CN210948820U - Dual-working-medium Rankine cycle waste heat power generation system and generator - Google Patents
Dual-working-medium Rankine cycle waste heat power generation system and generator Download PDFInfo
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- CN210948820U CN210948820U CN201921430130.3U CN201921430130U CN210948820U CN 210948820 U CN210948820 U CN 210948820U CN 201921430130 U CN201921430130 U CN 201921430130U CN 210948820 U CN210948820 U CN 210948820U
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- 239000002918 waste heat Substances 0.000 title claims abstract description 79
- 238000010248 power generation Methods 0.000 title claims abstract description 46
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 60
- 238000011084 recovery Methods 0.000 claims abstract description 43
- 238000004064 recycling Methods 0.000 claims description 10
- MSSNHSVIGIHOJA-UHFFFAOYSA-N pentafluoropropane Chemical compound FC(F)CC(F)(F)F MSSNHSVIGIHOJA-UHFFFAOYSA-N 0.000 claims description 6
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 claims description 4
- LVGUZGTVOIAKKC-UHFFFAOYSA-N 1,1,1,2-tetrafluoroethane Chemical compound FCC(F)(F)F LVGUZGTVOIAKKC-UHFFFAOYSA-N 0.000 claims description 2
- OHMHBGPWCHTMQE-UHFFFAOYSA-N 2,2-dichloro-1,1,1-trifluoroethane Chemical compound FC(F)(F)C(Cl)Cl OHMHBGPWCHTMQE-UHFFFAOYSA-N 0.000 claims description 2
- 239000001282 iso-butane Substances 0.000 claims description 2
- 230000009977 dual effect Effects 0.000 claims 4
- 238000001704 evaporation Methods 0.000 abstract description 11
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- 238000009833 condensation Methods 0.000 description 9
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- 230000005611 electricity Effects 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 5
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 239000003546 flue gas Substances 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
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- 238000010168 coupling process Methods 0.000 description 2
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- 230000009286 beneficial effect Effects 0.000 description 1
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- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Abstract
The utility model provides a two working medium rankine cycle waste heat power generation systems and generator, including two evaporation pressure exhaust-heat boilers, high-pressure steam heat recovery system and low pressure steam heat recovery system, high-pressure steam heat recovery system is used for carrying out recycle to the high-pressure steam waste heat, low pressure steam heat recovery system is used for carrying out recycle to the low pressure steam waste heat, high-pressure steam heat recovery system is the rankine cycle system of water, low pressure steam heat recovery system is the rankine cycle system who contains water and organic working medium. The utility model discloses a two evaporation pressure exhaust-heat boiler retrieve high-pressure steam through high-pressure steam heat recovery system, and low-pressure steam heat recovery system retrieves low-pressure steam, realizes the ladder grade recycle of steam waste heat, effectively utilizes the steam waste heat, for single evaporation pressure exhaust-heat boiler, can effectively improve the main steam parameter that gets into the steam turbine, improves steam turbine generating efficiency.
Description
Technical Field
The utility model relates to a steam waste heat recovery utilizes technical field, concretely relates to two working medium rankine cycle waste heat power generation systems and generator.
Background
In the industrial process, in order to effectively utilize the waste heat of the flue gas or the waste heat of other gas sources to save energy, the conventional waste heat utilization is to heat water by a single waste heat boiler to generate steam, and the steam enters a steam turbine to expand to do work to generate power. Only about 30% of heat energy in the conventional steam cycle is converted into electric energy, and 70% of the heat energy is taken away by circulating cooling water of a condenser in steam condensation, so that the utilization rate of waste heat is not high. In addition, when the steam generated by the single steam parameter boiler is used for non-power generation, the steam is often used after the steam parameters are reduced by the temperature and pressure reducer, the grade of the steam is reduced, exergy loss is increased, and further waste of energy is caused; the steam is adjusted and distributed in real time according to different purposes, so that the steam turbine is caused to operate frequently under variable working conditions, and the generating efficiency and the operation safety of the unit are influenced.
