CN110938723A - Pressure-equalizing gas self-cleaning purification and full-recovery process for blast furnace top charging bucket - Google Patents

Pressure-equalizing gas self-cleaning purification and full-recovery process for blast furnace top charging bucket Download PDF

Info

Publication number
CN110938723A
CN110938723A CN201911145015.6A CN201911145015A CN110938723A CN 110938723 A CN110938723 A CN 110938723A CN 201911145015 A CN201911145015 A CN 201911145015A CN 110938723 A CN110938723 A CN 110938723A
Authority
CN
China
Prior art keywords
pressure
gas
recovery
valve
blast furnace
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
CN201911145015.6A
Other languages
Chinese (zh)
Inventor
张占庄
杨兵
陆枢乙
彭子明
关文强
蔡成峰
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.)
Jiangsu Ruili Environmental Engineering Ltd By Share Ltd
Original Assignee
Jiangsu Ruili Environmental Engineering Ltd By Share 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 Jiangsu Ruili Environmental Engineering Ltd By Share Ltd filed Critical Jiangsu Ruili Environmental Engineering Ltd By Share Ltd
Priority to CN201911145015.6A priority Critical patent/CN110938723A/en
Publication of CN110938723A publication Critical patent/CN110938723A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B7/00Blast furnaces
    • C21B7/007Controlling or regulating of the top pressure
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B7/00Blast furnaces
    • C21B7/002Evacuating and treating of exhaust gases
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B7/00Blast furnaces
    • C21B7/22Dust arresters
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2100/00Handling of exhaust gases produced during the manufacture of iron or steel
    • C21B2100/40Gas purification of exhaust gases to be recirculated or used in other metallurgical processes
    • C21B2100/44Removing particles, e.g. by scrubbing, dedusting

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Blast Furnaces (AREA)

Abstract

The invention discloses a self-cleaning purification and full recovery process of blast furnace top charging bucket pressure-sharing gas, which utilizes the pressure difference between high-pressure gas and low-pressure gas pipe network in the charging bucket to carry out natural recovery, the high-pressure gas and the low-pressure gas pipe network are filtered by a top gas recovery cyclone cloth bag composite dust collector and then are merged into the low-pressure clean gas pipe network, 80 percent of pressure-sharing gas in the recovery charging bucket is recovered, a forced injection recoverer is opened to carry out forced recovery on the residual gas in a charging bucket at the end of natural recovery of the gas, the residual gas in the recovery charging bucket is transferred to the low-pressure gas pipe network, and the 100 percent recovery of pressure-sharing gas in the charging bucket is achieved, so; the top of the blast furnace is provided with the cyclone cloth bag composite dust collector, the dust collection efficiency is high, the self-cleaning type dust cleaning function is realized through the pressure-equalizing clean gas, the energy consumption is reduced, the automation degree of the recovery process is high, the full-automatic unmanned control can be realized through the PLC, and the occupied area and the project investment can be reduced.

