CN211950616U - Organic Rankine cycle power generation system capable of directly recycling black water waste heat - Google Patents
Organic Rankine cycle power generation system capable of directly recycling black water waste heat Download PDFInfo
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- CN211950616U CN211950616U CN202020477764.0U CN202020477764U CN211950616U CN 211950616 U CN211950616 U CN 211950616U CN 202020477764 U CN202020477764 U CN 202020477764U CN 211950616 U CN211950616 U CN 211950616U
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Abstract
The utility model relates to an organic Rankine cycle power generation system for directly recovering black water waste heat, which comprises an organic Rankine cycle power generation system consisting of an expander, a generator, an evaporator and a condenser, and further comprises a flash separator, a low-pressure flash tank and a preheater; the exhaust port of the expander is connected with the air inlet of the expander after sequentially passing through the first pipe of the condenser, the second pipe of the preheater and the second pipe of the evaporator; the expander is connected with the generator; the inlet of the first pipe of the evaporator is connected with the steam side outlet of the flash separator, and the outlet of the first pipe of the evaporator is connected with the low-pressure flash tank; the inlet of the first pipe of the preheater is connected with the water side outlet of the flash separator, and the outlet of the first pipe of the preheater is emptied; and a second pipe of the condenser is connected with the cooling tower to form a closed-loop cooling circulation. The utility model discloses can retrieve waste heat in black steam and the black water liquid simultaneously to provide organic rankine cycle power generation system and generate electricity, improved the utilization ratio of the energy.
Description
Technical Field
The utility model relates to a heat energy device, especially a power generation system, specific organic rankine cycle power generation system who directly retrieves black water waste heat that says so.
Background
For the black water waste heat recovery, the current common method is that black water passes through a high-pressure flash tank to generate black water flash steam, the black water flash steam is cooled into condensate through a cooler, and the condensate enters a low-pressure flash tank for recycling. In the way, the waste heat of the black water flash steam is in a waste state, so that not only is no economic benefit generated, but also a large amount of circulating cooling water is consumed.
Therefore, there is a need for improvement of the existing black water utilization method to improve the utilization efficiency of energy.
SUMMERY OF THE UTILITY MODEL
The utility model aims at the current not high problem of black water utilization efficiency, improve an organic rankine cycle power generation system who directly retrieves black water waste heat, can retrieve waste heat in black steam and the black water liquid simultaneously to provide organic rankine cycle power generation system and generate electricity, convert the waste heat of low grade into high-grade electric energy, improved the utilization ratio of the energy.
The technical scheme of the utility model is that:
an organic Rankine cycle power generation system for directly recovering black water waste heat comprises an organic Rankine cycle power generation system consisting of an expander, a generator, an evaporator and a condenser, and further comprises a flash separator, a low-pressure flash tank and a preheater; the exhaust port of the expander is connected with the air inlet of the expander after sequentially passing through the first pipe of the condenser, the second pipe of the preheater and the second pipe of the evaporator; the expander is connected with the generator; the inlet of the first pipe of the evaporator is connected with the steam side outlet of the flash separator, and the outlet of the first pipe of the evaporator is connected with the low-pressure flash tank; the inlet of the first pipe of the preheater is connected with the water side outlet of the flash separator, and the outlet of the first pipe of the preheater is emptied; and a second pipe of the condenser is connected with the cooling tower to form a closed-loop cooling circulation.
Furthermore, the number of the preheaters is two, and the preheaters are connected in parallel.
Further, the device also comprises a cooler, wherein the inlet of the cooler is connected with the steam side outlet of the flash separator, and the outlet of the cooler is connected with the low-pressure flash tank.
Furthermore, a working medium pump is arranged between the condenser and the preheater.
Furthermore, valves are respectively arranged at the inlet end of the first pipe of the preheater and the inlet end of the second pipe of the preheater; valves are respectively arranged at two ends of the first pipe of the evaporator; and valves are respectively arranged at two ends of the cooler.
Furthermore, two ends of the first pipe of the preheater and two ends of the second pipe of the preheater are respectively provided with a bypass which is connected in parallel; and each bypass is provided with a valve.
Further, the system also comprises a heat regenerator; the second tube of the regenerator is connected in series between the expander and the condenser, and the first tube of the regenerator is connected in series between the condenser and the preheater.
The utility model has the advantages that:
the utility model relates to a rationally, simple structure, control is convenient, can retrieve waste heat in black steam and the black water liquid simultaneously to provide organic rankine cycle power generation system and generate electricity, convert the waste heat of low grade into high-grade electric energy, improved the utilization ratio of the energy.
Drawings
Fig. 1 is a schematic diagram of a system structure according to a first embodiment of the present invention.
Fig. 2 is a schematic diagram of a system structure according to a second embodiment of the present invention.