The patent with application number CN201310626226.8 discloses a two working medium waste heat power generation systems, and this utility model discloses a through carrying out rational design to two working medium circulations, through many times heat transfer treatment, can be abundant utilize the steam extraction waste heat that produces among the steam cycle process as the heat source of low boiling point working medium circulation process, can improve waste heat utilization efficiency by a wide margin. However, the heat source of the organic rankine cycle of the present invention comes entirely from the steam turbine exhaust condensation heat, which requires that the steam turbine exhaust pressure and temperature not be too low, at least to ensure that the ORC system is able to operate properly. The steam turbine has too high exhaust back pressure, the water steam energy is not fully utilized, and the efficiency of the steam turbine is reduced. Whether the steam turbine exhaust parameters are improved to be used as a heat source for circulation of an ORC system is the best scheme or not needs to be demonstrated in further detail.
Application number CN201810089685.X proposes a geothermal power generation device and method combining double-stage flash evaporation and an organic Rankine cycle. The utility model discloses a power generation is carried out to the hot tail water waste heat of recoverable well low temperature, has improved the generated power of geothermal power station. However, the system directly uses geothermal water to flash and enter the expansion machine to do work to generate electricity, so that the water quality cannot be guaranteed, and the safe operation of the unit is seriously threatened; the flue gas-water heat exchange is carried out in the flue gas heat-taking heat exchanger, the water side has no phase change, the heat exchange amount is limited, the temperature of the discharged flue gas is still high after heat exchange, and the waste heat recovery rate is low.
Application No. CN201610008195.3 discloses a low temperature thermal fluid recycling system. The system comprises a steam Rankine cycle and two organic Rankine cycles, can fully utilize the waste heat of the reciprocating engine to generate power, and is energy-saving and environment-friendly. However, saturated steam flashed by the flash evaporator in the system is easy to carry liquid into the steam turbine, and threatens the safe operation of the steam turbine.
SUMMERY OF THE UTILITY MODEL
To the not enough of prior art, the utility model provides a two working medium rankine cycle waste heat power generation systems and generator.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
the double-working-medium Rankine cycle waste heat power generation system comprises a double-evaporation-pressure waste heat boiler, a high-pressure steam heat recovery system and a low-pressure steam heat recovery system, wherein the high-pressure steam heat recovery system is used for recycling high-pressure steam waste heat, the low-pressure steam heat recovery system is used for recycling low-pressure steam waste heat, the high-pressure steam heat recovery system is a Rankine cycle system of water, and the low-pressure steam heat recovery system is a Rankine cycle system containing water and an organic working medium. Adopt two evaporation pressure exhaust-heat boiler, retrieve high-pressure steam through high-pressure steam heat recovery system, low-pressure steam heat recovery system retrieves low-pressure steam, realizes the ladder grade recycle of steam waste heat, effectively utilizes the steam waste heat, for single evaporation pressure exhaust-heat boiler, can effectively improve the main steam parameter that gets into the steam turbine, improves steam turbine generating efficiency.
Further, high pressure steam heat recovery system specifically includes high pressure steam pocket, steam turbine, first condenser, first condensate pump, first oxygen-eliminating device, first circulating water pump, the exit end of high pressure steam pocket is connected the steam turbine entry end, the steam turbine exit end is connected first condenser entry end, first condenser exit end is through first condensate pump connection first oxygen-eliminating device entry end, first oxygen-eliminating device exit end is through first circulating water pump connection high pressure steam pocket entry end. The steam separated from the high-pressure steam pocket is superheated and then enters a turbine to generate power, the steam discharged by the turbine continuously releases partial steam condensation latent heat through a preheater, the steam enters a first condenser to continuously release heat and condense, condensed water is pressurized by a first condensed water pump to enter a first deaerator to be deaerated, and finally the condensed water is pressurized by a first circulating water pump to enter the high-pressure steam pocket. The waste heat of the high-pressure steam is effectively utilized, and the high quality of the steam entering the steam turbine is ensured.
