CN107794337A - A kind of converter gas purification and coal-gas recovering RD valve dynamic control methods - Google Patents

A kind of converter gas purification and coal-gas recovering RD valve dynamic control methods Download PDF

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Publication number
CN107794337A
CN107794337A CN201610802658.3A CN201610802658A CN107794337A CN 107794337 A CN107794337 A CN 107794337A CN 201610802658 A CN201610802658 A CN 201610802658A CN 107794337 A CN107794337 A CN 107794337A
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CN
China
Prior art keywords
valves
converter
gas
coal
exhaust gas
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
CN201610802658.3A
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Chinese (zh)
Inventor
张帆
金宝旭
耿辉
王金朋
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 CN201610802658.3A priority Critical patent/CN107794337A/en
Publication of CN107794337A publication Critical patent/CN107794337A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28Manufacture of steel in the converter
    • C21C5/38Removal of waste gases or dust

Abstract

The present invention provides a kind of converter gas purification and coal-gas recovering RD valve dynamic control methods, and RD valve actuation state control programs are set up in converter PLC;When converter starts oxygen blast, converter PLC overturns the aperture of adjustment RD valves by agate actuator control valves plate difficult to understand, and by the exhaust gas volumn of RD valves, increase 20000L/h, 16~17s recover conventional setting value afterwards automatically on the basis of conventional setting value.When coal-gas recovering starts, triple valve starts action, converter PLC overturns the aperture of adjustment RD valves by agate actuator control valves plate difficult to understand, and the exhaust gas volumn of RD valves is increased into 20000L/h automatically on the basis of conventional setting value, recovers conventional setting value after 16~17s.This invention removes the influence that the unfavorable factor of RD valve adjustment times is controlled exhaust gas volumn, solve that the flue gas caused by exhaust gas volumn reduces on a large scale is excessive and coal-gas recovering calorific value loss problem, ensure that the direct motion of production and the controllability of cost.

Description

A kind of converter gas purification and coal-gas recovering RD valve dynamic control methods
Technical field
It is more particularly to a kind of to be used for converter gas purification and coal-gas recovering RD valves the invention belongs to automatic control technology field Dynamic control method.
Background technology
Certain steelwork converter gas cleaning, using " OG " method, is adjusted with gas recovery system secondly text shouts mouth using RD valves Section.The adjustment control mode of RD valves is automatically controls, and the basic parameter controlled is converter gas amount, i.e., according to produce reality experience An exhaust gas volumn (175000 cubes ms/h) is determined, when actually detected exhaust gas volumn differs larger with setting exhaust gas volumn, control Program realizes the upset of valve plate to adjust the aperture of RD valves, with subtracting for above-mentioned two exhaust gas volumn difference by agate actuator difficult to understand Small, the amplitude of adjustment valve plate switch is also less and less, final to realize that detection exhaust gas volumn is equal with setting value.Actual production process In, because the intrinsic reason of technique causes actual exhaust gas volumn when beginning oxygen blast and coal-gas recovering to have a downward trough, also It is to say, the exhaust gas volumn in suction system is less than setting value, excessive which results in converter dust, easily causes environmentally friendly accident, sternly Recasting about produces direct motion.
By the way that in stokehold, it has been observed that when converter starts oxygen blast and starts coal-gas recovering, converter is smoldered larger.It is logical Cross the discovery of research exhaust gas volumn trend curve, start oxygen blast and during coal-gas recovering, be pumped into the exhaust gas volumn of dust pelletizing system have one to Under trough, it is minimum can to 151000 vertical/hours or so, and exhaust gas volumn about 175000 caused by actually bessemerizing it is vertical/hour, Unnecessary flue gas overflows naturally to be caused to smolder.
It the analysis found that, it is because flue gas causes exhaust gas volumn by cold conditions to hot instantaneous variation that exhaust gas volumn, which reduces, during oxygen blast Detected value becomes big suddenly, and the detected value is higher than the exhaust gas volumn in real system, and then causes control program " erroneous judgement " cigarette in logic Tolerance is more than setting value, and RD valves turn down aperture automatically, causes flue gas to overflow fire door.And because threeway valve events are made when starting to reclaim Pressure increases suddenly after into machine, and suction is die-offed before blower fan machine, and the exhaust gas volumn in actual suction system reduces, unnecessary flue gas With regard to overflowing fire door.And RD valves tackle above-mentioned two situations adjustment aperture and are required to time of more than ten seconds automatically, thus the two when Between section flue gas it is excessive be inevitable.
The content of the invention
The present invention is intended to provide one kind can avoid fire door flue gas excessive, improve the converter gas purification of coal-gas recovering calorific value with Coal-gas recovering RD valve dynamic control methods.
For up to this purpose, this invention takes following technical solution:
A kind of converter gas purification and coal-gas recovering RD valve dynamic control methods, using converter PLC and agate actuator difficult to understand, RD valve actuation state control programs are set up in converter PLC;When converter starts oxygen blast and coal-gas recovering, converter PLC is held by agate difficult to understand The control valve plate upset of row device, adjusts the aperture of RD valves, by the exhaust gas volumn of RD valves on conventional setting value basis by the upset of valve plate Recover conventional setting value after upper automatic increase 20000L/h, 16~17s, avoid flue gas from being caused by cold conditions to hot instantaneous variation Flue gas detection values become big suddenly, and then it is excessive to cause RD valves to turn down flue gas caused by aperture automatically.
Equally, when coal-gas recovering starts, triple valve starts action, converter PLC is turned over by agate actuator control valves plate difficult to understand The aperture of the whole RD valves of modulation, by the exhaust gas volumn of RD valves on the basis of conventional setting value increase 20000L/h automatically, after 16~17s Recover conventional setting value, avoid caused by threeway valve events that exhaust gas volumn die-offs, RD valves increased in the aperture reaction time automatically Flue gas it is excessive.
Beneficial effects of the present invention are:
The present invention need not increase equipment and investment, and the unfavorable factor of RD valve adjustment times has been eliminated since implementation to exhaust gas volumn The influence of control, solves caused by exhaust gas volumn reduces on a large scale that flue gas is excessive and coal-gas recovering calorific value loss problem, turns The calorific value of producer gas recovery is improved, and ensure that the direct motion of production and the controllability of cost.
Embodiment
Converter gas purification of the present invention and coal-gas recovering RD valve dynamic control methods, mainly using original converter PLC and Agate actuator difficult to understand, while RD valve actuation state control programs are set up in converter PLC.
When converter starts oxygen blast and coal-gas recovering, converter PLC is overturn by agate actuator control valves plate difficult to understand, passes through valve Plate upset adjustment RD valves aperture, by the exhaust gas volumn of RD valves on the basis of conventional setting value automatically increase 20000L/h, 15s it After recover conventional setting value, avoid flue gas flue gas detection values as caused by cold conditions to hot instantaneous variation from becoming big suddenly, and then RD valves are caused to turn down flue gas caused by aperture automatically excessive.
Equally, when coal-gas recovering starts, triple valve starts action, converter PLC is turned over by agate actuator control valves plate difficult to understand The aperture of the whole RD valves of modulation, by the exhaust gas volumn of RD valves, increase 20000L/h, 15s recover afterwards automatically on the basis of conventional setting value Conventional setting value, the exhaust gas volumn caused by threeway valve events is avoided to die-off, RD valves increase cigarette in the aperture reaction time automatically Gas is excessive.

