CN206203934U - With the double mode condensate polishing treatment runtime of heat supply and pure condensate - Google Patents

With the double mode condensate polishing treatment runtime of heat supply and pure condensate Download PDF

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Publication number
CN206203934U
CN206203934U CN201621237838.3U CN201621237838U CN206203934U CN 206203934 U CN206203934 U CN 206203934U CN 201621237838 U CN201621237838 U CN 201621237838U CN 206203934 U CN206203934 U CN 206203934U
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CN
China
Prior art keywords
condensate
runtime
heat supply
cooling water
double mode
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201621237838.3U
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Chinese (zh)
Inventor
李敏
陈哲
阿不都克里木.阿布来提
邓赟
高明
黄献华
汪生彪
胡小梅
宋涛
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Xinjiang Huadian Kashi thermoelectric limited liability company
Original Assignee
SHANDONG HONGAO ELECTRIC POWER TECHNOLOGY Co Ltd
Xinjiang Huadian Kashi Thermoelectric LLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by SHANDONG HONGAO ELECTRIC POWER TECHNOLOGY Co Ltd, Xinjiang Huadian Kashi Thermoelectric LLC filed Critical SHANDONG HONGAO ELECTRIC POWER TECHNOLOGY Co Ltd
Priority to CN201621237838.3U priority Critical patent/CN206203934U/en
Application granted granted Critical
Publication of CN206203934U publication Critical patent/CN206203934U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model is related to a kind of thermal power plant condensate polishing system, particularly discloses a kind of condensate polishing treatment runtime double mode with heat supply and pure condensate.This has heat supply and the double mode condensate polishing treatment runtime of pure condensate, including former precision processing system, it is characterised in that:The former precision processing system connects the delivery port of heat exchanger by condensate outlet conduit, and the water inlet of heat exchanger connects condenser, by-pass line is connected between condensate inlet channel and condensate outlet conduit by condensate inlet channel.The utility model simple structure, it is easy to use, it is reasonable in design, using flexible, effectively solve high back pressure thermal power plant unit condensing water temperature too high, the problem that condensed water precision processing system cannot run, while avoiding the defect that prior art one-time investment is big, operation and maintenance cost is high.

Description

With the double mode condensate polishing treatment runtime of heat supply and pure condensate
(One)Technical field
The utility model is related to a kind of thermal power plant condensate polishing system, more particularly to a kind of to have heat supply and pure condensate Double mode condensate polishing treatment runtime.
(Two)Background technology
Management with country to atmosphere pollution is increased and the popularization to energy-saving and emission-reduction project, and high back pressure recirculated water is supplied Heat has been the emphasis energy-saving and emission-reduction project that power industry is promoted in central heating area.
High back pressure circulating water heating project heats heat supply network recirculated water and reaches recovery turbine discharge to improve exhaust steam pressure The purpose of cold source energy, because greatly improving for exhaust steam pressure causes condensing water temperature significantly to raise, so that former condensate fine Processing system inlet water temperature degree exceedes system requirements, it is impossible to normal operation.
To solve this problem, original condensed water precision processing system should be transformed.Modification scheme before is replacing High-temperature resin(The patent No.:2013107185521), though this problem can be solved, bring that one-time investment is big, the resin longevity simultaneously Order shorter, operation and maintenance cost defect high.
(Three)The content of the invention
The utility model is in order to make up the deficiencies in the prior art, there is provided a kind of simple structure, operating cost are low to be had Heat supply and the double mode condensate polishing treatment runtime of pure condensate.
The utility model is achieved by the following technical solution:
A kind of condensate polishing treatment runtime double mode with heat supply and pure condensate, including former precision processing system, it is special Levy and be:The former precision processing system connects the delivery port of heat exchanger, the water inlet of heat exchanger by condensate outlet conduit Mouth connects condenser by condensate inlet channel, and bypass pipe is connected between condensate inlet channel and condensate outlet conduit Road.
The utility model increases a heat exchanger before agglutinating water enters former precision processing system, to reduce the temperature of condensate Degree;The summer that is provided for of by-pass line is opened, and makes condensate around over-heat-exchanger, and former precision processing is directly entered without condensation System.
More excellent technical scheme of the present utility model is:
Cooling water inlet pipe and cooling water outlet pipe are connected with the heat exchanger, it is cold between being connected with cooling water inlet pipe Tower recirculated water backwater, cooling water outlet pipe connection indirect cool tower recirculated water feed water inlet, realizes the cycling and reutilization of cooling water, is easy to section The about energy.
Valve is mounted on the condensate outlet conduit, condensate inlet channel and by-pass line;By valve control The opening and closing of the flow and by-pass line of condensate processed.
Valve is mounted on the cooling water inlet pipe and cooling water outlet pipe, by the stream of valve regulated cooling water Amount, controls condensing water temperature.
The utility model simple structure, it is easy to use, it is reasonable in design, using flexible, effectively solve high back pressure thermal power plant unit Condensing water temperature is too high, the problem that condensed water precision processing system cannot run, while avoiding that prior art one-time investment is big, fortune Row maintenance cost defect high.
(Four)Brief description of the drawings
The utility model is further described below in conjunction with the accompanying drawings.
Fig. 1 is structural representation of the present utility model.
In figure, 1 former precision processing system, 2 condensate outlet conduits, 3 heat exchangers, 4 condensate inlet channels, 5 condensers, 6 by-pass lines, 7 cooling water inlet pipes, 8 cooling water outlet pipes, 9 valves.
(Five)Specific embodiment
Accompanying drawing is a kind of specific embodiment of the present utility model.The embodiment includes former precision processing system 1, at the former essence Reason system 1 connects the delivery port of heat exchanger 3 by condensate outlet conduit 2, and the water inlet of heat exchanger 3 is entered by condensate Waterpipe 4 connects condenser 5, and by-pass line 6 is connected between condensate inlet channel 4 and condensate outlet conduit 2;The heat It is connected with exchanger 3 and indirect cool tower recirculated water time is connected with cooling water inlet pipe 7 and cooling water outlet pipe 8, cooling water inlet pipe 7 Water, the connection indirect cool tower recirculated water of cooling water outlet pipe 8 feed water inlet;The condensate outlet conduit 2, the and of condensate inlet channel 4 Valve 9 is mounted on by-pass line 6;Valve 9 is mounted on the cooling water inlet pipe 7 and cooling water outlet pipe 8.
When the Winter heat supply phase is run, the valve 9 on cooling water inlet pipe 7 and cooling water outlet pipe 8 is opened, in heat exchanger Cooling water is passed through in 3, the valve 9 on condensate outlet conduit 2 and condensate inlet channel 4 is opened, closed on by-pass line 6 Valve 9, before condensate enters former precision processing system 1 being first passed through heat exchanger 3 is exchanged heat, and condensate is controlled by control valve 9 Temperature is in rational scope.
When the non-heat supply phase is run, cold water inlet 7, cooling water outlet pipe 8, condensate outlet conduit 2 and condensate are closed Valve 9 on inlet channel 4, opens the valve 9 on by-pass line 6, makes condensate not carry out exchanging heat directly around over-heat-exchanger 3 Into former precision processing system 1.

