CN207776919U - A kind of Water vapour images for coagulating gas formula boiler - Google Patents

A kind of Water vapour images for coagulating gas formula boiler Download PDF

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Publication number
CN207776919U
CN207776919U CN201721759942.3U CN201721759942U CN207776919U CN 207776919 U CN207776919 U CN 207776919U CN 201721759942 U CN201721759942 U CN 201721759942U CN 207776919 U CN207776919 U CN 207776919U
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China
Prior art keywords
attemperator
pressure heater
connects
boiler
feed pump
Prior art date
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Application number
CN201721759942.3U
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Chinese (zh)
Inventor
张红刚
刘富强
李红民
任刚
吴谋新
杨华斌
黄书芳
余凯
龚登科
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.)
GUIZHOU QIANDONG POWER CO Ltd
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GUIZHOU QIANDONG POWER CO Ltd
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Priority to CN201721759942.3U priority Critical patent/CN207776919U/en
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Abstract

A kind of Water vapour images for coagulating gas formula boiler, it is characterised in that:Including high-pressure heater, boiler, superheater, attemperator, feed pump, steam turbine and gas trap, wherein feed pump connects high-pressure heater;High-pressure heater connects boiler and attemperator;Boiler connects superheater;Superheater connects attemperator;Attemperator connects steam turbine;Steam turbine connects gas trap;Condenser connects feed pump.Pass through the implementation of the utility model, the source of desuperheating water in attemperator is set at high-pressure heater, substantially increase the initial temperature of desuperheating water, make superheated steam that need not consume excessive heat during being cooled down, it ensure that and increase for being used for the steam energy of rotary electrification in Steam Turbine, the efficiency for improving extraction cycle greatly reduces the heat consumption of unit, improves generating efficiency.

Description

A kind of Water vapour images for coagulating gas formula boiler
Technical field
The utility model is related to a kind of Water vapour images for coagulating gas formula boiler.
Background technology
Currently, common thermal power unit boiler Water vapour images, often by the source setting of desuperheating water in attemperator with In water route connecting pipe after feed pump, desuperheating water is directly supplied into attemperator from feed pump, although thus pipe-line system It is relatively simple, but since the temperature being discharged in feed pump is relatively low low, directly resulting in the efficiency of extraction cycle reduces, unit Heat consumption is very big, and excessive heat consumption is really rotated for Steam Turbine in the mixed process of desuperheating water and superheated steam The thermal energy of power generation greatly reduces, and reduces the efficiency of power generation.
Utility model content
In order to solve the above technical problems, the utility model provides a kind of Water vapour images for coagulating gas formula boiler.
The utility model is achieved by the following technical programs.
It is provided by the utility model a kind of for coagulating the Water vapour images of gas formula boiler, including high-pressure heater, boiler, Superheater, attemperator, feed pump, steam turbine and gas trap, wherein feed pump connects high-pressure heater;High-pressure heater connects Connect boiler and attemperator;Boiler connects superheater;Superheater connects attemperator;Attemperator connects steam turbine;Steam turbine connection is solidifying Gas device;Condenser connects feed pump.
It is respectively level-one attemperator and two level attemperators that the attemperator, which is two, wherein level-one attemperator and superheater and High-pressure heater connects, and receives the superheated steam from superheater and the desuperheating water from high-pressure heater;Two level attemperator with Level-one attemperator, high-pressure heater and steam turbine connection receive the desuperheated system from level-one attemperator and come from high pressure The desuperheating water of heater, and to steam turbine feeding secondary desuperheated system.
Further include that a water feeding tank is connect with feed pump, water source is provided for feed pump.
It is additionally provided with oxygen-eliminating device in the water feeding tank.
Further include a low-pressure heater, low-pressure heater is connect with feed pump and high-pressure heater, and feed pump provides Hot water to be added after low-pressure heater is heated enter high-pressure heater in.
Further include a pressure gauge and alarm, pressure gauge is set on high-pressure heater and is connect with alarm.
The alarm is audible-visual annunciator.
The beneficial effects of the utility model are:By the implementation of the utility model, by the source of desuperheating water in attemperator Be set at high-pressure heater, substantially increase the initial temperature of desuperheating water, make superheated steam during being cooled down not Excessive heat must be consumed, ensure that and increase for being used for the steam energy of rotary electrification in Steam Turbine, improve backheat and follow The efficiency of ring greatly reduces the heat consumption of unit, improves generating efficiency.
Description of the drawings
Fig. 1 is the structure connection signal block diagram of the utility model.
Specific implementation mode
Be described further below the technical solution of the utility model, but claimed range be not limited to it is described.
It is a kind of for coagulating the Water vapour images of gas formula boiler, including high-pressure heater, boiler, superheater, attemperator, give Water pump, steam turbine and gas trap, wherein feed pump connects high-pressure heater;High-pressure heater connects boiler and attemperator;Pot Stove connects superheater;Superheater connects attemperator;Attemperator connects steam turbine;Steam turbine connects gas trap;Condenser connect to Water pump.
It is respectively level-one attemperator and two level attemperators that the attemperator, which is two, wherein level-one attemperator and superheater and High-pressure heater connects, and receives the superheated steam from superheater and the desuperheating water from high-pressure heater;Two level attemperator with Level-one attemperator, high-pressure heater and steam turbine connection receive the desuperheated system from level-one attemperator and come from high pressure The desuperheating water of heater, and to steam turbine feeding secondary desuperheated system.
Further include that a water feeding tank is connect with feed pump, water source is provided for feed pump.
It is additionally provided with oxygen-eliminating device in the water feeding tank.Increase oxygen-eliminating device and carry out deoxygenation, makes the purity into the water of Water, steam circulation Higher, conducive to carrying out being thermally formed steam.
Further include a low-pressure heater, low-pressure heater is connect with feed pump and high-pressure heater, and feed pump provides Hot water to be added after low-pressure heater is heated enter high-pressure heater in.
Further include a pressure gauge and alarm, pressure gauge is set on high-pressure heater and is connect with alarm.In height Pressure gauge is set on pressure heater and is connect with alarm, leads to safe thing in high-pressure heater because of hypertonia for preventing Therefore.
The alarm is audible-visual annunciator.
When work, water is pumped by low-pressure heater in high-pressure heater from water tank by feed pump, by hyperbaric heating The heating of device, the superheater that a part of water enters in boiler are heated as superheated steam, and another part enters level-one attemperator It is mixed with the superheated steam by superheater heating as desuperheating water with two level attemperator, superheated steam is subtracted Temperature eventually forms desuperheated system and does work to the steamer of steam turbine, and the vapor after acting becomes solidifying using the condensation of gas trap It bears water into feed pump, carries out heating acting again.
By the implementation of the utility model, the source of desuperheating water in attemperator is set at high-pressure heater, is carried significantly The high initial temperature of desuperheating water, makes superheated steam that need not consume excessive heat during being cooled down, ensure that use Steam energy for rotary electrification in Steam Turbine increases, and improves the efficiency of extraction cycle, greatly reduces unit Heat consumption improves generating efficiency.

