CN106702052A - Blast furnace top pressure-equalizing gas recovery system and method - Google Patents

Blast furnace top pressure-equalizing gas recovery system and method Download PDF

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Publication number
CN106702052A
CN106702052A CN201510791186.1A CN201510791186A CN106702052A CN 106702052 A CN106702052 A CN 106702052A CN 201510791186 A CN201510791186 A CN 201510791186A CN 106702052 A CN106702052 A CN 106702052A
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CN
China
Prior art keywords
pressure
gas
valve
coal
pipeline
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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
CN201510791186.1A
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Chinese (zh)
Inventor
孟凡双
赵正洪
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.)
Angang Steel Co Ltd
Original Assignee
Angang 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 Angang Steel Co Ltd filed Critical Angang Steel Co Ltd
Priority to CN201510791186.1A priority Critical patent/CN106702052A/en
Publication of CN106702052A publication Critical patent/CN106702052A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B5/00Making pig-iron in the blast furnace
    • C21B5/06Making pig-iron in the blast furnace using top gas in the blast furnace process

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Abstract

The invention provides a blast furnace top pressure-equalizing gas recovery system and a method, wherein a pressure-equalizing gas pipe is connected to the high-pressure end of a gas pipe at the front part of a pressure equalizing valve, a back pressure pipeline is additionally arranged, one end of the back pressure pipeline is connected with the gas pipe, the other end of the back pressure pipeline is connected with a clean gas main pipeline,and a recovery valve, a buffer tank, a regulating valve, a check valve and a stop valve are sequentially arranged on the back pressure pipeline. Opening a recovery valve, and allowing the gas to enter a clean gas main pipeline; when the gas pressure is balanced with the pressure of the clean gas main pipeline, closing the recovery valve, opening the relief valve and discharging the lower tank; opening a pressure equalizing valve after the discharging is finished, closing a relief valve, equalizing the pressure of the lower tank to the pressure of the top of the furnace, and starting to discharge the material into the blast furnace; recovering coal gas after discharging; when the pressure of the lower tank is balanced with the pressure of the main clean gas pipeline, the gas recovery is stopped, and the dispersion valve is opened. The invention can ensure that the dust content of the back pressure coal gas is less than 5mg/m3The coal gas is prevented from being diffused to cause environmental and noise pollution, and can be recycled, so that the dual effects of energy conservation and emission reduction are realized.

