CN104848732A - Back washing method of boiler superheater - Google Patents

Back washing method of boiler superheater Download PDF

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Publication number
CN104848732A
CN104848732A CN201410054549.9A CN201410054549A CN104848732A CN 104848732 A CN104848732 A CN 104848732A CN 201410054549 A CN201410054549 A CN 201410054549A CN 104848732 A CN104848732 A CN 104848732A
Authority
CN
China
Prior art keywords
water
superheater
washing
boiler
deoxygenation
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.)
Pending
Application number
CN201410054549.9A
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Chinese (zh)
Inventor
韩兴国
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.)
Shanxi Taigang Stainless Steel Co Ltd
Original Assignee
Shanxi Taigang Stainless Steel 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.)
Filing date
Publication date
Application filed by Shanxi Taigang Stainless Steel Co Ltd filed Critical Shanxi Taigang Stainless Steel Co Ltd
Priority to CN201410054549.9A priority Critical patent/CN104848732A/en
Publication of CN104848732A publication Critical patent/CN104848732A/en
Pending legal-status Critical Current

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Abstract

The invention discloses a back washing method of a boiler superheater, which is mainly used for washing drum boilers with various pressure grades. The back washing method comprises the following steps: (1) a washing water source adopts ammonified demineralized water with a pH value of 9.0-9.5; (2) the washing water source is deoxidized and heated to control the washing water temperature within 80-90 DEG C; and dissolved oxygen is 100 mg/l; (3) a water feeding pump and a deoxidizing water tank form self-circulation, and a temperature reducing water valve is used for charging water in the superheater; the flowing speed of water is 5 t/h; and the water is drained from a low point and is discharged; (4) when the superheater is stood for one hour after being fully filled with the water, the superheater is back washed; and the water is fed into the deoxidizing water tank for heating; and (5) the operations of (3, 4) are repeated until silicon dioxide and sodium content are the same with the washing water. The back washing method of the boiler superheater is short in washing time, low in water consumption and free of corrosion phenomenon in superheater pipes.

Description

Boiler superheater back-flushing method
Technical field
The present invention is mainly used in the cleaning of various pressure rating dum boiler, is specifically related to boiler superheater back-flushing method.
Background technology
Along with the constantly progress of boiler feedwater technology, boiler feed water condition of water quality is more and more excellent, dum boiler takes many measures in design simultaneously, ensure steam quality, but often can't ensure there is no salification completely in superheater, especially, separator effect is bad in the middle low-pressure boiler adopting demineralized water moisturizing or drum, serious salification in superheater will be caused.Because superheater Incrustation of pipe is complicated, institute's salt scale coagulation is subject to long-term baking, not soluble, how to remove salification safely and effectively, ensures boiler thermal output and security of operation.
Conventional flush adopts condensate water or demineralized water to rinse, and washing time is long, and water consumption is large, easily etching problem occurs simultaneously.
Summary of the invention
The invention provides washing time short, the boiler superheater back-flushing method that water consumption is little.
Technical scheme of the present invention comprises following content:
(1) the ammonification demineralized water that employing pH value in water source is 9.0 ~ 9.5 is rinsed;
(2) utilize and face stove steam and carry out deoxygenation heating to flushing water source, controlled by rinse water temperature at 80 ~ 90 DEG C, dissolved oxygen is 100 micrograms per litre.
(3) feed pump makes itself and deoxygenation water tank form self-loopa, and utilizes desuperheating water valve to carry out water-filling to superheater, and water flow velocity is 5t/h, discharges from low spot is hydrophobic.
(4) quiet bubble one hour after being full of water, starts superheater backwash; Heat to the moisturizing of deoxygenation water tank simultaneously.
(5) step 3,4 repeatedly, until silica, identical with flushing water containing sodium amount.
Washing time of the present invention is short, and water consumption is little, and the corrosion-free phenomenon of superheater pipeline.
Detailed description of the invention
(1) the ammonification demineralized water (or adopting hydrazine to regulate) that employing pH value in water source is 9.0 ~ 9.5 is rinsed;
(2) utilize and face stove steam and carry out deoxygenation heating to it, controlled by rinse water temperature at 80 ~ 90 DEG C, dissolved oxygen is 100 micrograms per litre.
(3) feed pump makes itself and deoxygenation water tank form self-loopa, and utilizes desuperheating water valve to carry out water-filling to superheater, and water flow velocity is 5t/h, discharges from low spot is hydrophobic.
(4) quiet bubble one hour after being full of water, starts superheater backwash; Heat to the moisturizing of deoxygenation water tank simultaneously.
(5) step 3,4 repeatedly, until silica, identical with flushing water containing sodium amount.