Further, the low-pressure steam heat recovery system specifically comprises a low-pressure steam drum, a second condensate pump, a second deaerator, a second circulating water pump, an expander, a second condenser, a working medium pump, a preheater and an evaporator, the outlet end of the low-pressure steam drum is connected with the inlet end of the evaporator, the outlet end of the evaporator is connected to the inlet end of the second deaerator through the second condensate pump, the outlet end of the second deaerator is connected to the inlet end of the low-pressure steam drum through the second circulating water pump, the inlet end of the preheater is connected with the outlet end of the steam turbine, the outlet end of the preheater is connected with the inlet end of the evaporator, the outlet end of the evaporator is connected with the inlet end of the expansion machine, the outlet end of the expansion machine is connected with the inlet end of the second condenser, and the outlet end of the second condenser is connected to the inlet end of the preheater through the working medium pump. The low pressure steam is separated by the low pressure steam pocket after, gets into the evaporimeter and releases heat the side and condense, and the condensate water gets into second oxygen-eliminating device deoxidization after the pressurization of second condensate pump, and the deaerated water is sent into the low pressure steam pocket through the pressurization of second circulating water pump, and organic working medium absorbs steam turbine exhaust heat through the preheater and preheats, and organic working medium after preheating gets into the heat that the evaporimeter absorbed low pressure steam, will organic working medium becomes high pressure steam and gets into expander expansion acting, expander and generator coaxial coupling, drags the generator electricity generation, and organic working medium exhaust gets into the second condenser condensation and becomes liquid, gets into the working medium pump afterwards, gets into the preheater after the pressurization, accomplishes whole circulation. The low-pressure steam waste heat is effectively utilized, and meanwhile, the expander works by utilizing the organic working medium for heating, so that the power generation efficiency is improved, and the utilization rate of the waste heat can be greatly improved.
Furthermore, a branch is further arranged at the outlet end of the low-pressure steam drum, and an adjusting valve is arranged on the branch. The heated steam is controlled to be delivered to the production life for use by adjusting valves, ensuring a proper supply of steam.
Further, the organic working medium is specifically one of pentafluoropropane, tetrafluoroethane, trifluorodichloroethane or isobutane. Different organic working media can correspond to different actual working conditions, and the reasonable selection of different organic working media is favorable for further improving the power generation efficiency.
Further, the expander is also coaxially connected with the generator. The expander is coaxially connected with the generator to drag the generator to generate electricity, and the operation efficiency of the expander is improved, namely the electricity generation efficiency of the generator is improved.
A double-working-medium Rankine cycle waste heat power generation method is characterized in that a high-pressure steam heat recovery system is used for recovering high-pressure steam in a double-evaporation-pressure waste heat boiler, a low-pressure steam heat recovery system is used for recovering low-pressure steam in the double-evaporation-pressure waste heat boiler, and the low-pressure steam heat recovery system is used for circularly heating an organic working medium to improve power generation efficiency. The steam waste heat is efficiently utilized, the double-evaporation-pressure waste heat boiler is adopted to carry out cascade recycling on the steam waste heat, compared with a single-evaporation-pressure waste heat boiler, the main steam parameters entering a steam turbine can be effectively improved, the power generation efficiency of the steam turbine is improved, and the waste heat utilization rate can be greatly improved by the aid of a Rankine cycle system and an organic Rankine cycle system containing water.
Further, the recycling of the high-pressure steam in the double-evaporation-pressure waste heat boiler by the high-pressure steam heat recovery system specifically comprises the following steps: the steam separated from the high-pressure steam pocket is superheated and then enters a turbine to generate power, the steam discharged by the turbine continuously releases partial steam condensation latent heat through a preheater, the steam enters a first condenser to continuously release heat and condense, condensed water is pressurized by a first condensed water pump to enter a first deaerator to be deaerated, and finally the condensed water is pressurized by a first circulating water pump to enter the high-pressure steam pocket. The waste heat of the high-pressure steam is effectively utilized, and the high quality of the steam entering the steam turbine is ensured.
Further, the recycling of the low-pressure steam in the double-evaporation-pressure waste heat boiler by the low-pressure steam heat recovery system specifically comprises the following steps: the low-pressure steam is separated by a low-pressure steam drum, and then is heated, and one path of steam is sent to production, living and other purposes by an adjusting valve; and the other path of condensed water enters the heat release side of the evaporator and is condensed after heat release, the condensed water enters a second deaerator for deaerating after being pressurized by a second condensed water pump, and the deaerated water is pressurized by a second circulating water pump and is sent into a low-pressure steam drum.