Description

Pressure-equalizing gas self-cleaning purification and full-recovery process for blast furnace top charging bucket
Technical Field
The invention relates to the field of environmental protection, in particular to a self-cleaning purification and full recovery process for pressure-equalizing coal gas of a charging bucket at the top of a blast furnace.
Background
In recent years, with the rising concern of people on environmental protection and climate, low-carbon, clean and efficient enterprises are bound to be built, in the process of blast furnace smelting production, high-pressure gas in a charging bucket needs to be decompressed and diffused before charging of a blast furnace charging bucket, a diffusing valve is opened in the traditional diffusing mode, dust-containing high-pressure gas in the charging bucket is directly discharged to the air through a diffusing pipe, noise is generated in the diffusing process, a large amount of blast furnace gas and dust are discharged, multiple pollution is caused to the environment, and a large amount of gas energy is wasted in vain.
According to the latest standard and the environmental protection requirement, the top of the blast furnace is provided with a top pressure discharge coal gas recovery device. Therefore, in order to recover energy and improve the environment, simultaneously eliminate the noise of the furnace top and improve the maintenance condition of the furnace top equipment, the furnace top pressure equalizing and bleeding system is required to be provided with a pressure equalizing gas recovery system.
Disclosure of Invention
The invention aims to provide a self-cleaning purification and full recovery process for pressure-equalizing coal gas of a charging bucket at the top of a blast furnace.
The technical scheme adopted by the invention is as follows:
the self-cleaning purification and full recovery process of pressure-equalizing coal gas of a blast furnace top charging bucket is characterized in that: the method comprises the following steps:
step 1: opening a sealing material-intercepting valve on the blast furnace burden tank, and allowing the blast furnace burden to fall into the blast furnace burden tank, wherein the pressure in the blast furnace burden tank is equal to the atmospheric pressure;
step 2: after the charging of the blast furnace charging bucket is finished, closing the upper sealing material intercepting valve, and opening the pressure equalizing valve to pressurize the charging bucket by clean gas;
and step 3: when the pressure in the material tank is equal to the pressure in the blast furnace, pressure equalization is completed, the lower sealing material-intercepting valve of the material tank is opened, and after the furnace burden falls into the blast furnace, the lower sealing material-intercepting valve is closed;
and 4, step 4: starting a recovery system, opening a natural recovery valve, and allowing high-pressure coal gas in the material tank to enter a low-pressure coal gas pipe network through a coal gas recovery pipeline, the natural recovery valve, a check valve, a manual butterfly valve and a manual blind plate valve after being filtered by a furnace top cyclone cloth bag composite dust collector;
and 5: after the gas is naturally recovered, when the pressure detection shows that the pressure of the gas recovery pipeline is equal to the pressure of a low-pressure gas pipe network, closing a natural recovery valve, simultaneously opening a forced recovery valve behind a forced recovery ejector and a communication valve in front of the forced recovery ejector, forming high-speed airflow in the forced recovery ejector through the pressure-equalizing gas with higher pressure to generate negative pressure, and forcibly recovering the residual gas in the material tank to the low-pressure gas pipe network through the communication valve to realize 100% recovery of the pressure-equalizing gas;
step 6: when the pressure detection detects that the pressure in the material tank is reduced to be consistent with the atmospheric pressure, the forced recovery valve and the communication valve are closed to complete the recovery of the gas in the material tank for the first time, and a check valve is added on the gas recovery pipeline in order to prevent the gas in the low-pressure pipe network from flowing backwards;
and 7: opening a material tank upper sealing material intercepting valve, enabling the material tank to enter the next charging procedure, closing the material tank upper sealing material intercepting valve after charging is finished, and opening a gas pressure equalizing valve, wherein high-pressure clean gas is used for taking dust deposited on the surface of a filter bag in the cyclone cloth bag composite dust collector into the material tank through a dust discharging valve sent by a dust hopper, so that self-cleaning type dust cleaning of the cyclone cloth bag composite dust collector is realized;
and 8: the recovery process is carried out repeatedly, and the blast furnace charge gas filling recovery is completed each time.
And the dust concentration detection is arranged on the recovery pipeline and is used for detecting whether the dust concentration of the recovered coal gas entering the low-pressure coal gas pipe network is qualified or not.
The manual butterfly valve and the manual blind plate valve are opened when the system operates normally, and are closed when other valves and equipment are overhauled, and coal gas is cut off.
The invention has the advantages that: the pressure-equalizing coal gas of the blast furnace top charging bucket is purified and is fully recovered by 100 percent, the energy waste is saved, the air pollution is reduced, the original diffused noise is eliminated, the cyclone cloth bag composite dust collector is arranged on the blast furnace top, the dust collection efficiency is high, the self-cleaning type dust cleaning function can be realized through the pressure-equalizing clean coal gas, the energy consumption is reduced, the automation degree of the recovery process is high, the full-automatic unmanned control can be realized through PLC, and compared with other blast furnace top charging bucket coal gas recovery processes, the occupied area and the project investment can be reduced.