Claims (7)

1. a kind of Water vapour images for coagulating gas formula boiler, it is characterised in that:Including high-pressure heater, boiler, superheater, Attemperator, feed pump, steam turbine and gas trap, wherein feed pump connects high-pressure heater;High-pressure heater connect boiler and Attemperator;Boiler connects superheater;Superheater connects attemperator;Attemperator connects steam turbine;Steam turbine connects gas trap;Condensing Device connects feed pump.
2. the Water vapour images as described in claim 1 for coagulating gas formula boiler, it is characterised in that:The attemperator is two A is respectively level-one attemperator and two level attemperator, and wherein level-one attemperator is connect with superheater and high-pressure heater, receives and Superheated steam from superheater and the desuperheating water from high-pressure heater;Two level attemperator and level-one attemperator, high-pressure heater And steam turbine connection, receive the desuperheated system from level-one attemperator and the desuperheating water from high-pressure heater, and to vapour Turbine feeding secondary desuperheated system.
3. the Water vapour images as described in claim 1 for coagulating gas formula boiler, it is characterised in that:Further include a water supply Case is connect with feed pump, and water source is provided for feed pump.
4. the Water vapour images as claimed in claim 3 for coagulating gas formula boiler, it is characterised in that:In the water feeding tank also Equipped with oxygen-eliminating device.
5. the Water vapour images as described in claim 1 for coagulating gas formula boiler, it is characterised in that:Further include a low pressure Heater, low-pressure heater are connect with feed pump and high-pressure heater, and the hot water to be added that feed pump provides passes through low-pressure heating Device enters after being heated in high-pressure heater.
6. the Water vapour images as described in claim 1 for coagulating gas formula boiler, it is characterised in that:Further include a pressure Meter and alarm, pressure gauge are set on high-pressure heater and are connect with alarm.
7. the Water vapour images as claimed in claim 6 for coagulating gas formula boiler, it is characterised in that:The alarm is sound Light crossing-signal.
CN201721759942.3U 2017-12-16 2017-12-16 A kind of Water vapour images for coagulating gas formula boiler Active CN207776919U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721759942.3U CN207776919U (en) 2017-12-16 2017-12-16 A kind of Water vapour images for coagulating gas formula boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721759942.3U CN207776919U (en) 2017-12-16 2017-12-16 A kind of Water vapour images for coagulating gas formula boiler

Publications (1)

Publication Number Publication Date
CN207776919U true CN207776919U (en) 2018-08-28

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721759942.3U Active CN207776919U (en) 2017-12-16 2017-12-16 A kind of Water vapour images for coagulating gas formula boiler

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CN (1) CN207776919U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112377891A (en) * 2020-11-10 2021-02-19 西安热工研究院有限公司 Energy-conserving power plant boiler over heater temperature reduction water system of degree of depth

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112377891A (en) * 2020-11-10 2021-02-19 西安热工研究院有限公司 Energy-conserving power plant boiler over heater temperature reduction water system of degree of depth

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