Further, the low-pressure steam heat recovery system improves the power generation efficiency by circularly heating the organic working medium and specifically comprises the following steps: the organic working medium absorbs the heat of the steam turbine exhaust through the preheater to preheat, the preheated organic working medium enters the evaporator to absorb the heat of low-pressure steam, the organic working medium is changed into high-pressure steam to enter the expander to expand and do work, the expander is coaxially connected with the generator to drag the generator to generate electricity, the organic working medium exhaust enters the second condenser to be condensed into liquid, then enters the working medium pump, enters the preheater after being pressurized, and the whole cycle is completed. The low-pressure steam waste heat is effectively utilized, and meanwhile, the expander works by utilizing the organic working medium for heating, so that the power generation efficiency is improved, and the utilization rate of the waste heat can be greatly improved.
A generator comprising a power generation system, wherein the power generation system is embodied as a dual-working-medium rankine cycle waste heat power generation system as described in any one of the above.
The utility model provides a pair of two working medium rankine cycle waste heat power generation systems and generator's beneficial effect lies in: (1) the double-working-medium-cycle waste heat power generation system comprises a Rankine cycle system containing water and an organic Rankine cycle system, and can greatly improve the waste heat utilization rate; (2) the steam waste heat is efficiently utilized, and the dual-evaporation-pressure waste heat boiler is adopted to carry out cascade recycling on the steam waste heat, so that compared with a single-evaporation-pressure waste heat boiler, the steam waste heat recycling device can effectively improve the parameters of main steam entering a steam turbine and improve the power generation efficiency of the steam turbine; (3) the steam used except the power generation system is distributed by the low-pressure steam system, the main steam flow of the steam turbine is kept unchanged, the rated working condition can be kept for long-term operation, the thermoelectric load change can be flexibly adjusted through the ORC system under the condition that the set is rated to meet the operation, and the thermoelectric utilization rate of the set is improved.
Drawings
Fig. 1 is a schematic diagram of the system structure of the present invention.
In the figure: 1. a double evaporation pressure waste heat boiler; 101. a high pressure steam drum; 102. a steam turbine; 103. a first condenser; 104. a first condensate pump; 105. a first deaerator; 106. a first circulating water pump; 201. a low pressure steam drum; 202. a second condensate pump; 203. a second deaerator; 204. a second circulating water pump; 205. adjusting a valve; 301. an expander; 302. a second condenser; 303. a working medium pump; 304. a preheater; 305. an evaporator.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. All other embodiments obtained by a person skilled in the art without any inventive step are within the scope of the present invention.
Example 1: a double-working-medium Rankine cycle waste heat power generation system.
A double-working-medium Rankine cycle waste heat power generation system comprises a double-evaporation-pressure waste heat boiler 1, a high-pressure steam heat recovery system and a low-pressure steam heat recovery system, wherein the high-pressure steam heat recovery system specifically comprises a high-pressure steam drum 101, a steam turbine 102, a first condenser 103, a first condensate pump 104, a first deaerator 105 and a first circulating water pump 106, the outlet end of the high-pressure steam drum 101 is connected with the inlet end of the steam turbine 102, the outlet end of the steam turbine 102 is connected with the inlet end of the first condenser 103, the outlet end of the first condenser 103 is connected with the inlet end of the first deaerator 105 through the first condensate pump 104, and the outlet end of the first deaerator 105 is connected with the inlet end of the high-pressure steam drum; the low-pressure steam heat recovery system specifically comprises a low-pressure steam drum 201, a second condensate pump 202, a second deaerator 203, a second circulating water pump 204, an expander 301, a second condenser 302, a working medium pump 303, a preheater 304 and an evaporator 305, the outlet end of the low-pressure steam drum 201 is connected with the inlet end of the evaporator 305, the outlet end of the evaporator 305 is connected with the inlet end of the second deaerator 203 through the second condensate pump 202, the outlet end of the second deaerator 203 is connected to the inlet end of the low-pressure steam drum 201 through the second circulating water pump 204, the inlet end of the preheater 304 is connected to the outlet end of the steam turbine 102, the outlet end of the preheater 304 is connected to the inlet end of the evaporator 305, the outlet end of the evaporator 305 is connected with the inlet end of the expansion machine 301, the outlet end of the expansion machine 301 is connected with the inlet end of the second condenser 302, the outlet end of the second condenser 302 is connected to the inlet end of the preheater 304 through the working medium pump 303; the outlet end of the low-pressure steam drum 201 is also provided with a branch, and the branch is provided with a regulating valve 205.