Drawings
The present invention will be described in further detail with reference to the accompanying drawings and specific embodiments.
FIG. 1 is a schematic structural diagram of the present invention.
Wherein: 1. a natural recovery valve; 2. a forced recovery valve; 3. a communication valve; 4. forcibly recovering the ejector; 5. a bleed valve; 6. a pressure equalizing valve; 7. a check valve; 8. a manual butterfly valve; 9. a manual blind plate valve; 10. a cyclone cloth bag composite dust collector; 11. an ash discharge valve; 12. an upper sealing material stopping valve; 13. a lower sealing material-stopping valve; 14. detecting pressure; 15. detecting the dust concentration; 16. a gas recovery pipeline; 17. low pressure gas pipe network.
Detailed Description
As shown in figure 1, the blast furnace top charging bucket pressure-equalizing gas self-cleaning purification and full recovery process comprises the following steps:
step 1: opening the sealing material-intercepting valve 12 on the blast furnace burden tank, and allowing the blast furnace burden to fall into the blast furnace burden tank, wherein the pressure in the blast furnace burden tank is equal to the atmospheric pressure;
step 2: after the charging of the blast furnace charging bucket is finished, closing the upper sealing material intercepting valve 12, and opening the pressure equalizing valve 6 to pressurize the charging bucket by using clean coal gas;
and step 3: when the pressure in the material tank is equal to the pressure in the blast furnace, the pressure equalization is completed, the lower sealing material-intercepting valve 13 of the material tank is opened, and after the furnace burden falls into the blast furnace, the lower sealing material-intercepting valve 13 is closed;
and 4, step 4: starting a recovery system, opening a natural recovery valve 1, filtering high-pressure gas in a material tank through a furnace top cyclone cloth bag composite dust collector 10, and then entering a low-pressure gas pipe network 17 through a gas recovery pipeline 16, the natural recovery valve 1, a check valve 7, a manual butterfly valve 8 and a manual blind plate valve 9;
and 5: after the gas is naturally recovered, when the pressure detection 14 shows that the pressure of the gas recovery pipeline 16 is equal to the pressure of a low-pressure gas pipe network, closing the natural recovery valve 1, simultaneously opening the forced recovery valve 2 behind the forced recovery ejector 4 and the communication valve 3 in front of the forced recovery ejector 4, forming high-speed airflow in the forced recovery ejector 4 through the pressure-equalizing gas with higher pressure to generate negative pressure, and forcibly recovering the residual gas in the material tank to the low-pressure gas pipe network through the communication valve 3 to realize 100% recovery of the pressure-equalizing gas;
step 6: when the pressure detection 14 detects that the pressure in the material tank is reduced to be consistent with the atmospheric pressure, the forced recovery valve 2 and the communication valve 3 are closed to complete the recovery of the gas in the material tank for one time, and a check valve 7 is additionally arranged on a gas recovery pipeline in order to prevent the gas in a low-pressure pipe network from flowing backwards;
and 7: opening the material tank upper sealing material intercepting valve 12, enabling the charging bucket to enter the next charging procedure, closing the material tank upper sealing material intercepting valve 12 after charging is finished, and opening the gas pressure equalizing valve 6, wherein high-pressure clean gas brings dust deposited on the surface of a filter bag in the cyclone cloth bag composite dust collector 10 into the charging bucket through the dust discharging valve 11 issued by the dust hopper, so that self-cleaning type dust removal of the cyclone cloth bag composite dust collector is realized;
and 8: the recovery process is carried out repeatedly, and the blast furnace charge gas filling recovery is completed each time.
The dust concentration detection 15 is arranged on the recovery pipeline and is used for detecting whether the dust concentration of the recovered coal gas entering the low-pressure coal gas pipe network is qualified or not.
The manual butterfly valve 8 and the manual blind plate valve 9 are opened when the system normally operates, and are closed when other valves and equipment are overhauled, and coal gas is cut off.
The invention utilizes the pressure difference between high-pressure gas (pressure 180-220 KPa) and low-pressure gas pipe network (pressure 10-25 KPa) in the charging bucket to carry out natural recovery, the high-pressure gas and the low-pressure gas pipe network are filtered by a cyclone cloth bag composite dust collector for recovering the top gas and then are merged into a low-pressure clean gas pipe network, 80 percent of pressure-equalizing gas in the charging bucket can be recovered at the stage, a forced injection recoverer is opened to carry out forced recovery on the residual gas in a charging bucket at the end of natural recovery of the gas, the residual gas in the charging bucket is recycled to the low-pressure gas pipe network to achieve 100 percent recovery of the pressure-equalizing gas in the charging bucket, the pressure-equalizing gas in the top of the blast furnace is purified and fully recovered by 100 percent, the energy waste is saved, the air pollution is reduced, the original diffused noise is eliminated, the cyclone cloth bag composite dust collector is arranged on the top of the blast furnace, the energy consumption is reduced, the automation degree of the recovery process is high, full-automatic unmanned control can be realized through the PLC, and the occupied area and the project investment can be reduced compared with other blast furnace top material gas filling recovery processes.