Description

A kind of blast furnace roof presses gas recovery system and method
Technical field
The invention belongs to smelt iron field of pipeline equipment, more particularly to a kind of recovery system for pressing coal gas for blast furnace roof and its return Receiving method.
Background technology
Blast furnace roof feeding system, is returned by half purified gas of blast furnace roof, and after being pressed with furnace top pressure, valve material is put into blast furnace Interior, then the coal gas under blast furnace roof in tank is discharged into air via pressure gas pipe, not only causes the dirt of environment and noise Dye, and the significant wastage energy.
The content of the invention
The present invention provides a kind of blast furnace roof and presses gas recovery system and method, it is intended to coal-gas recovering after pressing to purified gas In pipe network, so as to realize the purpose of energy-saving and emission-reduction.
Therefore, the technical solution that the present invention is taken is:
A kind of blast furnace roof presses the pressure gas pipe of tank under gas recovery system, including connection blast furnace roof, is connected to dry method and removes Gas pipe and equalizing valve after dirt on coal gas main pipeline, access the anterior gas pipe high-pressure side of equalizing valve, and increase by pressure gas pipe If back pressure pipeline, back pressure pipeline one end connection gas pipe, the other end is connected with purified gas main pipeline, is installed successively on back pressure pipeline There are recovery valve, surge tank, regulating valve, check-valves and stop valve.
A kind of blast furnace roof presses coal-gas recovering method, and its specific removal process is:
When furnace top even pressure terminates, upper pressure tank is 220kPa, is balanced with furnace top pressure;Open stock gas recovery valve, coal gas warp Surge tank, regulating valve, check-valves, stop valve are crossed, into purified gas main pipeline;When gas pressure and purified gas main pipeline pressure When 12kPa is balanced, stop coal-gas recovering, close coal gas recovery valve, turn on the gas diffusion valve makes lower pressure tank reach 0kPa, weight Newly to lower tank blowing;After blanking terminates, equalizing valve is opened, close diffusion valve, when lower tank is pressed onto into furnace top pressure 220kPa, Start to blowing in blast furnace;After blowing terminates, upper pressure tank is 220kPa, carries out coal-gas recovering;Instantly pressure tank and purified gas When main pipeline pressure is 12kPa, stop coal-gas recovering, open diffusion valve, re-start blanking process.
Beneficial effects of the present invention are:
Simple structure of the present invention, it is easy to arrange, safe, good dedusting effect, gas recovery is without dedusting, it is ensured that back pressure The dustiness of coal gas is less than 5mg/m3, can not only effectively solve the environment that causes of pressure coal gas diffusion and noise pollution, and can be by Coal-gas recovering, realizes the double effectses of energy-saving and emission-reduction.Meanwhile, the coal gas of recovery is directly entered clean coal gas pipe network, therefore to system The almost influence without pressure oscillation.
Brief description of the drawings
Fig. 1 is to press gas recovery system structural representation.
In figure:Coal gas main pipeline 3 after tank 1 under furnace roof, pressure gas pipe 2, dry method dust, gas pipe 4, equalizing valve 5, put Dissipate valve 6, back pressure pipeline 7, recovery valve 8, surge tank 9, regulating valve 10, check-valves 11, stop valve 12, purified gas supervisor Road 13.
Specific embodiment
As seen from Figure 1, blast furnace roof of the present invention presses gas recovery system, be it is original connection blast furnace roof under tank 1 and on Pressure gas pipe 2 of the end with diffusion valve 6, gas pipe 4 after connection dry method dust on coal gas main pipeline 3 and its installed in coal On the basis of equalizing valve 8 on tracheae 4, on the one hand pressure gas pipe 2 is accessed the high pressure of the gas pipe 4 of the front portion of equalizing valve 5 End, 5mg/m is less than with the dustiness for ensureing back pressure coal gas3.Simultaneously be additionally arranged including back pressure pipeline 7, recovery valve 8, surge tank 9, Regulating valve 10, check-valves 11, stop valve 12 are in interior recovery system.One end of back pressure pipeline 7 is connected into gas pipe 4, separately One end is connected with purified gas main pipeline 13, and be mounted with successively on back pressure pipeline 7 recovery valve 8, surge tank 9, regulating valve 10, Check-valves 11 and stop valve 12.So as to after blanking terminates, will press coal-gas recovering to be responsible for purified gas by back pressure pipeline 7 Recycled in road 13, overbottom pressure is then diffused in air.
Blast furnace roof of the present invention presses the specific removal process of coal-gas recovering method to be:
When furnace top even pressure terminates, upper pressure tank is 220kPa, is balanced with furnace top pressure;Open stock gas recovery valve 8, coal gas By surge tank 9, regulating valve 10, check-valves 11, stop valve 12, into purified gas main pipeline 13;When gas pressure with it is net When the pressure 12kPa of coal gas main pipeline 13 is balanced, stop coal-gas recovering, close coal gas recovery valve 8, turn on the gas diffusion valve 6 makes Lower pressure tank reaches 0kPa, again to lower tank blowing;After blanking terminates, equalizing valve 5 is opened, diffusion valve 6 is closed, by lower tank When being pressed onto furnace top pressure 220kPa, start to blowing in blast furnace, after blowing terminates, upper pressure tank is 220kPa, carries out coal Gas is reclaimed;Instantly when pressure tank is 12kPa with the pressure of purified gas main pipeline 13, stop coal-gas recovering, open diffusion valve 6, again Carry out blanking process.