Wherein: 1-a flash separator; 2-valve I; 3-a cooler; 4-valve II; 5-low pressure flash tank; 6-valve III; 7-an evaporator; 8-valve IV; 9-valve V; 10-valve VI; 11-valve VII; 12-valve VIII; 13-preheater I; 14-valve IX; 15-preheater II; 16-valve X; 17-valve XI; 18-valve XII; 19-an expander; 20-a generator; 21-a condenser; 22-working medium pump; 23-a cooling water pump; 24-a cooling tower; 25-regenerator. The arrows in the figure indicate the medium flow direction.
Detailed Description
The present invention will be further described with reference to the accompanying drawings and examples.
Embodiment one, as shown in fig. 1.
An organic Rankine cycle power generation system capable of directly recovering waste heat of black water comprises a flash separator 1, a cooler 3, a low-pressure flash tank 5, an evaporator 7, a preheater I13, a preheater II15, an expansion machine 19, a power generator 20, a condenser 21 and a cooling tower 24. An exhaust port of the expander 19 is connected with an air inlet of the expander 19 after sequentially passing through the first pipe of the condenser 21, the working medium pump 22, the second pipe of the preheater II15, the second pipe of the preheater I13 and the second pipe of the evaporator 7, and meanwhile, the expander 19 is connected with the generator 20, so that an organic rankine cycle power generation system is formed. The inlet of the first pipe of the evaporator 7 is connected with the steam side outlet of the flash separator 1, and the outlet of the first pipe is connected with the low-pressure flash tank 5. The inlet of the first pipe of the preheater I13 is connected to the water side outlet of the flash separator 1, and its outlet is connected to the inlet of the first pipe of the preheater II 15. The outlet of the first pipe of this preheater II15 was vented. The second pipe of the condenser 21 is connected to a cooling tower 24 to form a closed loop cooling cycle.
Further, the system also comprises a cooler 3, the inlet of which is connected with the steam side outlet of the flash separator 1, and the outlet of which is connected with the low-pressure flash tank 5. The inlet and outlet ends of the cooler 3 are provided with a valve I2 and a valve II4, respectively.
Further, the inlet end and the outlet end of the first pipe of the evaporator 7 are respectively provided with a valve III6 and a valve IV 8. The inlet end of the first pipe of the preheater I13 is provided with a valve VII 11. The inlet end of the first pipe of the preheater II115 is provided with a valve VIII 12. A bypass I is arranged at two ends of the first pipe of the preheater I13 and is connected with the first pipe in parallel, and a valve V9 is arranged on the bypass I. And two ends of the first pipe of the preheater II15 are provided with a bypass II connected with the first pipe in parallel, and the bypass II is provided with a valve VI 10. The inlet end of the second pipe of the preheater I13 is provided with a valve IX 14. The inlet end of the second pipe of the preheater II15 is provided with a valve X16. And a bypass III connected with the two ends of the second pipe of the preheater I13 in parallel is arranged at the two ends of the second pipe, and a valve XI17 is arranged on the bypass III. And two ends of the second pipe of the preheater II15 are provided with a bypass IV in parallel connection with the second pipe, and the bypass IV is provided with a valve XII 18.
Preferably, the flash separator adopts an SZ-2 type medium temperature flash separator. The evaporator adopts a BXM type flooded shell-and-tube heat exchanger. The condenser, the cooler, the preheater I and the preheater II all adopt BEM type one-way shell head-sealed tube box type heat exchangers. Working media in the organic Rankine cycle loop are organic working media such as R134a and R245 fa.
The utility model discloses a working process does:
during normal operation, the valve I2 and the valve II4 are closed, the valve III6 and the valve IV8 are opened, the black water generates black water flash steam and black water liquid through the flash separator, the black water flash steam enters the evaporator, the black water liquid enters the preheater I or the preheater II, the steam waste heat and the liquid waste heat are enabled to participate in heat exchange of the working medium in the organic Rankine cycle, the temperature of the working medium is improved, and the whole recovery of the black water waste heat is achieved. The black water flash steam contains a certain component of corrosive gas, so the evaporator is preferably made of corrosion-resistant stainless steel. The black water liquid contains impurities with certain components, so that the operation switching of the preheater I and the preheater II can be realized through the valve switching, and the overhauling and maintenance of the preheater are facilitated. The method specifically comprises the following steps: when the preheater I operates, the valve VI and the valve VII are opened, the valve V and the valve VIII are closed, and the black water liquid enters the preheater I for heat exchange. And the black water liquid after heat exchange enters a low-pressure flash tank for recovery. Meanwhile, a valve IX14 and a valve XII18 are opened, a valve X16 and a valve XI17 are closed, so that the working medium is pressurized by the working medium pump to enter the preheater I, and enters the evaporator after being subjected to heat exchange with the black water liquid. At this time, the preheater II can be repaired and maintained. When the preheater II is in operation, the valve V9 and the valve VIII12 are opened, the valve VI10 and the valve VII11 are closed, and the black water liquid enters the preheater II for heat exchange. And the black water liquid after heat exchange enters a low-pressure flash tank for recovery. Meanwhile, a valve X16 and a valve XI17 are opened, a valve IX14 and a valve XII18 are closed, so that the working medium is pressurized by the working medium pump to enter a preheater II, and enters an evaporator after being subjected to heat exchange with the black water liquid. At this time, the preheater I can be repaired and maintained. The working medium enters the evaporator after coming out of the preheater, is further heated by exchanging heat with the black water vapor, and is changed into gas from liquid, so that the expansion machine is pushed to do work, and the generator is driven to generate power. The expander adopts a turbine and has higher power generation efficiency. And the working medium gas which does work is discharged from the expansion machine, enters the condenser, exchanges heat with cooling water to be cooled into liquid, and enters the working medium pump to complete the whole organic Rankine cycle. And cooling the high-temperature cooling water subjected to heat exchange by the cooling tower, and then entering the cooling water pump to complete cooling circulation. When the organic Rankine cycle power generation system is overhauled and maintained, the valve I2 and the valve II4 are opened, the valve III6 and the valve IV8 are closed, the black water flash steam enters the cooler after coming out of the flash separator, and the condensed water after heat exchange enters the low-pressure flash tank, so that the maintenance of the power generation system is more convenient.