Claims (3)

1. The self-cleaning purification and full recovery process of pressure-equalizing coal gas of a blast furnace top charging bucket is characterized in that: the method comprises the following steps:
step 1: opening a sealing material-intercepting valve on the blast furnace burden tank, and allowing the blast furnace burden to fall into the blast furnace burden tank, wherein the pressure in the blast furnace burden tank is equal to the atmospheric pressure;
step 2: after the charging of the blast furnace charging bucket is finished, closing the upper sealing material intercepting valve, and opening the pressure equalizing valve to pressurize the charging bucket by clean gas;
and step 3: when the pressure in the material tank is equal to the pressure in the blast furnace, pressure equalization is completed, the lower sealing material-intercepting valve of the material tank is opened, and after the furnace burden falls into the blast furnace, the lower sealing material-intercepting valve is closed;
and 4, step 4: starting a recovery system, opening a natural recovery valve, filtering high-pressure coal gas in a material tank through a furnace top cyclone cloth bag composite dust collector, and then entering a low-pressure coal gas pipe network through a coal gas recovery pipeline, the natural recovery valve, a check valve, a manual butterfly valve and a manual blind plate valve;
and 5: after the gas is naturally recovered, when the pressure detection shows that the pressure of the gas recovery pipeline is equal to the pressure of a low-pressure gas pipe network, closing a natural recovery valve, simultaneously opening a forced recovery valve behind a forced recovery ejector and a communication valve in front of the forced recovery ejector, forming high-speed airflow in the forced recovery ejector through the pressure-equalizing gas with higher pressure to generate negative pressure, and forcibly recovering the residual gas in the material tank to the low-pressure gas pipe network through the communication valve to realize 100% recovery of the pressure-equalizing gas;
step 6: when the pressure detection detects that the pressure in the material tank is reduced to be consistent with the atmospheric pressure, the forced recovery valve and the communication valve are closed to complete the recovery of the gas in the material tank for the first time, and a check valve is added on the gas recovery pipeline in order to prevent the gas in the low-pressure pipe network from flowing backwards;
and 7: opening a material tank upper sealing material intercepting valve, enabling the material tank to enter the next charging procedure, closing the material tank upper sealing material intercepting valve after charging is finished, and opening a gas pressure equalizing valve, wherein high-pressure clean gas is used for taking dust deposited on the surface of a filter bag in the cyclone cloth bag composite dust collector into the material tank through a dust discharging valve sent by a dust hopper, so that self-cleaning type dust cleaning of the cyclone cloth bag composite dust collector is realized;
and 8: the recovery process is carried out repeatedly, and the blast furnace charge gas filling recovery is completed each time.
2. The blast furnace top bucket pressure-equalizing gas self-cleaning purification and total recovery process according to claim 1, characterized in that: and the dust concentration detection is arranged on the recovery pipeline and is used for detecting whether the dust concentration of the recovered coal gas entering the low-pressure coal gas pipe network is qualified or not.
3. The blast furnace top bucket pressure-equalizing gas self-cleaning purification and total recovery process according to claim 1, characterized in that: the manual butterfly valve and the manual blind plate valve are opened when the system operates normally, and are closed when other valves and equipment are overhauled, and coal gas is cut off.
CN201911145015.6A 2019-11-21 2019-11-21 Pressure-equalizing gas self-cleaning purification and full-recovery process for blast furnace top charging bucket Pending CN110938723A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201911145015.6A CN110938723A (en) 2019-11-21 2019-11-21 Pressure-equalizing gas self-cleaning purification and full-recovery process for blast furnace top charging bucket

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201911145015.6A CN110938723A (en) 2019-11-21 2019-11-21 Pressure-equalizing gas self-cleaning purification and full-recovery process for blast furnace top charging bucket