The working principle of the embodiment is as follows: steam Rankine cycle power generation process: the steam separated from the high-pressure steam drum 101 is superheated and then rushes to the steam turbine 102 to generate power, the steam discharged from the steam turbine 102 continuously releases partial steam condensation latent heat through the preheater 304, the steam enters the first condenser 103 to continuously release heat and condense, the condensed water is pressurized by the first condensed water pump 104 and enters the first deaerator 105 to be deaerated, and finally the condensed water is pressurized by the first circulating water pump 106 and enters the high-pressure steam drum 101.
ORC cycle power generation process: the ORC circulating power generation heat source is provided by low-pressure steam of the double-evaporation-pressure waste heat boiler 1, the low-pressure steam is separated by the low-pressure steam drum 201, and one path of steam after being heated is sent to production, living and other purposes through the regulating valve 205; the other path of the condensed water enters the heat release side of the evaporator 305 to be condensed after releasing heat, the condensed water enters the second deaerator 203 to be deaerated after being pressurized by the second condensed water pump 202, and the second deaerated water is pressurized by the second circulating water pump 204 and is sent to the low-pressure steam drum 201 of the boiler. The ORC cycle power generation system organic working medium pentafluoropropane absorbs the heat of the exhaust steam of the steam turbine 102 through the preheater 304 to be preheated, the preheated organic working medium pentafluoropropane enters the evaporator 305 to absorb the heat of the low-pressure steam, the preheated organic working medium pentafluoropropane is changed into high-pressure steam to enter the expansion machine 301 to do work through expansion, and the expansion machine 301 is coaxially connected with the generator to drag the generator to generate power. The exhausted gas of the organic working medium pentafluoropropane enters a second condenser 302 to be condensed into liquid, then enters a working medium pump 303, enters a preheater 304 after being pressurized, and the whole ORC cycle is completed.
The embodiment has the advantages that: adopt two evaporation pressure exhaust-heat boiler 1, retrieve high-pressure steam through high-pressure steam heat recovery system, low-pressure steam heat recovery system retrieves low-pressure steam, realizes the ladder grade recycle of steam waste heat, effectively utilizes steam waste heat, for single evaporation pressure exhaust-heat boiler, can effectively improve the main steam parameter that gets into steam turbine 102, improves steam turbine 102 generating efficiency.
Example 2: a double-working-medium Rankine cycle waste heat power generation method.
A double working medium Rankine cycle waste heat power generation method is characterized in that high-pressure steam in a double-evaporation-pressure waste heat boiler 1 is recycled through a high-pressure steam heat recovery system for utilization, the steam separated from a high-pressure steam drum 101 is superheated and then flows to a steam turbine 102 for power generation, steam discharged by the steam turbine 102 continues to release part of steam condensation latent heat through a preheater 304, the steam enters a first condenser 103 for continuous heat release and condensation, condensed water is pressurized by a first condensed water pump 104 and enters a first deaerator 105 for deaerating, and finally the condensed water is pressurized by a first circulating water pump 106 and enters the high-pressure steam drum 101. The waste heat of the high-pressure steam is effectively utilized, the high quality of the steam entering the steam turbine 102 is ensured, the low-pressure steam in the double-evaporation-pressure waste heat boiler 1 is recovered by the low-pressure steam heat recovery system for utilization, the low-pressure steam is separated by the low-pressure steam drum 201, and one path of hot steam is sent to production and living and other purposes through the regulating valve 205; another way gets into evaporimeter 305 exothermic side and condenses after giving out heat, the condensate water gets into second oxygen-eliminating device 203 deoxidization after the pressurization of second condensate pump 202, the deaerated water is sent into low pressure steam pocket 201 through the pressurization of second circulating water pump 204, low pressure steam heat recovery system still improves the generating efficiency through circulation heating organic working medium, organic working medium absorbs steam turbine 102 exhaust heat through pre-heater 304 and preheats, organic working medium after preheating gets into evaporimeter 305 and absorbs the heat of low pressure steam, will organic working medium becomes high pressure steam and gets into expander 301 expansion work, expander 301 and generator coaxial coupling, drags the generator electricity generation, and organic working medium exhaust gets into second condenser 302 condensation and becomes liquid, gets into working medium pump 303 afterwards, gets into pre-heater 304 after the pressurization, accomplishes whole circulation. The low-pressure steam waste heat is effectively utilized, and meanwhile, the expander 301 is heated by the organic working medium, so that the power generation efficiency is improved, and the utilization rate of the waste heat can be greatly improved.
