN201610759030.XA CN201610759030A CN106246253A CN 106246253 A CN106246253 A CN 106246253A CN 201610759030 A CN201610759030 A CN 201610759030A CN 106246253 A CN106246253 A CN 106246253A
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waste gas
oil field
heat energy
condensation
transformation efficiency
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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
    • F28B5/00—Condensers employing a combination of the methods covered by main groups F28B1/00 and F28B3/00; Other condensers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/0206—Heat exchangers immersed in a large body of liquid
    • 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)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

The invention discloses a kind of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation, including 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 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 lead firearm and steam discharge pipe, condensing unit includes condensing tube, heat emission fan and multiple booster body, heat emission fan is arranged on above or below condensing tube, booster body is evenly distributed in the middle part of condensing tube step by step；Oil field heat energy from waste gas dynamical system based on multi-stage booster condensation of the present invention has condensing rate faster, can reduce condensation row's energy, improve heat energy transformation efficiency, and stable, power adjustable.

Description

A kind of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation
Technical field
The invention belongs to utilization of energy apparatus field, a kind of oil field waste gas heat based on multi-stage booster condensation is active Force 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.
Summary of the invention
The purpose that the present invention is to be realized is: the hot type amount of reduction and thermal waste, improves heat energy transformation efficiency, stablizes work Matter gasification temperature and refrigerant flow rate, improve working medium quality, prevent working medium go bad, improve turbine structure, it is to avoid turbine reveal and Rotary speed unstabilization, improves condensing unit, accelerates condensing rate；Existing for existing thermal hardware in the above-mentioned background technology of solution: Heat energy transformation efficiency 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 impurity, whirlpool occurs Easily there is refrigerant leakage in turbine, and secondary speed is unstable and easily occurs stuck, and the thermal waste of condensing unit is big, cold Solidifying speed 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: give up in a kind of oil field based on multi-stage booster condensation Gas dynamic system of heat energy, including heat collector, gasification installation, turbine, oil field waste gas burner, condensing unit, circulation pipe Road, cycle fluid and one-way hydraulic pump, gasification installation, turbine, condensing unit and one-way hydraulic pump pass sequentially through circulating line Realizing circulation UNICOM, circulating line is contained within cycle fluid, and heat collector is arranged on outside gasification installation, in gasification installation The biomass gasification boiler of working medium；
It is characterized in that: 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, waste gas inlet, waste gas burning room and steam discharge pipe UNICOM successively, oil field waste gas air-introduced machine is installed At waste gas inlet, persistently leading firearm and be arranged on waste gas burning indoor, described firearm of persistently leading is continuous discharge spark plug or heat Silk screen, steam discharge pipe is connected to heat collector；
Described condensing unit includes condensing tube, heat emission fan and multiple booster body, and heat emission fan is arranged on above or below condensing tube, Booster body is evenly distributed in the middle part of condensing tube step by step, and described booster body includes pressurized cylinder, piston, eccentric, air inlet, goes out QI KOU, breather cheek valve, unidirectional air outlet valve and gas-pressure adjustable valve, piston is arranged in pressurized cylinder, and piston passes through push rod by bias Wheel drives, and is provided with air inlet and gas outlet, is provided with breather cheek valve at air inlet bottom pressurized cylinder, and gas outlet is provided with list To air outlet valve and gas-pressure adjustable valve；Use this structure can reduce the pressure of turbine outlet, increase at turbine inlet with go out Pressure reduction at gas, thus increase expanding gas amount of work in the turbine, and reduce the temperature of expanding gas, thus, this structure Preferable condensation effect can be produced, and improve the heat energy conversion ratio of dynamic system of heat energy.
As optimizing further, between gasification installation and condensing unit, it is additionally provided with contaminant filter pump.
As optimizing further, heat collector includes upper cover and lower cover, offers heating gate, upper cover and lower cover and divide in the middle part of lower cover Not being positioned at upper and lower, be heat collector cavity between upper cover and lower cover, the upper cover lower part of heat collector is furnished with multilamellar upper cover and dashes forward ring, thermal-arrest The lower cover upper part of device is furnished with multilamellar lower cover and dashes forward ring, and 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 described condensing tube is made by thermo-electric generation sheet, thermo-electric generation sheet Including sheet metal, p-type semiconductor, n-type semiconductor, dielectric substrate layer and output electrode, dielectric substrate layer is uniformly interspersed with p-type half Conductor and n-type semiconductor, equally distributed p-type semiconductor and n-type semiconductor connected by sheet metal, p-type semiconductor and N-shaped The series connection end at the whole story of quasiconductor connects output electrode respectively.