Example two, as shown in fig. 2.
The second embodiment is basically the same as the first embodiment in structure, and the main difference is that: the second embodiment further comprises a heat regenerator; the second tube of the regenerator is connected in series between the expander and the first tube of the condenser, and the first tube of the regenerator is connected in series between the condenser and the preheater. When the organic Rankine cycle system operates, working medium gas which does work is discharged from the expansion machine, enters the heat regenerator to exchange heat with liquid working medium, enters the condenser to be cooled into liquid, so that the liquid working medium can be preheated, and the efficiency of the organic Rankine cycle system is improved. Meanwhile, the heat of the exhaust of the expansion machine can be fully recovered, and the energy utilization rate is improved.
The utility model discloses the part that does not relate to all is the same with prior art or can adopt prior art to realize.
Claims (7)
1. An organic Rankine cycle power generation system for directly recovering black water waste heat comprises an organic Rankine cycle power generation system consisting of an expander, a generator, an evaporator and a condenser, and is characterized in that: the system also comprises a flash separator, a low-pressure flash tank and a preheater; the exhaust port of the expander is connected with the air inlet of the expander after sequentially passing through the first pipe of the condenser, the second pipe of the preheater and the second pipe of the evaporator; the expander is connected with the generator; the inlet of the first pipe of the evaporator is connected with the steam side outlet of the flash separator, and the outlet of the first pipe of the evaporator is connected with the low-pressure flash tank; the inlet of the first pipe of the preheater is connected with the water side outlet of the flash separator, and the outlet of the first pipe of the preheater is emptied; and a second pipe of the condenser is connected with the cooling tower to form a closed-loop cooling circulation.
2. The organic Rankine cycle power generation system for directly recovering waste heat of black water according to claim 1, wherein: the number of the preheaters is two, and the preheaters are connected in parallel.
3. The organic Rankine cycle power generation system for directly recovering waste heat of black water according to claim 1, wherein: the inlet of the cooler is connected with the steam side outlet of the flash separator, and the outlet of the cooler is connected with the low-pressure flash tank.
4. The organic Rankine cycle power generation system for directly recovering waste heat of black water according to claim 1, wherein: and a working medium pump is arranged between the condenser and the preheater.
5. The organic Rankine cycle power generation system for directly recovering waste heat of black water according to claim 3, wherein: the inlet end of the first pipe of the preheater and the inlet end of the second pipe of the preheater are respectively provided with a valve; valves are respectively arranged at two ends of the first pipe of the evaporator; and valves are respectively arranged at two ends of the cooler.
6. The organic Rankine cycle power generation system for directly recovering waste heat of black water according to claim 1, wherein: two ends of the first pipe of the preheater and two ends of the second pipe of the preheater are respectively provided with a bypass which is connected in parallel; and each bypass is provided with a valve.
7. The organic Rankine cycle power generation system for directly recovering waste heat of black water according to claim 1, wherein: the system also comprises a heat regenerator; the second tube of the regenerator is connected in series between the expander and the condenser, and the first tube of the regenerator is connected in series between the condenser and the preheater.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111287816A (en) * | 2020-04-03 | 2020-06-16 | 南京天加热能技术有限公司 | Organic Rankine cycle power generation system capable of directly recycling black water waste heat |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111287816A (en) * | 2020-04-03 | 2020-06-16 | 南京天加热能技术有限公司 | Organic Rankine cycle power generation system capable of directly recycling black water waste heat |
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Address after: No. 2 Hengxiang Road, Nanjing Economic and Technological Development Zone, Nanjing, Jiangsu Province, 210000 Patentee after: Nanjing Tianjia Energy Technology Co.,Ltd. Patentee after: NANJING CHENGZHI CLEAN ENERGY Co.,Ltd. Address before: 210046 No.6 Hengye Road, Nanjing Economic and Technological Development Zone, Jiangsu Province Patentee before: Nanjing tianheating Technology Co.,Ltd. Patentee before: NANJING CHENGZHI CLEAN ENERGY Co.,Ltd. |