Claims (1)

1. a kind of converter gas purification and coal-gas recovering RD valve dynamic control methods, using converter PLC and agate actuator difficult to understand, it is special Sign is, RD valve actuation state control programs are set up in converter PLC;When converter starts oxygen blast and coal-gas recovering, converter PLC leads to Agate actuator control valves plate upset difficult to understand is crossed, the aperture of RD valves is adjusted by the upset of valve plate, the exhaust gas volumn of RD valves is set routinely Increase 20000L/h, 16~17s recover conventional setting value afterwards, avoid flue gas by cold conditions to hot moment automatically in the basis of valuation Flue gas detection values caused by change become big suddenly, and then it is excessive to cause RD valves to turn down flue gas caused by aperture automatically;
Equally, when coal-gas recovering starts, triple valve starts action, converter PLC is overturn by agate actuator control valves plate difficult to understand and adjusted The aperture of whole RD valves, by the exhaust gas volumn of RD valves, increase 20000L/h, 16~17s recover afterwards automatically on the basis of conventional setting value Conventional setting value, the exhaust gas volumn caused by threeway valve events is avoided to die-off, RD valves increase cigarette in the aperture reaction time automatically Gas is excessive.
CN201610802658.3A 2016-09-06 2016-09-06 A kind of converter gas purification and coal-gas recovering RD valve dynamic control methods Pending CN107794337A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610802658.3A CN107794337A (en) 2016-09-06 2016-09-06 A kind of converter gas purification and coal-gas recovering RD valve dynamic control methods

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610802658.3A CN107794337A (en) 2016-09-06 2016-09-06 A kind of converter gas purification and coal-gas recovering RD valve dynamic control methods

Publications (1)

Publication Number Publication Date
CN107794337A true CN107794337A (en) 2018-03-13

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610802658.3A Pending CN107794337A (en) 2016-09-06 2016-09-06 A kind of converter gas purification and coal-gas recovering RD valve dynamic control methods

Country Status (1)

Country Link
CN (1) CN107794337A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113403445A (en) * 2021-05-18 2021-09-17 山东师范大学 Intelligent control system and control method for purifying and recycling converter flue gas

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102399935A (en) * 2011-11-11 2012-04-04 甘肃酒钢集团宏兴钢铁股份有限公司 Device and method for improving gas effect of OG (Oxygen Gas Recovery System) method recovery converter
CN202380016U (en) * 2011-11-12 2012-08-15 马鞍山伏斯特自控技术有限公司 Optimized control device for recycling coal gas of converter
CN204690030U (en) * 2015-05-27 2015-10-07 鞍钢股份有限公司 A kind of converter gas dust removing automatic controller

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102399935A (en) * 2011-11-11 2012-04-04 甘肃酒钢集团宏兴钢铁股份有限公司 Device and method for improving gas effect of OG (Oxygen Gas Recovery System) method recovery converter
CN202380016U (en) * 2011-11-12 2012-08-15 马鞍山伏斯特自控技术有限公司 Optimized control device for recycling coal gas of converter
CN204690030U (en) * 2015-05-27 2015-10-07 鞍钢股份有限公司 A kind of converter gas dust removing automatic controller

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
马中海: "转炉煤气回收过程优化控制技术研究与应用", 《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》 *
马荣芳等: "转炉烟气净化及煤气回收系统中炉口微差压的自动控制", 《电气传动》 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113403445A (en) * 2021-05-18 2021-09-17 山东师范大学 Intelligent control system and control method for purifying and recycling converter flue gas
WO2022241920A1 (en) * 2021-05-18 2022-11-24 山东师范大学 Converter flue gas purification and recovery intelligent control system and control method

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