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, the power supply of one-way hydraulic pump.
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 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 heat energy from waste gas dynamical system based on multi-stage booster condensation described in this invention, during work, gasification Cycle fluid in device flows to turbine from heat collector cavity endothermic gasification, gasification working medium, drives rotating turbine, simultaneously turbine Drive generator rotation generates electricity；After gasification working medium flows through turbine, due to externally acting, its Temperature of Working and air pressure all can drop Low, 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 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.
Of the present invention based on multi-stage booster condensation oil field heat energy from waste gas dynamical system by condensing unit step by step Booster body is set, it is possible to decrease the pressure of turbine outlet, increases the pressure reduction with place of giving vent to anger at turbine inlet, thus increase Expanding gas amount of work in the turbine, and reduce the temperature of expanding gas largely；Thus, this structure can produce preferably Condensation effect, and improve the heat energy conversion ratio of dynamic system of heat energy.
Beneficial effect: oil field heat energy from waste gas dynamical system based on multi-stage booster condensation of the present invention, the most existing Heat energy machine in technology, has advantage and the progress of following several respects: 1. by setting up booster body in condensing unit, increases The amount of work of gas turbine, can improve condensing rate largely, reduces condensation power consumption, and improves the conversion of system heat energy Rate；2. by setting up precondenser, it is possible to increase air inlet and the pressure reduction of air vent in turbine, and the heat of working medium can be recycled Can, it is achieved heat absorption and heat rejection process to cycle fluid difference section comprehensively utilize, reduce thermal waste and cooling power consumption； 3., by setting up contaminant filter pump and one-way hydraulic pump, can effectively prevent working medium rotten and more impurity occurs, and preventing work Matter refluxes；4. by setting up working medium actuator, pressure and flow to working medium are controlled, and can be effectively improved gasification usefulness and cold Solidifying efficiency, and stablize working medium gasification temperature and refrigerant flow rate, prevent sealing member deformation bigger, it is to avoid secondary speed shakiness and working medium Leakage problem；5. condensing tube uses thermo-electric generation sheet make, the temperature difference calorific potential utilizing condensation process can be divided, improve heat energy and convert Efficiency, and utilize the interior electric current produced of thermo-electric generation sheet to accelerate thermal energy conduction speed；6. fully utilize the flammable of oil field waste gas Gas, reduces energy waste, and reduces 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 booster body structural representation 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 thermo-electric generation chip architecture schematic diagram of the present invention program 17；
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 for booster body, 531 for pressurized cylinder, 532 for piston, 533 for eccentric, 534 for air inlet, 535 For gas outlet, 536 be breather cheek valve, 537 for unidirectional air outlet valve, 538 for gas-pressure adjustable valve, 54 for catch box, 55 for heat radiation Sheet；
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 heat energy from waste gas dynamical system based on multi-stage booster condensation, including collection Thermal 1, gasification installation 2, turbine 3, oil field waste gas burner 4, condensing unit 5, circulating line 6, cycle fluid 7 and list To 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, and steam discharge pipe 45 is connected to heat collector 1；
(as shown in Figure 3) described condensing unit 5 includes condensing tube 51, heat emission fan 52 and multiple booster body 53, and condensing tube 51 is equal Even point of Multi-layers distributing, the mutual UNICOM of condensing tube 51, heat emission fan 52 is arranged on above or below condensing tube 51, and heat emission fan 52 is with convulsion Mode or pressure wind mode drive；
(as shown in Figure 4) described booster body 53 is evenly distributed in the middle part of condensing tube 51 step by step, and described booster body 53 includes increasing Cylinder pressure 531, piston 532, eccentric 533, air inlet 534, gas outlet 535, breather cheek valve 536, unidirectional air outlet valve 537 and can Regulating QI pressure valve 538, piston 532 is arranged in pressurized cylinder 531, and piston 532 is driven by eccentric 533 by push rod, pressurized cylinder 531 Bottom is provided with air inlet 534 and gas outlet 535, is provided with breather cheek valve 536 at air inlet 534, and gas outlet 535 is provided with Unidirectional air outlet valve 537 and gas-pressure adjustable valve 538；Use this structure can reduce the pressure in turbine 3 exit, increase turbine 3 With the pressure reduction located of giving vent to anger at air inlet, thus increase expanding gas amount of work in turbine 3, and reduce the temperature of expanding gas, Thus, this structure can produce preferable condensation effect, and improves the heat energy conversion ratio of dynamic system of heat energy.
