CN205341478U - Gu useless integrated power production system that handles based on organic rankine cycle - Google Patents

Gu useless integrated power production system that handles based on organic rankine cycle Download PDF

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Publication number
CN205341478U
CN205341478U CN201620051156.7U CN201620051156U CN205341478U CN 205341478 U CN205341478 U CN 205341478U CN 201620051156 U CN201620051156 U CN 201620051156U CN 205341478 U CN205341478 U CN 205341478U
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China
Prior art keywords
solid waste
organic
heat energy
working medium
heat exchanger
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CN201620051156.7U
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Inventor
邸建军
娄世松
胡传芬
王影辉
陈溪
安利敏
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Bi Haizhou (beijing) Energy Saving Environmental Protection Equipment Co Ltd
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Bi Haizhou (beijing) Energy Saving Environmental Protection Equipment Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/12Heat utilisation in combustion or incineration of waste
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/20Waste processing or separation

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  • Processing Of Solid Wastes (AREA)

Abstract

The utility model discloses a gu useless integrated power production system that handles based on organic rankine cycle. Wherein, include: admittedly useless drying device for carry out drying process to solid waste material, the cracker for carry out schizolysis gasification treatment with the solid waste material behind the drying process, the fluid bed furnace is connected with the cracker for cracking result to obtaining behind the schizolysis gasification treatment carries out combustion processing, heat energy circulating device sets up heat energy circulating device and loops through fluid bed furnace, organic lang ken power generating equipment and drying device useless admittedly for the heat energy that produces during transmission combustion processing cracking result, solar collector for be heat energy with solar energy transformation, and add thermal treatment to the conduction oil, organic lang ken power generating equipment for be the electric energy with the heat energy development of evil in febrile disease of heat energy circulating device transmission. The utility model provides a because problem that the heat energy that produces can't be to solid useless the processing time carries out make full use of, the wasting of resources that leads to.

