CN205717148U - A kind of boiler steam temperature regulation system - Google Patents

A kind of boiler steam temperature regulation system Download PDF

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Publication number
CN205717148U
CN205717148U CN201620631006.3U CN201620631006U CN205717148U CN 205717148 U CN205717148 U CN 205717148U CN 201620631006 U CN201620631006 U CN 201620631006U CN 205717148 U CN205717148 U CN 205717148U
Authority
CN
China
Prior art keywords
group
water
heat exchanger
low temperature
reheater
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
CN201620631006.3U
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Chinese (zh)
Inventor
薛朝囡
石慧
刘安
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.)
Xian Thermal Power Research Institute Co Ltd
Huaneng Group Technology Innovation Center Co Ltd
Original Assignee
Xian Thermal Power Research Institute Co Ltd
Huaneng Group Technology Innovation Center Co Ltd
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.)
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Application filed by Xian Thermal Power Research Institute Co Ltd, Huaneng Group Technology Innovation Center Co Ltd filed Critical Xian Thermal Power Research Institute Co Ltd
Priority to CN201620631006.3U priority Critical patent/CN205717148U/en
Application granted granted Critical
Publication of CN205717148U publication Critical patent/CN205717148U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model discloses a kind of boiler steam temperature regulation system, including superheater group and reheater group, the some vapor of superheater group and the superheated steam of reheater group and reheated steam outlet is connected to water at low temperature heat exchanger, water at low temperature heat exchanger is parallel to economizer, when overheated vapour is by superheater group, not only by overheated attemperator, also part accesses water at low temperature heat exchanger, when reheating vapour is by reheater group, not only by reheating attemperator, also part accesses water at low temperature heat exchanger, a feedwater part passes through economizer, it is partly into water at low temperature heat exchanger, in water at low temperature heat exchanger, respectively superheated steam and reheated steam are carried out heat exchange, final and economizer exit assemble jamming is to subordinate's heater.This utility model can equalize the temperature between different heating surface, it is possible to the heat exchange amount between the different heating surfaces such as regulation radiation, convection current, improves coal, the adaptability of load, reduces the energy loss during temperature regulation.

Description

A kind of boiler steam temperature regulation system
[technical field]
This utility model belongs to field of thermal power, is specifically related to a kind of boiler steam temperature regulation system.
[background technology]
The regulative mode of vapor (steam) temperature is broadly divided into two big classes: fume side regulates and steam tempering.During fume side regulation, The general modes such as regulating burner pivot angle, flue gas recirculation, regulation gas baffle that uses, the degree of regulation of vapor (steam) temperature is poor; Mainly using the mode of attemperator during steam tempering, temperature regulation is the finest.General two ways uses, with flue gas simultaneously Side regulation carrys out coarse adjustment as thermoregulator major way, using steam tempering as thin tuning, thus reaches boiler export The purpose of vapor (steam) temperature regulation.
But, limited by boiler structure, fume side regulation range of accommodation limited, especially when coal type change scope relatively Time big, regulation more difficulty.Along with the development of current energy-saving and emission-reduction situation, steam turbine reformation proposes significantly change feed temperature Demand, also to boiler steam temperature regulation propose requirements at the higher level.
And steam tempering is due to needs desuperheating water, unit recycling economy there is considerable influence.
[utility model content]
The purpose of this utility model is to overcome above-mentioned deficiency, it is provided that a kind of boiler steam temperature regulation system, can not only Enough fine regulation vapor (steam) temperatures, and can adapt to the various factors change impacts such as coal, load, feed temperature, and reduce The energy loss caused because of desuperheating water regulation temperature.
In order to achieve the above object, this utility model includes superheater group and reheater group, superheater group and reheater group Superheated steam and reheated steam outlet some vapor be connected to water at low temperature heat exchanger, water at low temperature heat exchanger is parallel to province's coal Device.
It is provided with overheated desuperheating water between described superheater group and water at low temperature heat exchanger.
It is provided with reheating desuperheating water between described reheater group and water at low temperature heat exchanger.
Described superheater group accesses overheated vapour.
Described reheater group accesses reheating vapour.
Described superheater group, reheater group and economizer are placed in exhaust gases passes.
Described superheater group includes that multiple superheater, reheater group include multiple reheater.
Compared with prior art, the steam in this utility model passes through superheater group and reheater group is by water at low temperature heat exchanger In water heating after, make own temperature reduce, thus reach regulation vapor (steam) temperature purpose, this utility model can equalize difference Temperature between heating surface, it is possible to the heat exchange amount between the different heating surfaces such as regulation radiation, convection current, improves coal, the adaptability of load, Reduce the energy loss during temperature regulation.
Further, this utility model is still provided with desuperheating water, it is possible to when, temperature not enough in heat exchange is too high, to steam Lower the temperature.
[accompanying drawing explanation]
Fig. 1 is structural representation of the present utility model.
[detailed description of the invention]
Below in conjunction with the accompanying drawings this utility model is described further.
Seeing Fig. 1, this utility model includes the overheated of superheater group 1 and reheater group 2, superheater group 1 and reheater group 2 The some vapor of steam and reheated steam outlet is connected to water at low temperature heat exchanger 3, and water at low temperature heat exchanger 3 is parallel to economizer 4, mistake It is provided with overheated desuperheating water 5 between hot device group 1 and water at low temperature heat exchanger 3, is provided with again between reheater group 2 and water at low temperature heat exchanger 3 Hot desuperheating water 6, superheater group 1 accesses overheated vapour, and reheater group 2 accesses reheating vapour, superheater group 1, reheater group 2 and economizer 4 are placed in exhaust gases passes, and superheater group 1 includes that multiple superheater, reheater group 2 include multiple reheater.
Method of work of the present utility model, when overheated vapour is by superheater group 1, not only by overheated attemperator 5, also part Accessing water at low temperature heat exchanger 3, when reheating vapour is by reheater group 2, not only by reheating attemperator 6, also part accesses water at low temperature Heat exchanger 3, a feedwater part, by economizer 4, is partly into water at low temperature heat exchanger 3, the most right in water at low temperature heat exchanger 3 Superheated steam and reheated steam carry out heat exchange, and final and economizer exit assemble jamming is to subordinate's heater;By the mistake after heat exchange Vapours eventually flows to next equipment;Next equipment is eventually flowed to by the reheated steam after heat exchange.