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 the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment one 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 according to the oil field heat energy from waste gas condensed based on multi-stage booster The operation stability of dynamical 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 17%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 20%, Ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 25%, in oil field waste gas burner 4 Ignition temperature be 250 DEG C, heat energy transformation efficiency is about 30%, 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 36%, and when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy converts Efficiency is about 42%；The heat energy transformation efficiency of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in the present embodiment one Comparing than conventional thermal energy power machine (when 200 DEG C, average out to 18%), gives up in the oil field based on multi-stage booster condensation of the present embodiment The energy transformation efficiency of gas dynamic system of heat energy is higher by 7% than the heat energy transformation efficiency of conventional heat energy machine, and it is 40% left side that efficiency improves ratio Right；Meanwhile, the oil field heat energy from waste gas dynamical system cooldown rate that the present embodiment condenses based on multi-stage booster is fast, and hot driving is little, fortune Row noise is little, good operation 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 the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment two 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 according to the oil field heat energy from waste gas condensed based on multi-stage booster The operation stability of dynamical 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 17.5%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 21%, the ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 26%, oil field waste gas burner Ignition temperature in 4 is 250 DEG C, and heat energy transformation efficiency is about 31%, 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 37%, 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 43%；In the present embodiment two, the heat energy of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation converts effect Rate is compared than conventional thermal energy power machine (when 200 DEG C, average out to 18%), the oil field based on multi-stage booster condensation of the present embodiment The energy transformation efficiency of heat energy from waste gas dynamical system is higher by 7.8% than the heat energy transformation efficiency of conventional heat energy machine, and efficiency improves ratio and is About 44%.
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 the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment three 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 according to the oil field heat energy from waste gas condensed based on multi-stage booster The operation stability of dynamical 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 17.5%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 21.5%, the ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 26.5%, oil field waste gas burning Ignition temperature in device 4 is 250 DEG C, and heat energy transformation efficiency is about 31.5%, the ignition temperature in oil field waste gas burner 4 When being about 300 DEG C, heat energy transformation efficiency is about 37.5%, and the ignition temperature in oil field waste gas burner 4 is about 400 DEG C Time, heat energy transformation efficiency is about 43.5%；Oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in the present embodiment three 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 multi-stage booster The energy transformation efficiency of the oil field heat energy from waste gas dynamical system of condensation is higher by 8.2% than the heat energy transformation efficiency of conventional heat energy machine, and efficiency carries Height ratio is about 46%.
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 the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment four 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 according to the oil field heat energy from waste gas condensed based on multi-stage booster The operation stability of dynamical 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 18%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 22%, Ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 27%, in oil field waste gas burner 4 Ignition temperature be 250 DEG C, heat energy transformation efficiency is about 33%, 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 39%, and when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy converts Efficiency is about 45%；The heat energy transformation efficiency of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in the present embodiment four Comparing than conventional thermal energy power machine (when 200 DEG C, average out to 18%), gives up in the oil field based on multi-stage booster condensation of the present embodiment The energy transformation efficiency of gas dynamic system of heat energy is higher by 9.5% than the heat energy transformation efficiency of conventional heat energy machine, and it is 54% that efficiency improves ratio Left and right.
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 by the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation of above-described embodiment five 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 active according to the oil field waste gas heat condensed based on multi-stage booster 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 19% by transformation efficiency, 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 35%, and the ignition temperature in oil field waste gas burner 4 is about 300 DEG C Time, 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 converts effect Rate is about 47%；The heat energy transformation efficiency ratio of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in the present embodiment five Conventional thermal energy power machine (when 200 DEG C, average out to 18%) is compared, the oil field waste gas based on multi-stage booster condensation of the present embodiment The energy transformation efficiency of dynamic system of heat energy is higher by 11% than the heat energy transformation efficiency of conventional heat energy machine, and it is 62% left side that efficiency improves ratio Right.
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 the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment six 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 according to the oil field heat energy from waste gas condensed based on multi-stage booster The operation stability of dynamical 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%, Ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 30%, in oil field waste gas burner 4 Ignition temperature be 250 DEG C, heat energy transformation efficiency is about 37%, 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 42%, and when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy converts Efficiency is about 48%；The heat energy transformation efficiency of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in the present embodiment six Comparing than conventional thermal energy power machine (when 200 DEG C, average out to 18%), gives up in the oil field based on multi-stage booster condensation of the present embodiment The energy transformation efficiency of gas dynamic system of heat energy is higher by 12.3% than the heat energy transformation efficiency of conventional heat energy machine, and efficiency improves ratio and is About 69.5%.
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 the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment seven 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 according to the oil field heat energy from waste gas condensed based on multi-stage booster The operation stability of dynamical 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 20.5%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 24.5%, the ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 30.5%, oil field waste gas burning Ignition temperature in device 4 is 250 DEG C, and heat energy transformation efficiency is about 38%, and the ignition temperature in oil field waste gas burner 4 is When about 300 DEG C, heat energy transformation efficiency is about 43%, when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, and heat 49% can be about by transformation efficiency；In the present embodiment seven, the heat energy of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation turns Change efficiency to compare than conventional thermal energy power machine (when 200 DEG C, average out to 18%), the present embodiment based on multi-stage booster condensation The energy transformation efficiency of oil field heat energy from waste gas dynamical system is higher by 13% than the heat energy transformation efficiency of conventional heat energy machine, and efficiency improves ratio It is about 73.3%.
Embodiment eight: be with embodiment seven difference: described turbine 3 is the steamturbine comprising multistage blade Machine.
By the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment eight 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 according to the oil field heat energy from waste gas condensed based on multi-stage booster The operation stability of dynamical 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%, Ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 32%, in oil field waste gas burner 4 Ignition temperature be 250 DEG C, heat energy transformation efficiency is about 40%, 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 45%, and when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy converts Efficiency is about 51%；The heat energy transformation efficiency of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in the present embodiment eight Comparing than conventional thermal energy power machine (when 200 DEG C, average out to 18%), gives up in the oil field based on multi-stage booster condensation of the present embodiment The energy transformation efficiency of gas dynamic system of heat energy is higher by 14.8% than the heat energy transformation efficiency of conventional heat energy machine, and efficiency improves ratio and is About 83.3%.
Embodiment nine: be with embodiment seven difference: described turbine 3 is tesla's turbine.
By the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment nine 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 according to the oil field heat energy from waste gas condensed based on multi-stage booster The operation stability of dynamical 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%, the 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 burning Ignition temperature in device 4 is 250 DEG C, and heat energy transformation efficiency is about 40.5%, the ignition temperature in oil field waste gas burner 4 When being about 300 DEG C, heat energy transformation efficiency is about 46%, when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, Heat energy transformation efficiency is about 52%；The heat energy of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in the present embodiment nine Transformation efficiency is compared than conventional thermal energy power machine (when 200 DEG C, average out to 18%), condensing based on multi-stage booster of the present embodiment Oil field heat energy from waste gas dynamical system can transformation efficiency high by 15.4% than the heat energy transformation efficiency of conventional heat energy machine, efficiency raising Ratio is about 86.5%.
Embodiment ten: be with embodiment one difference: described turbine 3 is radial outward flow turbine.
By the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment ten 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 according to the oil field heat energy from waste gas condensed based on multi-stage booster The operation stability of dynamical 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%, Ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 32%, in oil field waste gas burner 4 Ignition temperature be 250 DEG C, heat energy transformation efficiency is about 40.5%, 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 45.5%, when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy Transformation efficiency is about 51%；In the present embodiment ten, the heat energy of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation converts Efficiency is compared than conventional thermal energy power machine (when 200 DEG C, average out to 18%), the oil based on multi-stage booster condensation of the present embodiment The energy transformation efficiency of field heat energy from waste gas dynamical system is higher by 15% than the heat energy transformation efficiency of conventional heat energy machine, and efficiency improves ratio and is About 84.5%.
Embodiment 11 (shown in Figure 12 and 13): be with embodiment ten difference: as described in turbine 3 be centrifugal Working medium actuator 10 it is additionally provided with between turbine 3 and condensing unit 5 described in formula turbine；Working medium actuator 10 includes that turbine limits Stream device 101 and pressure voltage stabilizing pressure controller 102, turbine current limiter 101 includes turbine structure 103 and secondary speed controller 104, pressure Strong voltage stabilizing pressure controller 102 includes slow pressure storage stream cylinder 105 gentle pressure piston 106 and barostat 107, slow pressure storage stream cylinder 105 Top UNICOM circulating line 6, the bottom UNICOM barostat 107 of slow pressure storage stream cylinder 105, slow pressure piston 106 is arranged on slow pressure In storage stream cylinder 105；When in circulating line 6, the pressure of working medium or flow velocity change, turbine current limiter 101 can be by limiting whirlpool The rotation of wheel construction 103 and realize the restriction of flow velocity, part working medium pressure storage stream cylinder 105 of can postponing flows out or flows into and realizes body simultaneously Long-pending expansion or compression, thus realize stablizing the effect of pressure.
By the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment 11 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 the oil field waste gas condensed based on multi-stage booster The operation stability of dynamic system of heat energy 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, heat energy transformation efficiency Being about 26.5%, the ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 33%, and oil field waste gas fires The ignition temperature burnt in device 4 is 250 DEG C, and heat energy transformation efficiency is about 42%, the ignition temperature in oil field waste gas burner 4 When being about 300 DEG C, heat energy transformation efficiency is about 47%, when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, Heat energy transformation efficiency is about 52%；The heat energy of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in the present embodiment ten Transformation efficiency is compared than conventional thermal energy power machine (when 200 DEG C, average out to 18%), condensing based on multi-stage booster of the present embodiment Oil field heat energy from waste gas dynamical system can transformation efficiency high by 15.6% than the heat energy transformation efficiency of conventional heat energy machine, efficiency raising Ratio is about 87.5%.
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 the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment 12 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 the oil field waste gas condensed based on multi-stage booster The operation stability of dynamic system of heat energy 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 23%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about Being 27%, the ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 34%, and oil field waste gas burning fills Putting the ignition temperature in 4 is 250 DEG C, and heat energy transformation efficiency is about 43%, 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 53%；In the present embodiment ten, the heat energy of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation converts Efficiency is compared than conventional thermal energy power machine (when 200 DEG C, average out to 18%), the oil based on multi-stage booster condensation of the present embodiment The energy transformation efficiency of field heat energy from waste gas dynamical system is higher by 16.4% than the heat energy transformation efficiency of conventional heat energy machine, and efficiency improves ratio It is about 92%.
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 the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment 13 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 the oil field waste gas condensed based on multi-stage booster The operation stability of dynamic system of heat energy 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 23.5%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, heat energy transformation efficiency Being about 27.5%, the 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 Ignition temperature in burner 4 is 250 DEG C, and heat energy transformation efficiency is about 43.5%, the burning in oil field waste gas burner 4 When temperature is about 300 DEG C, heat energy transformation efficiency is about 48.5%, and the ignition temperature in oil field waste gas burner 4 is 400 DEG C During left and right, heat energy transformation efficiency is about 53.5%；Oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in the present embodiment ten The heat energy transformation efficiency of system is compared than conventional thermal energy power machine (when 200 DEG C, average out to 18%), the present embodiment based on multistage The energy transformation efficiency of the oil field heat energy from waste gas dynamical system of supercharging condensation is higher by 16.9% than the heat energy transformation efficiency of conventional heat energy machine, It is about 95% that efficiency improves ratio.
Embodiment 14 (as shown in figure 16): be with embodiment 13 difference: described condensing tube 51 becomes oblique type to divide Cloth.
By the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment 14 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 the oil field waste gas condensed based on multi-stage booster The operation stability of dynamic system of heat energy 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 23.5%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, heat energy transformation efficiency Being about 28%, the ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 35%, oil field waste gas burning Ignition temperature in device 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 When about 300 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, and heat 54% can be about by transformation efficiency；The heat energy of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in the present embodiment 14 Transformation efficiency is compared than conventional thermal energy power machine (when 200 DEG C, average out to 18%), condensing based on multi-stage booster of the present embodiment Oil field heat energy from waste gas dynamical system can transformation efficiency high by 17.3% than the heat energy transformation efficiency of conventional heat energy machine, efficiency raising Ratio is about 98%.
