CN210464103U - Chemical industry condensate water recovery processing system - Google Patents
Chemical industry condensate water recovery processing system Download PDFInfo
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- CN210464103U CN210464103U CN201921226048.9U CN201921226048U CN210464103U CN 210464103 U CN210464103 U CN 210464103U CN 201921226048 U CN201921226048 U CN 201921226048U CN 210464103 U CN210464103 U CN 210464103U
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- steam turbine
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Abstract
The utility model provides a chemical industry condensate water recovery processing system, which comprises a flash chamber, a steam turbine and a generator; the flash evaporation chamber is used for collecting condensed water from chemical industry and carrying out flash evaporation treatment on the condensed water to generate high-temperature steam; the flash evaporation chamber is communicated with a steam turbine through a fluid conveying pipeline, the steam turbine is used for enabling a steam turbine rotor to rotate under the driving of high-temperature steam, and the generator rotor is fixedly connected with the steam turbine rotor and used for driving the generator to operate to generate electric energy through the rotation of the steam turbine rotor. Adopt the technical scheme of the utility model, the heat energy conversion that will deposit in the comdenstion water is the electric energy and supplies the user to use, makes the comdenstion water can reasonable recycle, has reduced the waste of resource to the low-temperature cooling water that forms after a series of processing to the high temperature comdenstion water is harmless to the environment, and avoids the direct emission of high temperature comdenstion water, has reduced the probability that peripheral personnel are scalded, has improved the security.
Description
Technical Field
The utility model belongs to the technical field of chemical industry comdenstion water processing apparatus, especially, relate to a chemical industry comdenstion water recovery processing system.
Background
At present, in the chemical industry production process, often can produce a large amount of comdenstion water, these a large amount of comdenstion water are often directly discharged by chemical enterprises, cause a large amount of wasting of resources, however, often contain a large amount of heat energy in these industry comdenstion water, consequently, urgent need research and development design a recycle system who recycles chemical industry comdenstion water.
SUMMERY OF THE UTILITY MODEL
In order to solve the technical problem, the utility model provides a chemical industry condensate water recovery processing system.
The utility model discloses a following technical scheme can realize.
The utility model provides a chemical industry condensate water recovery processing system, which comprises a flash chamber, a steam turbine and a generator;
a flash chamber: the system is used for collecting condensed water from chemical industry and carrying out flash evaporation treatment on the condensed water to generate high-temperature steam;
a steam turbine: the flash chamber is communicated with the steam turbine through a fluid conveying pipeline and is used for receiving high-temperature steam from the flash chamber and driving the steam turbine rotor to rotate through the high-temperature steam;
a generator: the generator rotor is fixedly connected with the turbine rotor and is used for driving the generator to operate to generate electric energy through rotation of the turbine rotor.
The number of the flash evaporation chambers is 2, and the 2 flash evaporation chambers are respectively communicated with the steam turbine through fluid conveying pipelines.
The 2 flash chambers are also in communication with each other by adjoining conduits.
The chemical industry condensate water recovery processing system also comprises a recovery tank, which is used for recovering cooling water formed after condensate water and high-temperature steam are used, and the recovery tank is communicated with the steam turbine or one of the flash chambers through a return pipe.
The number of the recovery tanks is 2.
The condensed water temperature was 100 ℃.
The beneficial effects of the utility model reside in that: adopt the technical scheme of the utility model, utilize flash distillation technique to form high temperature steam after gathering through chemical industry comdenstion water, rotate by high temperature steam drive steam turbine rotor again, thereby change the heat energy that contains in the comdenstion water into steam turbine rotor pivoted mechanical energy, then the steam turbine rotor orders about generator rotor through the rethread, the heat energy that contains in the comdenstion water in the future finally converts into the electric energy, for the user uses, make the comdenstion water can reasonable recycle, the waste of resource has been reduced, and the low temperature cooling water that forms after a series of processing to the high temperature comdenstion water is harmless to the environment, and avoid the direct emission of high temperature comdenstion water, the probability that peripheral personnel were scalded has been reduced, the security has been improved.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
Detailed Description
The technical solution of the present invention is further described below, but the scope of the claimed invention is not limited to the described.