Claims (1)

1. boiler superheater back-flushing method, is characterized in that comprising following content:
(1) the ammonification demineralized water that employing pH value in water source is 9.0 ~ 9.5 is rinsed;
(2) carry out deoxygenation heating to flushing water source, controlled by rinse water temperature at 80 ~ 90 DEG C, dissolved oxygen is 100 micrograms per litre;
(3) feed pump makes itself and deoxygenation water tank form self-loopa, and utilizes desuperheating water valve to carry out water-filling to superheater, and water flow velocity is 5t/h, discharges from low spot is hydrophobic;
(4) superheater quiet bubble one hour after being full of water, starts superheater backwash; Heat to the moisturizing of deoxygenation water tank simultaneously;
(5) (3), (4) operation is repeatedly carried out, until silica, identical with flushing water containing sodium amount.
CN201410054549.9A 2014-02-18 2014-02-18 Back washing method of boiler superheater Pending CN104848732A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410054549.9A CN104848732A (en) 2014-02-18 2014-02-18 Back washing method of boiler superheater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410054549.9A CN104848732A (en) 2014-02-18 2014-02-18 Back washing method of boiler superheater

Publications (1)

Publication Number Publication Date
CN104848732A true CN104848732A (en) 2015-08-19

Family

ID=53848565

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410054549.9A Pending CN104848732A (en) 2014-02-18 2014-02-18 Back washing method of boiler superheater

Country Status (1)

Country Link
CN (1) CN104848732A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106247316A (en) * 2016-07-29 2016-12-21 太仓英达锅炉设备有限公司 A kind of boiler superheater

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201974430U (en) * 2011-03-24 2011-09-14 昆明醋酸纤维有限公司 Water feeding device for boiler water pressure test
CN102796537A (en) * 2012-08-31 2012-11-28 上海宝钢节能技术有限公司 System and method for recovering superheated steam of waste heat of raw gas of combined coke oven
CN102816574A (en) * 2012-08-31 2012-12-12 上海宝钢节能技术有限公司 Device for generating electricity from waste heat of raw coke oven gas
CN202836340U (en) * 2012-08-08 2013-03-27 华电潍坊发电有限公司 Chemical washing device for boiler superheater
CN203100538U (en) * 2013-02-03 2013-07-31 成都酷玩网络科技有限公司 Superheater tube washing system

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201974430U (en) * 2011-03-24 2011-09-14 昆明醋酸纤维有限公司 Water feeding device for boiler water pressure test
CN202836340U (en) * 2012-08-08 2013-03-27 华电潍坊发电有限公司 Chemical washing device for boiler superheater
CN102796537A (en) * 2012-08-31 2012-11-28 上海宝钢节能技术有限公司 System and method for recovering superheated steam of waste heat of raw gas of combined coke oven
CN102816574A (en) * 2012-08-31 2012-12-12 上海宝钢节能技术有限公司 Device for generating electricity from waste heat of raw coke oven gas
CN203100538U (en) * 2013-02-03 2013-07-31 成都酷玩网络科技有限公司 Superheater tube washing system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106247316A (en) * 2016-07-29 2016-12-21 太仓英达锅炉设备有限公司 A kind of boiler superheater
CN106247316B (en) * 2016-07-29 2019-05-03 安徽中节环保新能源有限公司 A kind of boiler superheater

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EXSB Decision made by sipo to initiate substantive examination
SE01 Entry into force of request for substantive examination
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Application publication date: 20150819