Embodiment 15 (as shown in figure 17): be with embodiment one difference: described condensing tube 51 becomes vertical distribution.
By the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment 15 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 the oil field waste gas condensed based on multi-stage booster The operation stability of dynamic system of heat energy 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 23.5%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, heat energy transformation efficiency Being about 28%, the ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 35.5%, and oil field waste gas fires The ignition temperature burnt in device 4 is 250 DEG C, and heat energy transformation efficiency is about 44.5%, the burning temperature in oil field waste gas burner 4 When degree is about 300 DEG C, heat energy transformation efficiency is about 49.5%, and the ignition temperature in oil field waste gas burner 4 is 400 DEG C of left sides Time right, heat energy transformation efficiency is about 54.5%；Oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in the present embodiment 15 The heat energy transformation efficiency of system is compared than conventional thermal energy power machine (when 200 DEG C, average out to 18%), the present embodiment based on multistage The energy transformation efficiency of the oil field heat energy from waste gas dynamical system of supercharging condensation is higher by 17.7% than the heat energy transformation efficiency of conventional heat energy machine, It is about 102% that efficiency improves ratio.
Embodiment 16 (as shown in figure 18): be with embodiment one difference: described condensing tube 51 becomes horizontal distribution Time, upper and lower layer condensing tube mutually staggers.
By the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment 16 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 the oil field waste gas condensed based on multi-stage booster The operation stability of dynamic system of heat energy 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 23.5%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, heat energy transformation efficiency Being about 28%, the ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 35%, oil field waste gas burning Ignition temperature in device 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 When about 300 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, and heat 54% can be about by transformation efficiency；The heat energy of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in the present embodiment 16 Transformation efficiency is compared than conventional thermal energy power machine (when 200 DEG C, average out to 18%), condensing based on multi-stage booster of the present embodiment Oil field heat energy from waste gas dynamical system can transformation efficiency high by 17.3% than the heat energy transformation efficiency of conventional heat energy machine, efficiency raising Ratio is about 98%.
Embodiment 17 (as shown in figure 19): be with embodiment 16 difference: described condensing tube 51 passes through the temperature difference Generating sheet 511 is made, and described thermo-electric generation sheet 511 includes sheet metal 512, p-type semiconductor 513, n-type semiconductor 514, insulation base Matter layer 515 and output electrode 516, dielectric substrate layer 515 is uniformly interspersed with p-type semiconductor 513 and n-type semiconductor 514, uniformly divides P-type semiconductor 513 and the n-type semiconductor 514 of cloth are connected by sheet metal 512, p-type semiconductor 513 and n-type semiconductor 514 Series connection end at the whole story connects output electrode 516 respectively；Output electrode 516 voltage of thermo-electric generation sheet 511 reaches more than 3V.
Having explanation further as above-mentioned embodiment, output electrode 516 end of described thermo-electric generation sheet 511 is successively Connecting and have manostat 517, booster transformer 518, accumulator 519, accumulator 519 is for heat emission fan 52, the confession of one-way hydraulic pump 9 Electricity.
By the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment 17 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 the oil field waste gas condensed based on multi-stage booster The operation stability of dynamic system of heat energy 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, heat energy transformation efficiency Being 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 Ignition temperature in burner 4 is 250 DEG C, and heat energy transformation efficiency is about 45.5%, the burning in oil field waste gas burner 4 When temperature is about 300 DEG C, heat energy transformation efficiency is about 50.5%, and the ignition temperature in oil field waste gas burner 4 is 400 DEG C During left and right, heat energy transformation efficiency is about 55.5%；Oil field heat energy from waste gas power based on multi-stage booster condensation in the present embodiment 17 The heat energy transformation efficiency of system is compared than conventional thermal energy power machine (when 200 DEG C, average out to 18%), the present embodiment based on many The energy transformation efficiency of the oil field heat energy from waste gas dynamical system of level supercharging condensation is higher than the heat energy transformation efficiency of conventional heat energy machine 17.8%, it is about 100% that efficiency improves ratio.
Embodiment 18: be with embodiment 17 difference: described cycle fluid 7 uses the freon of routine；Adopt With freon as working medium, can be used for the utilization of lower temperature thermal source, but owing to it needs the pressure in circulating line 6 higher, The processing technology of circulating line 6 and seal member is required higher by implementation process.
By the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment 18 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, heighten the pressure of working medium in condensing unit 5, heighten work in gasification installation 2 simultaneously Matter pressure, in circulation pipe, refrigerant flow rate is according to the operation stability of the oil field heat energy from waste gas dynamical system condensed based on multi-stage booster It is adjusted；Experiment effect is: the ignition temperature in oil field waste gas burner 4 is 120 DEG C, and heat energy transformation efficiency is about 23%, Ignition temperature in oil field waste gas burner 4 is 150 DEG C, and heat energy transformation efficiency is about 28%, in oil field waste gas burner 4 Ignition temperature be 200 DEG C, heat energy transformation efficiency is about 35%, and the ignition temperature in oil field waste gas burner 4 is 250 DEG C, heat Can be about 44% by transformation efficiency, when the ignition temperature in oil field waste gas burner 4 is about 300 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%；The present embodiment ten In eight, the heat energy transformation efficiency of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation is than conventional thermal energy power machine (when 200 DEG C, average out to 18%) are compared, the energy of the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation of the present embodiment Transformation efficiency is higher by 16.2% than the heat energy transformation efficiency of conventional heat energy machine, and it is about 91% that efficiency improves ratio.
Embodiment 19: be with embodiment 17 difference: described cycle fluid 7 uses methanol；This kind of working medium Boiling point at normal temperatures is 64.7 DEG C, easily gasifies, relatively low to the temperature requirement of high temperature heat source, can be used for the low temperature less than 100 DEG C Heat resource power generation, but belong to poisonous and harmful inflammable gas, high to the sealing requirements of circulating line.
By the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment 19 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 the oil field waste gas condensed based on multi-stage booster The operation stability of dynamic system of heat energy 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 23.5%, and the ignition temperature in oil field waste gas burner 4 is 150 DEG C, heat energy transformation efficiency Being about 28.5%, the ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 35.5%, oil field waste gas Ignition temperature in burner 4 is 250 DEG C, and heat energy transformation efficiency is about 44.5%, the burning in oil field waste gas burner 4 When temperature is about 300 DEG C, heat energy transformation efficiency is about 49.5%, and the ignition temperature in oil field waste gas burner 4 is 400 DEG C During left and right, heat energy transformation efficiency is about 54.5%；Oil field heat energy from waste gas power based on multi-stage booster condensation in the present embodiment 19 The heat energy transformation efficiency of system is compared than conventional thermal energy power machine (when 200 DEG C, average out to 18%), the present embodiment based on many The energy transformation efficiency of the oil field heat energy from waste gas dynamical system of level supercharging condensation is higher than the heat energy transformation efficiency of conventional heat energy machine 16.7%, it is about 94% that efficiency improves ratio.
Embodiment 20: be with embodiment 17 difference: described cycle fluid 7 uses ethanol；This kind of working medium Boiling point at normal temperatures is 78.15 DEG C, and easily gasify incendivity, relatively low to the temperature requirement of high temperature heat source, can be used for being less than The low temperature heat resource power generation of 100 DEG C, but high to the sealing requirements of circulating line.
By the oil field heat energy from waste gas dynamical system based on multi-stage booster condensation in above-described embodiment 20 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 the oil field waste gas condensed based on multi-stage booster The operation stability of dynamic system of heat energy 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 Being 29%, the ignition temperature in oil field waste gas burner 4 is 200 DEG C, and heat energy transformation efficiency is about 36%, and oil field waste gas burning fills Putting the ignition temperature in 4 is 250 DEG C, and heat energy transformation efficiency is about 45%, and the ignition temperature in oil field waste gas burner 4 is 300 Time about DEG C, heat energy transformation efficiency is about 50%, when the ignition temperature in oil field waste gas burner 4 is about 400 DEG C, heat energy Transformation efficiency is about 55%；In the present embodiment 20, the heat energy of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation turns Change efficiency to compare than conventional thermal energy power machine (when 200 DEG C, average out to 18%), the present embodiment based on multi-stage booster condensation The energy transformation efficiency of oil field heat energy from waste gas dynamical system is higher by 17.2% than the heat energy transformation efficiency of conventional heat energy machine, and efficiency improves ratio Rate is about 96.5%.