Description

Fixed-end forces combined generating system based on Organic Rankine Cycle
Technical field
This utility model relates to fixed-end forces field, in particular to a kind of fixed-end forces combined generating system based on Organic Rankine Cycle.
Background technology
At present, when solid waste is processed, the modes adopting burning process more.Although, utilize the mode of burning, in that context it may be convenient to solid waste is processed.But, when burning, insufficient owing to burning, very easily produce substantial amounts of dioxin, cause the secondary pollution for environment.Further, when solid waste is burnt, a large amount of heat energy can be produced.
For how avoiding the dioxin produced due to solid waste burn incompletely, and the heat energy produced during how to burning carries out Appropriate application, not yet proposes effective solution at present.
Utility model content
This utility model embodiment provides a kind of fixed-end forces combined generating system based on Organic Rankine Cycle, with at least solve due to cannot to fixed-end forces time produce heat energy make full use of, the technical problem of the wasting of resources caused.
An aspect according to this utility model embodiment, it is provided that a kind of fixed-end forces combined generating system based on Organic Rankine Cycle, including: solid waste drying device, for solid waste is dried process;Cracker, for carrying out cracking gasification process by the solid waste after dried;Fluid bed furnace, is connected with cracker, carries out burn processing for the crackate obtained after cracking gasization is processed;Heat energy circulating device, arranges heat energy circulating device and passes sequentially through fluid bed furnace, organic Lang Ken generating equipment and solid waste drying device, the heat energy produced during for transmitting burn processing crackate;Solar thermal collector, is used for converting solar energy into heat energy, and is heated conduction oil processing;Organic Lang Ken generating equipment, for being transferred to electric energy by the heat energy that heat energy circulating device transmits.
Further, heat energy circulating device includes: First Heat Exchanger, for being transferred in organic Lang Ken generating equipment by the heat energy transmitted by conduction oil;Second heat exchanger, is arranged at the downstream of First Heat Exchanger, for the heat that conduction oil transmits being transferred in solid waste drying device;Oil circulating pump, is used for utilizing conveyance conduit to be carried successively by conduction oil by fluid bed furnace, First Heat Exchanger and the second heat exchanger, makes conduction oil circulate between fluid bed furnace, First Heat Exchanger and the second heat exchanger.
Further, combined generating system also includes: flue gas purification system, is connected with cracker and fluid bed furnace, for processing cracker and the waste gas of fluid bed furnace generation.
Further, combined generating system also includes: heater, for being heated the conduction oil in heat energy circulating device processing.
Further, heater includes: solar thermal collector, is used for converting solar energy into heat energy, and is heated conduction oil processing.
Further, heater also includes: heat-conducting oil furnace, for being heated conduction oil processing.
Further, solid waste drying device, including: drying oven, for solid waste is dried process;First feed arrangement, is connected with drying oven, is used for drying oven conveying solid substance waste material.
Further, the first feed arrangement is spiral feed system.
Further, cracker, including: pyrolysis furnace, for the solid waste through dried being carried out cracking gasification process, obtain cracked gas and solid residue;Second feed arrangement, is connected with drying oven and pyrolysis furnace respectively, for the solid waste through dried is delivered to pyrolysis furnace.
Further, First Heat Exchanger is organic working medium heat exchanger.
Further, organic Lang Ken generating equipment, including: organic working medium vaporizer, it is arranged at the downstream of organic working medium heat exchanger, for gasifying organic working medium for organic gas;Organic Lang Ken generating set, utilizes the organic gas that the gasification of organic working medium vaporizer obtains to generate electricity;Organic working medium cooler, by the organic working medium that organic gas cooling is liquid after generating;Organic working medium circulating pump, for organic working medium is forced into the second pressure, and carries organic working medium by organic working medium heat exchanger.
In this utility model embodiment, by solid waste drying device, for solid waste is dried process;Cracker, for carrying out cracking gasification process by the solid waste after dried;Fluid bed furnace, is connected with cracker, carries out burn processing for the crackate obtained after cracking gasization is processed;Heat energy circulating device, arranges heat energy circulating device and passes sequentially through fluid bed furnace, organic Lang Ken generating equipment and solid waste drying device, the heat energy produced during for transmitting burn processing crackate;Solar thermal collector, is used for converting solar energy into heat energy, and is heated conduction oil processing;Organic Lang Ken generating equipment, for the heat energy that heat energy circulating device transmits is transferred to electric energy, the purpose that when having reached solid waste is processed, generation crackate and heat make full use of, it is achieved thereby that the technique effect that can also generate electricity while solid waste is processed, and then solve due to cannot to fixed-end forces time produce heat energy make full use of, the technical problem of the wasting of resources caused.
Accompanying drawing explanation