Claims (4)

1. a kind of condensate polishing treatment runtime double mode with heat supply and pure condensate, including former precision processing system(1), it is special Levy and be:The former precision processing system(1)By condensate outlet conduit(2)Connection heat exchanger(3)Delivery port, heat exchange Device(3)Water inlet pass through condensate inlet channel(4)Connection condenser(5), condensate inlet channel(4)With condensate water outlet Pipeline(2)Between be connected with by-pass line(6).
2. the condensate polishing treatment runtime double mode with heat supply and pure condensate according to claim 1, its feature exists In:The heat exchanger(3)On be connected with cooling water inlet pipe(7)And cooling water outlet pipe(8), cooling water inlet pipe(7)It is interior It is connected with indirect cool tower recirculated water backwater, cooling water outlet pipe(8)Connection indirect cool tower recirculated water feed water inlet.
3. the condensate polishing treatment runtime double mode with heat supply and pure condensate according to claim 1, its feature exists In:The condensate outlet conduit(2), condensate inlet channel(4)And by-pass line(6)On be mounted on valve(9).
4. the condensate polishing treatment runtime double mode with heat supply and pure condensate according to claim 2, its feature exists In:The cooling water inlet pipe(7)And cooling water outlet pipe(8)On be mounted on valve(9).
CN201621237838.3U 2016-11-18 2016-11-18 With the double mode condensate polishing treatment runtime of heat supply and pure condensate Expired - Fee Related CN206203934U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621237838.3U CN206203934U (en) 2016-11-18 2016-11-18 With the double mode condensate polishing treatment runtime of heat supply and pure condensate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621237838.3U CN206203934U (en) 2016-11-18 2016-11-18 With the double mode condensate polishing treatment runtime of heat supply and pure condensate

Publications (1)

Publication Number Publication Date
CN206203934U true CN206203934U (en) 2017-05-31

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621237838.3U Expired - Fee Related CN206203934U (en) 2016-11-18 2016-11-18 With the double mode condensate polishing treatment runtime of heat supply and pure condensate

Country Status (1)

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CN (1) CN206203934U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107120713A (en) * 2017-06-16 2017-09-01 华电郑州机械设计研究院有限公司 A kind of anti-overtemperature cooling system of high back pressure thermal power plant unit condensate

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107120713A (en) * 2017-06-16 2017-09-01 华电郑州机械设计研究院有限公司 A kind of anti-overtemperature cooling system of high back pressure thermal power plant unit condensate
CN107120713B (en) * 2017-06-16 2022-09-13 华电郑州机械设计研究院有限公司 High back pressure heat supply unit condensate water prevents super temperature cooling system

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Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CB03 Change of inventor or designer information

Inventor after: Li Min

Inventor after: Song Tao

Inventor after: Chen Zhe

Inventor after: Abdukerim Ablet

Inventor after: Deng Bin

Inventor after: Maimaiti Tokoti

Inventor after: Gao Ming

Inventor after: Huang Xianhua

Inventor after: Wang Shengbiao

Inventor after: Hu Xiaomei

Inventor before: Li Min

Inventor before: Chen Zhe

Inventor before: Abdul Kerim ablet.

Inventor before: Deng Bin

Inventor before: Gao Ming

Inventor before: Huang Xianhua

Inventor before: Wang Shengbiao

Inventor before: Hu Xiaomei

Inventor before: Song Tao

CB03 Change of inventor or designer information
TR01 Transfer of patent right

Effective date of registration: 20171117

Address after: Shenzhen Kashi Economic Development Zone Industrial Park 844000 the Xinjiang Uygur Autonomous Region Kashi two road Shenka areas of entrepreneurship and entrepreneurship Service Center

Patentee after: Xinjiang Huadian Kashi thermoelectric limited liability company

Address before: Shenzhen Kashi Economic Development Zone Industrial Park 844000 the Xinjiang Uygur Autonomous Region Kashi two road Shenka areas of entrepreneurship and entrepreneurship Service Center

Co-patentee before: Shandong Hongao Electric Power Technology Co., Ltd.

Patentee before: Xinjiang Huadian Kashi thermoelectric limited liability company

TR01 Transfer of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170531

Termination date: 20171118

CF01 Termination of patent right due to non-payment of annual fee