In this embodiment, realized high-efficient utilization steam waste heat, adopted two evaporation pressure exhaust-heat boiler 1 to carry out the step recycle to steam waste heat, compare in single evaporation pressure exhaust-heat boiler, can effectively improve the main steam parameter that gets into steam turbine 102, improve steam turbine 102 power generation efficiency, contain aqueous rankine cycle system and organic rankine cycle system, can improve waste heat utilization by a wide margin.
Example 3: a generator is provided.
A generator comprising a power generation system, wherein the power generation system is embodied as a dual-working-medium rankine cycle waste heat power generation system as described in any one of embodiments 1.
The above description is a preferred embodiment of the present invention, but the present invention should not be limited to the disclosure of the embodiment and the accompanying drawings, and therefore, all equivalents and modifications that can be accomplished without departing from the spirit of the present invention are within the protection scope of the present invention.
Claims (7)
1. The double-working-medium Rankine cycle waste heat power generation system is characterized by comprising a double-evaporation-pressure waste heat boiler, a high-pressure steam heat recovery system and a low-pressure steam heat recovery system, wherein the high-pressure steam heat recovery system is used for recycling high-pressure steam waste heat, the low-pressure steam heat recovery system is used for recycling low-pressure steam waste heat, the high-pressure steam heat recovery system is a Rankine cycle system of water, and the low-pressure steam heat recovery system is a Rankine cycle system containing water and an organic working medium.
2. The dual-working-medium rankine cycle waste heat power generation system of claim 1, wherein: the high-pressure steam heat recovery system specifically comprises a high-pressure steam drum, a steam turbine, a first condenser, a first condensate pump, a first deaerator and a first circulating water pump, wherein the outlet end of the high-pressure steam drum is connected with the inlet end of the steam turbine, the outlet end of the steam turbine is connected with the inlet end of the first condenser, the outlet end of the first condenser is connected with the inlet end of the first deaerator through the first condensate pump, and the outlet end of the first deaerator is connected with the inlet end of the high-pressure steam drum through the first circulating water pump.
3. The dual mass rankine cycle waste heat power generation system of claim 2, wherein: the low-pressure steam heat recovery system specifically comprises a low-pressure steam drum, a second condensate pump, a second deaerator, a second circulating water pump, an expansion machine, a second condenser, a working medium pump, a preheater and an evaporator, wherein the outlet end of the low-pressure steam drum is connected with the inlet end of the evaporator, the outlet end of the evaporator is connected with the inlet end of the second deaerator through the second condensate pump, the outlet end of the second deaerator is connected with the inlet end of the low-pressure steam drum through the second circulating water pump, the inlet end of the preheater is connected with the outlet end of a steam turbine, the outlet end of the preheater is connected with the inlet end of the evaporator, the outlet end of the evaporator is connected with the inlet end of the expansion machine, the outlet end of the expansion machine is connected with the inlet end of the second condenser.
4. The dual mass rankine cycle waste heat power generation system of claim 3, wherein: the outlet end of the low-pressure steam drum is also provided with a branch, and the branch is provided with an adjusting valve.
5. The dual-working-medium rankine cycle waste heat power generation system of claim 1, wherein: the organic working medium is particularly one of pentafluoropropane, tetrafluoroethane, trifluorodichloroethane or isobutane.
6. The dual mass rankine cycle waste heat power generation system of claim 3, wherein: the expander is also coaxially connected with the generator.
7. A generator comprising a power generation system, characterized in that the power generation system is in particular a dual mass rankine cycle cogeneration system according to any of claims 1-6.
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110593977A (en) * | 2019-08-30 | 2019-12-20 | 珠海格力电器股份有限公司 | Dual-working-medium Rankine cycle waste heat power generation method and system and generator |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110593977A (en) * | 2019-08-30 | 2019-12-20 | 珠海格力电器股份有限公司 | Dual-working-medium Rankine cycle waste heat power generation method and system and generator |
| CN110593977B (en) * | 2019-08-30 | 2024-04-16 | 珠海格力电器股份有限公司 | Dual-working-medium Rankine cycle waste heat power generation method, system and power generator |
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