Accompanying drawing described herein is used for providing being further appreciated by of the present utility model, constitutes the part of the application, and schematic description and description of the present utility model is used for explaining this utility model, is not intended that improper restriction of the present utility model.In the accompanying drawings:
Fig. 1 is the schematic diagram of a kind of optional fixed-end forces combined generating system based on Organic Rankine Cycle according to this utility model embodiment;And
Fig. 2 is the schematic diagram of a kind of optional fixed-end forces combined generating system based on Organic Rankine Cycle according to this utility model embodiment.
Detailed description of the invention
In order to make those skilled in the art be more fully understood that this utility model scheme, below in conjunction with the accompanying drawing in this utility model embodiment, technical scheme in this utility model embodiment is clearly and completely described, obviously, described embodiment is only the embodiment of this utility model part, rather than whole embodiments.Based on the embodiment in this utility model, the every other embodiment that those of ordinary skill in the art obtain under not making creative work premise, all should belong to the scope of this utility model protection.
It should be noted that term " first " in specification and claims of the present utility model and above-mentioned accompanying drawing, " second " etc. are for distinguishing similar object, without being used for describing specific order or precedence.Should be appreciated that the data of so use can be exchanged in the appropriate case, in order to embodiment of the present utility model described herein can with except here diagram or describe those except order implement.In addition, term " includes " and " having " and their any deformation, it is intended to cover non-exclusive comprising, such as, contain series of steps or the process of unit, method, system, product or equipment be not necessarily limited to those steps or the unit clearly listed, but can include clearly not listing or for intrinsic other step of these processes, method, product or equipment or unit.
According to this utility model embodiment, provide the system embodiment of a kind of fixed-end forces combined generating system based on Organic Rankine Cycle, Fig. 1 is the schematic diagram of the fixed-end forces combined generating system based on Organic Rankine Cycle according to this utility model embodiment, as it is shown in figure 1, this system includes: solid waste drying device 10, cracker 20, fluid bed furnace 30, heat energy circulating device 40, solar thermal collector 50 and organic Lang Ken generating equipment 60.
Wherein, solid waste drying device 10, for being dried process to solid waste;Cracker 20, for carrying out cracking gasification process by the solid waste after dried;Fluid bed furnace 30, is connected with cracker 20, carries out burn processing for the crackate obtained after cracking gasization is processed;Heat energy circulating device 40, arranges heat energy circulating device 40 and passes sequentially through fluid bed furnace 30, organic Lang Ken generating equipment 60 and solid waste drying device 10, the heat energy produced during for transmitting burn processing crackate;Organic Lang Ken generating equipment 60, for being transferred to electric energy by the heat energy that heat energy circulating device 40 transmits.
Solid waste drying device 10, for solid waste being dried process, the moisture in elimination solid waste;Cracker 20, for the solid waste after dried carries out cracking gasification process, obtains crackate, and wherein, crackate at least includes: cracked gas and solid residue;Fluid bed furnace 30, is connected with cracker 20, for crackate is carried out burn processing;Heat energy circulating device 40, sequentially pass through fluid bed furnace 30, organic Lang Ken generating equipment 60 and solid waste drying device 10, the heat energy produced during for gathering fluid bed furnace 30 combustion cracking product, and transfer thermal energy in organic Lang Ken generating equipment 60 and solid waste drying device 10;Solar thermal collector 50, is used for converting solar energy into heat energy, and is heated conduction oil processing;Organic Lang Ken generating equipment 60, for obtaining heat energy by heat energy circulating device 40, is transferred to electric energy by heat energy.
Concrete, solid waste drying device 10 can use inside and outside the rotary furnace that simultaneously heats.First, solid waste enters solid waste drying device 10 by the first charging aperture 01, by the flue gas of the outer layer interlayer of drying oven and internal conduction oil, solid waste is heated, solid waste is dried process, makes the water vapour rapid evaporation in solid waste.
Then, the solid waste after process will be dried, be inputted to cracker 20 by the second charging aperture 02.Solid waste is high-temperature cracked into gaseous organic substance and solid residue in cracker 20.Use wherein it is possible to gaseous organic substance is delivered in cracker 20 and fluid bed furnace 30 as fuel.Can be delivered to solid residue to connect and fluid bed furnace 30 carries out high-temp combustion, such that it is able to avoid the generation of dioxin.The high-temperature flue gas that cracker 20 produces in cracking process can also be delivered to the outside interlayer of solid waste drying device 10, as the thermal source of solid waste drying device 10, solid waste is dried process.Simultaneously, it is possible to use the conduction oil in heat energy circulating device 40 is heated by solar thermal collector 50.Wherein, solar thermal collector 50 can adopt groove type solar thermal collector, it would however also be possible to employ butterfly solar thermal collector, is not specifically limited herein.
Further, cracker 20 and fluid bed furnace 30 burn produced heat, it is possible to for the conduction oil in heat energy circulating device 40 is heated.By heat energy circulating device 40, the conduction oil after heating is delivered in the middle of organic Lang Ken generating equipment 60 and solid waste drying device 10.Wherein, Lang Ken generating equipment 60 obtains heat energy by organic working medium heat exchanger from conduction oil, and generates electricity.Solid waste drying device 10 utilizes remaining heat energy that solid waste is dried process.
In addition, in cracking processes, the gaseous organic substance produced and solid residue often can not meet the needs of cracker 20 and fluid bed furnace 30, therefore, the fuel gas such as natural gas, coal gas can also be utilized as fuel, thus the high-temp combustion in the cracking process met in cracker 20 and fluid bed furnace 30.
In the technical scheme of the present embodiment, by solid waste being dried process with the inside and outside rotary furnace heated simultaneously, revolution pyrolysis furnace is used to utilize the mode that anoxybiotic cracks that solid waste is carried out cracking process, and utilize fluid bed furnace that crackate is carried out high-temperature process, thus avoid the generation of dioxin when fixed-end forces.And, utilize the heat produced when dried, cracking process and high-temperature process that conduction oil is heated, and by conduction oil, heat energy is conducted, thus utilizing heat energy to drive organic Lang Ken generating equipment to generate electricity, meanwhile, conduction oil is heated with solar thermal collector for supplemental heat source.Thus carry out fixed-end forces at the same time it can also be obtain electric energy.Adopting organic Lang Ken electricity generation system compared with conventional vapor electricity generation system, device structure and flow process are more succinct, and the Load Regulation of electricity generation system is more flexible.
In sum, by above-mentioned solid waste drying device 10, cracker 20, fluid bed furnace 30, heat energy circulating device 40, solar thermal collector 50 and organic Lang Ken generating equipment 60, the purpose that when can reach solid waste is processed, generation crackate and heat make full use of, achieve the technique effect that can also generate electricity while solid waste is processed, solve due to cannot to fixed-end forces time produce heat energy make full use of, the problem of the wasting of resources caused.
As the optional embodiment of one, can also include in based on the fixed-end forces combined generating system of Organic Rankine Cycle: flue gas purification system 70.Wherein, flue gas purification system 70 is connected with cracker 20 and fluid bed furnace 30, for processing cracker 20 and the waste gas of fluid bed furnace 30 generation.
Concrete, the waste gas that cracker 20 and fluid bed furnace 30 produce can be collected by flue gas purification system 70, and focus on, thus avoiding the secondary pollution for environment.
As the optional embodiment of one, heat energy circulating device 40 includes: First Heat Exchanger the 401, second heat exchanger 403 and oil circulating pump 405.
Wherein, First Heat Exchanger 401, for being transferred to the heat energy transmitted by conduction oil in organic Lang Ken generating equipment 60;Second heat exchanger 403, is arranged at the downstream of First Heat Exchanger 401, for the heat that conduction oil transmits being transferred in solid waste drying device 10;Oil circulating pump 405, is used for utilizing conveyance conduit to be carried successively by conduction oil by fluid bed furnace 30, First Heat Exchanger 401 and the second heat exchanger 403, makes conduction oil at fluid bed furnace 30, circulates between First Heat Exchanger 401 and the second heat exchanger 403.
As the optional embodiment of one, above-mentioned oil circulating pump 405 is utilized to make the conduction oil in heat energy circulating device 40 at fluid bed furnace 30, be circulated between organic Lang Ken generating equipment 60 and solid waste drying device 10.Wherein, above-mentioned First Heat Exchanger 401 can use conduction oil-organic working medium heat exchanger, the heat conducted by conduction oil can be transferred in the middle of the organic working medium in the middle of organic Lang Ken electricity generation system by First Heat Exchanger 401, thus utilizing organic Lang Ken electromotor to generate electricity.Utilize above-mentioned second heat exchanger 403 to be transferred in solid waste drying device 10 by the remaining heat in conduction oil, solid waste is dried process.Wherein, in above-mentioned heat energy circulating device, conduction oil first passes through organic Lang Ken generating equipment 60, again through solid waste drying device 10.
As the optional embodiment of one, as in figure 2 it is shown, combined generating system can also include: heat-conducting oil furnace 80.
Wherein, heat-conducting oil furnace 80, for being heated conduction oil processing.
Concrete, owing to conduction oil being heated by cracker 20, fluid bed furnace 30 and solar thermal collector 50, the requirement that organic Lang Ken generating equipment 60 is generated electricity by way of merging two or more grid systems sometimes can not be met.Further, when solid waste not being processed, organic Lang Ken generating equipment 60 can not generate electricity.Continuing, in order to meet, the demand that generates electricity, it is possible to add independent heat-conducting oil furnace 80 in combined generating system, in fixed-end forces process, produced heat energy can not meet when sending out some demand, it is possible to by starting heat-conducting oil furnace 80, conduction oil carries out auxiliary heating.Wherein, heat-conducting oil furnace 80, as standby firing equipment, uses when shortage of heat in combined generating system.
As the optional embodiment of one, as in figure 2 it is shown, above-mentioned solid waste drying device 10, including: drying oven 101 and the first feed arrangement 103.