As shown in fig. 1, the utility model provides a chemical industry condensate water recovery processing system, which comprises a flash chamber, a steam turbine and a generator;
a flash chamber: the system is used for collecting condensed water from chemical industry and carrying out flash evaporation treatment on the condensed water to generate high-temperature steam;
a steam turbine: the flash chamber is communicated with the steam turbine through a fluid conveying pipeline and is used for receiving high-temperature steam from the flash chamber and driving the steam turbine rotor to rotate through the high-temperature steam;
a generator: the generator rotor is fixedly connected with the turbine rotor and is used for driving the generator to operate to generate electric energy through rotation of the turbine rotor. The condensed water temperature was 100 ℃.
Adopt the technical scheme of the utility model, utilize flash distillation technique to form high temperature steam after gathering through chemical industry comdenstion water, rotate by high temperature steam drive steam turbine rotor again, thereby change the heat energy that contains in the comdenstion water into steam turbine rotor pivoted mechanical energy, then the steam turbine rotor orders about generator rotor through the rethread, the heat energy that contains in the comdenstion water in the future finally converts into the electric energy, for the user uses, make the comdenstion water can reasonable recycle, the waste of resource has been reduced, and the low temperature cooling water that forms after a series of processing to the high temperature comdenstion water is harmless to the environment, and avoid the direct emission of high temperature comdenstion water, the probability that peripheral personnel were scalded has been reduced, the security has been improved.
Further, the number of the flash evaporation chambers is 2, and the 2 flash evaporation chambers are respectively communicated with the steam turbine through fluid conveying pipelines. The 2 flash chambers are also in communication with each other by adjoining conduits. The 2 flash chambers are respectively used as a primary flash chamber and a secondary flash chamber.
In addition, the chemical industry condensate water recovery processing system also comprises a recovery tank, which is used for recovering cooling water formed after condensate water and high-temperature steam are used, and the recovery tank is communicated with the steam turbine or one of the flash chambers through a return pipe. The number of the recovery tanks is 2.
Claims (6)
1. The utility model provides a chemical industry comdenstion water recovery processing system which characterized in that: the device comprises a flash chamber, a steam turbine and a generator;
a flash chamber: the system is used for collecting condensed water from chemical industry and carrying out flash evaporation treatment on the condensed water to generate high-temperature steam;
a steam turbine: the flash chamber is communicated with the steam turbine through a fluid conveying pipeline and is used for receiving high-temperature steam from the flash chamber and driving the steam turbine rotor to rotate through the high-temperature steam;
a generator: the generator rotor is fixedly connected with the turbine rotor and is used for driving the generator to operate to generate electric energy through rotation of the turbine rotor.
2. The chemical industry condensate water recovery processing system of claim 1, wherein: the number of the flash evaporation chambers is 2, and the 2 flash evaporation chambers are respectively communicated with the steam turbine through fluid conveying pipelines.
3. The chemical industry condensate water recovery processing system of claim 2, wherein: the 2 flash chambers are also in communication with each other by adjoining conduits.
4. The chemical industry condensate water recovery processing system of claim 1, wherein: the chemical industry condensate water recovery processing system also comprises a recovery tank, which is used for recovering cooling water formed after condensate water and high-temperature steam are used, and the recovery tank is communicated with the steam turbine or one of the flash chambers through a return pipe.
5. The chemical industry condensate water recovery processing system of claim 4, wherein: the number of the recovery tanks is 2.
6. The chemical industry condensate water recovery processing system of claim 1, wherein: the condensed water temperature was 100 ℃.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921226048.9U CN210464103U (en) | 2019-07-31 | 2019-07-31 | Chemical industry condensate water recovery processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921226048.9U CN210464103U (en) | 2019-07-31 | 2019-07-31 | Chemical industry condensate water recovery processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210464103U true CN210464103U (en) | 2020-05-05 |
Family
ID=70448845
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921226048.9U Expired - Fee Related CN210464103U (en) | 2019-07-31 | 2019-07-31 | Chemical industry condensate water recovery processing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210464103U (en) |
-
2019
- 2019-07-31 CN CN201921226048.9U patent/CN210464103U/en not_active Expired - Fee Related
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20200505 Termination date: 20210731 |
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| CF01 | Termination of patent right due to non-payment of annual fee |