Claims (7)

1. a boiler steam temperature regulation system, it is characterised in that: include superheater group (1) and reheater group (2), superheater The some vapor of group (1) and the superheated steam of reheater group (2) and reheated steam outlet is connected to water at low temperature heat exchanger (3), low Warm water heat exchanger (3) is parallel to economizer (4).
A kind of boiler steam temperature regulation system the most according to claim 1, it is characterised in that: described superheater group (1) And it is provided with overheated desuperheating water (5) between water at low temperature heat exchanger (3).
A kind of boiler steam temperature regulation system the most according to claim 1, it is characterised in that: described reheater group (2) And it is provided with reheating desuperheating water (6) between water at low temperature heat exchanger (3).
A kind of boiler steam temperature regulation system the most according to claim 1, it is characterised in that: described superheater group (1) Access overheated vapour.
A kind of boiler steam temperature regulation system the most according to claim 1, it is characterised in that: described reheater group (2) Access reheating vapour.
A kind of boiler steam temperature regulation system the most according to claim 1, it is characterised in that: described superheater group (1), Reheater group (2) and economizer (4) are placed in exhaust gases passes.
A kind of boiler steam temperature regulation system the most according to claim 1, it is characterised in that: described superheater group (1) Including multiple superheaters, reheater group (2) includes multiple reheater.
CN201620631006.3U 2016-06-22 2016-06-22 A kind of boiler steam temperature regulation system Expired - Fee Related CN205717148U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620631006.3U CN205717148U (en) 2016-06-22 2016-06-22 A kind of boiler steam temperature regulation system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620631006.3U CN205717148U (en) 2016-06-22 2016-06-22 A kind of boiler steam temperature regulation system

Publications (1)

Publication Number Publication Date
CN205717148U true CN205717148U (en) 2016-11-23

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620631006.3U Expired - Fee Related CN205717148U (en) 2016-06-22 2016-06-22 A kind of boiler steam temperature regulation system

Country Status (1)

Country Link
CN (1) CN205717148U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105953205A (en) * 2016-06-22 2016-09-21 西安热工研究院有限公司 Boiler steam temperature adjusting system and working method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105953205A (en) * 2016-06-22 2016-09-21 西安热工研究院有限公司 Boiler steam temperature adjusting system and working method

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20161123

Termination date: 20170622