Wherein, drying oven 101, for being dried process to solid waste;First feed arrangement 103, is connected with drying oven, is used for drying oven conveying solid substance waste material.
Concrete, the first feed arrangement 103 can adopt spiral feed system, drying oven 101 can adopt the logical high-temperature flue gas of outside interlayer, the rotary furnace of internal admittance deep fat.
As the optional embodiment of one, the first feed arrangement is spiral feed system.
As the optional embodiment of one, as in figure 2 it is shown, above-mentioned cracker 20, including: pyrolysis furnace 201 and the second feed arrangement 203.
Wherein, pyrolysis furnace 201, for the solid waste through dried being carried out cracking gasification process, obtain cracked gas and solid residue;Second feed arrangement 203, is connected with drying oven and pyrolysis furnace respectively, for the solid waste through dried is delivered to pyrolysis furnace.
Concrete, pyrolysis furnace 201 can adopt the outside interlayer rotary furnace by gas heating.
As the optional embodiment of one, First Heat Exchanger is organic working medium heat exchanger.
As the optional embodiment of one, as in figure 2 it is shown, organic Lang Ken generating equipment 60, including: organic working medium vaporizer 601, organic Lang Ken generating set 603, organic working medium cooler 605 and organic working medium circulating pump 607.
Wherein, organic working medium vaporizer 601, it is arranged at the downstream of organic working medium heat exchanger, for gasifying organic working medium for organic gas;Organic Lang Ken generating set 603, utilizes the organic gas that the gasification of organic working medium vaporizer obtains to generate electricity;Organic working medium cooler 605, by the organic working medium that organic gas cooling is liquid after generating;Organic working medium circulating pump 607, for organic working medium is forced into the second pressure, and carries organic working medium by organic working medium heat exchanger.
Concrete, in above-mentioned organic Lang Ken generating equipment 60, organic Lang Ken generating set 603 can adopt expansion power generation unit, organic working medium circulating pump 607 can adopt conduction oil-organic working medium heat exchanger.Further, in organic working medium cooler 605, it is possible to adopt air-cooled mode to cool down, it would however also be possible to employ the mode of water-cooled cools down, and is not specifically limited herein.
As the optional embodiment of one, present embodiments provide for a kind of cogeneration machine based on heliotechnics, fixed-end forces technology and organic Lang Ken generation technology.Wherein, after solid waste is successively dried by drying equipment and pyrolysis furnace process and cracking process, the direct influent stream fluidized bed boiler high-temp combustion of solid residue that will produce, using the produced cracking gas fuel as pyrolysis furnace and fluidized-bed combustion boiler, the heat that pyrolysis furnace and fluid bed furnace produce is taken out by conduction oil, generate electricity for organic Lang Ken, utilize the waste heat after conduction oil generating to be also used as the thermal source of drying device.And, it is also possible to the flue gas that pyrolysis furnace and fluidized-bed combustion boiler produce is delivered to drying equipment, thus solid waste is dried process.
As the optional embodiment of one, in above-mentioned combined generating system, by solid waste is sent in drying equipment, it is heated to 100 DEG C and removes moisture.Then the solid waste after dried is sent in pyrolysis furnace, Pintsch process in temperature more than 400 DEG C, make the major part therein cleaved gasification of Organic substance, remaining solid residue is sent in the fluid bed furnace of more than 800 DEG C and carry out high-temperature oxydation, thus avoiding the temperature that dioxin produces.The heat produced in above-mentioned cracking gasification process and burn processing is transferred in organic Lang Ken generating equipment by conduction oil, thus reaching the purpose utilizing the heat produced when solid waste is processed to generate electricity.
By above-mentioned combined power generation device, the anoxybiotic of solid waste is cracked and high-temperature process, avoid the generation of dioxin, make use of solar energy and waste heat to be generated electricity by organic Lang Ken generating equipment simultaneously, improve utilization rate of waste heat, while fixed-end forces, obtain the energy.
Above-mentioned this utility model embodiment sequence number, just to describing, does not represent the quality of embodiment.
In above-described embodiment of the present utility model, the description of each embodiment is all emphasized particularly on different fields, certain embodiment there is no the part described in detail, it is possible to referring to the associated description of other embodiments.
In several embodiments provided herein, it should be understood that disclosed technology contents, can realize by another way.Wherein, device embodiment described above is merely schematic, the such as division of described unit, can be that a kind of logic function divides, actual can have other dividing mode when realizing, such as multiple unit or assembly can in conjunction with or be desirably integrated into another system, or some features can be ignored, or does not perform.Another point, shown or discussed coupling each other or direct-coupling or communication connection can be through INDIRECT COUPLING or the communication connection of some interfaces, unit or module, it is possible to be electrical or other form.
The above is only preferred implementation of the present utility model; it should be pointed out that, for those skilled in the art, under the premise without departing from this utility model principle; can also making some improvements and modifications, these improvements and modifications also should be regarded as protection domain of the present utility model.

Claims (9)

1. the fixed-end forces combined generating system based on Organic Rankine Cycle, it is characterised in that including:
Solid waste drying device, for being dried process to solid waste;
Cracker, for carrying out cracking gasification process by the solid waste after described dried;
Fluid bed furnace, is connected with described cracker, for the crackate obtained after described cracking gasification process is carried out burn processing;
Heat energy circulating device, arranges described heat energy circulating device and passes sequentially through described fluid bed furnace, organic Lang Ken generating equipment and described solid waste drying device, the heat energy produced during for transmitting crackate described in burn processing;
Solar thermal collector, is used for converting solar energy into heat energy, and is heated conduction oil processing;
Described organic Lang Ken generating equipment, for being transferred to electric energy by the heat energy that described heat energy circulating device transmits.
2. combined generating system according to claim 1, it is characterised in that described heat energy circulating device includes:
First Heat Exchanger, for being transferred to the heat energy transmitted by conduction oil in described organic Lang Ken generating equipment;
Second heat exchanger, is arranged at the downstream of described First Heat Exchanger, for the heat that described conduction oil transmits being transferred in solid waste drying device;
Oil circulating pump, for utilizing conveyance conduit to be carried successively by described conduction oil by described fluid bed furnace, described First Heat Exchanger and described second heat exchanger, described conduction oil is made to circulate between described fluid bed furnace, described First Heat Exchanger and described second heat exchanger.
3. combined generating system according to claim 2, it is characterised in that described combined generating system also includes:
Flue gas purification system, is connected with described cracker and described fluid bed furnace, for processing described cracker and the waste gas of described fluid bed furnace generation.
4. combined generating system according to claim 2, it is characterised in that described combined generating system also includes:
Heat-conducting oil furnace, for being heated described conduction oil processing.
5. combined generating system according to claim 1, it is characterised in that described solid waste drying device, including:
Drying oven, for being dried process to described solid waste;
First feed arrangement, is connected with described drying oven, for carrying described solid waste to described drying oven.
6. combined generating system according to claim 5, it is characterised in that described first feed arrangement is spiral feed system.
7. combined generating system according to claim 6, it is characterised in that described cracker, including:
Pyrolysis furnace, for the described solid waste through dried carries out cracking gasification process, obtains cracked gas and solid residue;
Second feed arrangement, is connected with described drying oven and described pyrolysis furnace respectively, for the described solid waste through dried is delivered to described pyrolysis furnace.
8. combined generating system according to claim 2, it is characterised in that described First Heat Exchanger is organic working medium heat exchanger.
9. combined generating system according to claim 8, it is characterised in that described organic Lang Ken generating equipment, including:
Organic working medium vaporizer, is arranged at the downstream of described organic working medium heat exchanger, for gasifying described organic working medium for organic gas;
Organic Lang Ken generating set, utilizes the described organic gas that the gasification of described organic working medium vaporizer obtains to generate electricity;
Organic working medium cooler, by the described organic working medium that the cooling of described organic gas is liquid after generating;
Organic working medium circulating pump, for described organic working medium is forced into the second pressure, and carries described organic working medium by described organic working medium heat exchanger.
CN201620051156.7U 2016-01-19 2016-01-19 Gu useless integrated power production system that handles based on organic rankine cycle Active CN205341478U (en)

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Application Number Priority Date Filing Date Title
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Application Number Priority Date Filing Date Title
CN201620051156.7U CN205341478U (en) 2016-01-19 2016-01-19 Gu useless integrated power production system that handles based on organic rankine cycle

Publications (1)

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