Claims (2)

1. a kind of blast furnace roof presses the pressure gas pipe of tank under gas recovery system, including connection blast furnace roof, It is connected to gas pipe and equalizing valve on coal gas main pipeline after dry method dust, it is characterised in that will press coal gas Pipe accesses the anterior gas pipe high-pressure side of equalizing valve, and sets up back pressure pipeline, back pressure pipeline one end connection coal gas Pipe, the other end is connected with purified gas main pipeline, and recovery valve, surge tank, tune are sequentially installed with back pressure pipeline Section valve, check-valves and stop valve.
2. the method that blast furnace roof described in a kind of application claim 1 presses gas recovery system, its feature exists In specific removal process is:
When furnace top even pressure terminates, upper pressure tank is 220kPa, is balanced with furnace top pressure;Stock gas is opened to return Receive valve, coal gas by surge tank, regulating valve, check-valves, stop valve, into purified gas main pipeline;Work as coal When atmospheric pressure is balanced with purified gas main pipeline pressure 12kPa, stop coal-gas recovering, close coal gas recovery valve, Turn on the gas diffusion valve, makes lower pressure tank reach 0kPa, again to lower tank blowing;After blanking terminates, open equal Pressure valve, closes diffusion valve, when lower tank is pressed onto into furnace top pressure 220kPa, starts, to blowing in blast furnace, to put After material terminates, upper pressure tank is 220kPa, carries out coal-gas recovering;Instantly pressure tank and purified gas main pipeline pressure When power is 12kPa, stop coal-gas recovering, open diffusion valve, re-start blanking process.
CN201510791186.1A 2015-11-17 2015-11-17 Blast furnace top pressure-equalizing gas recovery system and method Pending CN106702052A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510791186.1A CN106702052A (en) 2015-11-17 2015-11-17 Blast furnace top pressure-equalizing gas recovery system and method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510791186.1A CN106702052A (en) 2015-11-17 2015-11-17 Blast furnace top pressure-equalizing gas recovery system and method

Publications (1)

Publication Number Publication Date
CN106702052A true CN106702052A (en) 2017-05-24

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510791186.1A Pending CN106702052A (en) 2015-11-17 2015-11-17 Blast furnace top pressure-equalizing gas recovery system and method

Country Status (1)

Country Link
CN (1) CN106702052A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023061027A1 (en) * 2021-10-12 2023-04-20 中冶南方工程技术有限公司 Blast furnace top material tank pressure equalization gas purification and recovery system and method

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3884677A (en) * 1972-11-25 1975-05-20 Nippon Kokan Kk Blast furnace operating methods
CN202054851U (en) * 2011-04-29 2011-11-30 中冶赛迪工程技术股份有限公司 Blast-furnace dry-method even-pressure gas recycling device
CN202912974U (en) * 2012-09-28 2013-05-01 中冶南方工程技术有限公司 Pressure-equalizing coal gas recovery device for furnace roof of blast furnace
CN104073581A (en) * 2014-06-18 2014-10-01 鞍钢集团工程技术有限公司 Process method and device for forcibly recovering diffused gas of blast furnace

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3884677A (en) * 1972-11-25 1975-05-20 Nippon Kokan Kk Blast furnace operating methods
CN202054851U (en) * 2011-04-29 2011-11-30 中冶赛迪工程技术股份有限公司 Blast-furnace dry-method even-pressure gas recycling device
CN202912974U (en) * 2012-09-28 2013-05-01 中冶南方工程技术有限公司 Pressure-equalizing coal gas recovery device for furnace roof of blast furnace
CN104073581A (en) * 2014-06-18 2014-10-01 鞍钢集团工程技术有限公司 Process method and device for forcibly recovering diffused gas of blast furnace

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023061027A1 (en) * 2021-10-12 2023-04-20 中冶南方工程技术有限公司 Blast furnace top material tank pressure equalization gas purification and recovery system and method

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Application publication date: 20170524