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. based on multi-stage booster condensation an oil field 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 described condensing unit (5) includes condensing tube (51), heat emission fan (52) and multiple increasing Press mechanism (53), heat emission fan (52) is arranged on above or below condensing tube (51), and booster body (53) is evenly distributed on cold step by step Solidifying pipe (51) middle part, described booster body (53) includes pressurized cylinder (531), piston (532), eccentric (533), air inlet (534), gas outlet (535), breather cheek valve (536), unidirectional air outlet valve (537) and gas-pressure adjustable valve (538), piston (532) Being arranged in pressurized cylinder (531), piston (532) is driven by eccentric (533) by push rod, and pressurized cylinder (531) bottom is provided with Air inlet (534) and gas outlet (535), air inlet (534) place is provided with breather cheek valve (536), and gas outlet (535) are provided with Unidirectional air outlet valve (537) and gas-pressure adjustable valve (538), be additionally provided with contaminant filter between condensing unit (5) and gasification installation (2) Pump (8).
Oil field heat energy from waste gas dynamical system based on multi-stage booster condensation the most according to claim 1, is characterized in that: described Booster body (53) also includes differential pressure sensor (533) and automatic controller (534), automatic controller (534) reduction of fractions to a common denominator analysis pressure reduction Turbine pressure regulator (532) is automatically controlled by the signal of induction apparatus (533).
Oil field heat energy from waste gas dynamical system based on multi-stage booster condensation the most according to claim 1, is characterized in that: described Heat collector (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), in, upper cover (11) lower part of described heat collector (1) is furnished with multilamellar upper cover and dashes forward ring (111), the lower cover of heat collector (1) (12) upper 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 heat energy from waste gas dynamical system based on multi-stage booster condensation the most according to claim 1, is characterized in that: described Gasification installation (2) includes gasification chamber (21) and preheating cavity (22), and gasification chamber (21) is that gasification installation (2) interior working medium realizes gasification Cavity, 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 The preheating of working medium.
Oil field heat energy from waste gas dynamical system based on multi-stage booster condensation the most according to claim 4, is characterized in that: described Preheating cavity (22) is spiral cast cavity, and gasification chamber (21) is spherical cavity.
Oil field heat energy from waste gas dynamical system based on multi-stage booster condensation the most according to claim 3, is characterized in that: described Being additionally provided with atomizing mouth (23) between preheating cavity (22) and gasification chamber (21), atomizing mouth (23) is for by the liquid in preheating cavity (22) State working medium is atomized, and sprays in gasification chamber (21).
Oil field heat energy from waste gas dynamical system based on multi-stage booster condensation the most according to claim 6, is characterized in that: described Gasification chamber (21) is ellipse cavity.
Oil field heat energy from waste gas dynamical system based on multi-stage booster condensation the most according to claim 6, is characterized in that: described Gasification chamber (21) becomes tapered, and the horizontal cross-section of gasification chamber (21) is that Rhizoma Nelumbinis is poroid.
Oil field heat energy from waste gas dynamical system based on multi-stage booster condensation the most according to claim 6, is characterized in that: described Gasification chamber (21) becomes polygon tapered, and the horizontal cross-section of gasification chamber (21) is that honeycomb is poroid.
Oil field heat energy from waste gas dynamical system based on multi-stage booster condensation the most according to claim 1, is characterized in that: institute Stating turbine (3) is any in conventional steam turbine, multiple-stage steam turbine, tesla's turbine or radial outward flow turbine A kind of.
CN201610759030.XA 2016-08-30 2016-08-30 A kind of oil field heat energy from waste gas dynamical system based on multi-stage booster condensation Withdrawn CN106246253A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108159728A (en) * 2018-02-05 2018-06-15 广州泛美实验室系统科技股份有限公司 Strong acid-base vent cabinet exhaust gas discharges waste liquid condensing collector

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108159728A (en) * 2018-02-05 2018-06-15 广州泛美实验室系统科技股份有限公司 Strong acid-base vent cabinet exhaust gas discharges waste liquid condensing collector

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Application publication date: 20161221