Publications (1)

Publication Number Publication Date
CN110938723A true CN110938723A (en) 2020-03-31

Family

ID=69907945

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201911145015.6A Pending CN110938723A (en) 2019-11-21 2019-11-21 Pressure-equalizing gas self-cleaning purification and full-recovery process for blast furnace top charging bucket

Country Status (1)

Country Link
CN (1) CN110938723A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115386668A (en) * 2022-09-02 2022-11-25 中冶华天工程技术有限公司 Novel pressure-equalizing coal gas full-recovery method

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN207727100U (en) * 2017-11-29 2018-08-14 中冶南方工程技术有限公司 A kind of full recovery system of blast furnace top pressure-equalizing bleeding coal gas
CN110004258A (en) * 2019-04-02 2019-07-12 北京首钢国际工程技术有限公司 A kind of device recycling blast furnace top pressure-equalizing bleeding coal gas

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN207727100U (en) * 2017-11-29 2018-08-14 中冶南方工程技术有限公司 A kind of full recovery system of blast furnace top pressure-equalizing bleeding coal gas
CN110004258A (en) * 2019-04-02 2019-07-12 北京首钢国际工程技术有限公司 A kind of device recycling blast furnace top pressure-equalizing bleeding coal gas

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115386668A (en) * 2022-09-02 2022-11-25 中冶华天工程技术有限公司 Novel pressure-equalizing coal gas full-recovery method
CN115386668B (en) * 2022-09-02 2023-12-05 中冶华天工程技术有限公司 Pressure equalizing gas full recovery method

Similar Documents

Publication Publication Date Title
CN101892336A (en) Coal-gas recovering process and device of charging, equalizing and bleeding of blast furnace
CN102337364A (en) Device for recovering coal gas in equalizing and relieving process of furnace top of blast furnace
CN205062095U (en) Blast furnace furnace roof material jar diffuses gas purifying, recovery system
CN102864257A (en) Pressure-equalizing and bleeding method for injecting furnace roof tank coal gas by using high-pressure gas
CN211255968U (en) Pressure-equalizing gas self-cleaning purifying and full-recovering device for blast furnace top charging bucket
CN104073581A (en) Process method and device for forcibly recovering diffused gas of blast furnace
CN202912974U (en) Pressure-equalizing coal gas recovery device for furnace roof of blast furnace
CN108165693B (en) Coupling method and system for equalizing gas recovery of charging bucket and dry dust removal of blast furnace gas
CN211689134U (en) Novel blast furnace top pressure-equalizing gas and blast furnace damping-down waste gas integrated treatment system
CN110004258B (en) Device for recycling blast furnace top pressure equalizing and diffusing gas
CN110938723A (en) Pressure-equalizing gas self-cleaning purification and full-recovery process for blast furnace top charging bucket
CN102337365A (en) Process for recovering coal gas in equalizing and relieving process of furnace top of blast furnace
CN215404318U (en) Non-diffusion recovery system for blast furnace top pressure-equalizing gas
CN217438223U (en) Purification treatment recovery and diffusion system for diffused gas in maintenance of blast furnace top
CN105177206A (en) Pressure-equalizing blowing-off device and method for blast furnace charging bucket
CN102925603B (en) Process and device for recycling pressure-equalizing diffusion gas at blast furnace top
CN102864260A (en) Pressure-equalizing bleeding device for ejecting furnace-top tank gas by high pressure gas
CN205170886U (en) Device is diffused in voltage -sharing of high furnace charge jar
CN204690022U (en) A kind of blast furnace top pressure-equalizing bleeding gas recovering device
CN115652001A (en) Blast furnace top pressure-equalizing gas recovery system and recovery method thereof
CN201981222U (en) Blast furnace top pressure equalizing gas recovery device
CN202208727U (en) Gas recovering device used during uniform pressure diffusing of blast furnace top
CN208949324U (en) Economical blast furnace top pressure-equalizing gas recovery system
CN210103990U (en) Device for recovering pressure-equalizing diffused gas at top of blast furnace
CN213866287U (en) Blast furnace charging bucket pressure-equalizing coal gas full-recovery system

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination