KR20030038922A - Cokes input control apparatus in blast furnace - Google Patents

Cokes input control apparatus in blast furnace Download PDF

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Publication number
KR20030038922A
KR20030038922A KR1020010069129A KR20010069129A KR20030038922A KR 20030038922 A KR20030038922 A KR 20030038922A KR 1020010069129 A KR1020010069129 A KR 1020010069129A KR 20010069129 A KR20010069129 A KR 20010069129A KR 20030038922 A KR20030038922 A KR 20030038922A
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KR
South Korea
Prior art keywords
charging
blast furnace
amount
hopper
nitrogen
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KR1020010069129A
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Korean (ko)
Inventor
김종택
김창오
Original Assignee
주식회사 포스코
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Priority to KR1020010069129A priority Critical patent/KR20030038922A/en
Publication of KR20030038922A publication Critical patent/KR20030038922A/en

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    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B7/00Blast furnaces
    • C21B7/18Bell-and-hopper arrangements
    • C21B7/20Bell-and-hopper arrangements with appliances for distributing the burden
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B7/00Blast furnaces
    • C21B7/24Test rods or other checking devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B1/00Shaft or like vertical or substantially vertical furnaces
    • F27B1/10Details, accessories, or equipment peculiar to furnaces of these types
    • F27B1/20Arrangements of devices for charging
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B1/00Shaft or like vertical or substantially vertical furnaces
    • F27B1/10Details, accessories, or equipment peculiar to furnaces of these types
    • F27B1/26Arrangements of controlling devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D21/00Arrangements of monitoring devices; Arrangements of safety devices
    • F27D21/0035Devices for monitoring the weight of quantities added to the charge
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D3/00Charging; Discharging; Manipulation of charge
    • F27D3/10Charging directly from hoppers or shoots

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacture Of Iron (AREA)

Abstract

PURPOSE: A charging control apparatus for blast furnace is provided to control the amount of nitrogen flown into charging hopper to stabilize distribution of charging materials so that stable shape of the charging materials and the optimum blast furnace state are maintained, and productivity of molten iron is improved. CONSTITUTION: In a charging control apparatus (100) for blast furnace comprising a charging hopper positioned at the upper part of the blast furnace (1), and pressure equalization control valves (7) for supplying nitrogen into the charging hopper and cutting off supply of nitrogen into the charging hopper, the charging control apparatus (100) comprises a weight indication part (20) for outputting detected values of the weight of the charging hopper (3); first operation part (21) for calculating the rotation time in realtime by multiplying rotation cycles by rotation time per unit time when charging is initiated; second operation part (22) for calculating a target value of the charging quantity per unit time by the hopper weight value detected in the weight indication part by the total rotation time calculated in the first operation part; third operation part (23) for calculating actual charging quantities per unit time by receiving the weight detection values outputted from the weight indication part; a subtraction part (24) for obtaining a deviation between the actual charging quantities per unit time and target value calculated in the second and third operation parts; a proportionator (25) for calculating a nitrogen value for compensating the deviation outputted from the subtraction part through a relation between the nitrogen amount and charging quantity supplied into the charging hopper; and a differential pressure control part (28) for controlling opening degree of the pressure equalization control valves according to the nitrogen amount compensation value for compensating deviation of the charging quantity from the proportionator as controlling the pressure equalization control valves so that pressure of the charging hopper is equal to that of the blast furnace during charging.

Description

고로설비의 장입 제어 장치{COKES INPUT CONTROL APPARATUS IN BLAST FURNACE}Charge control device of blast furnace facility {COKES INPUT CONTROL APPARATUS IN BLAST FURNACE}

본 발명은 벨러스(Bell Less)타입 용광로에 원료 및 연료를 장입하는 장입설비에 관한 것으로, 보다 상세하게는 장입물의 분포가 안정되도록 장입호퍼내로 유입되는 질소량을 제어하여 안정된 장입물의 형상과 최적의 용광로 상태를 유지하고 용선의 생산성 향상을 도모할 수 있는 고로설비에 있어서의 장입제어장치에 관한 것이다.The present invention relates to a charging facility for charging raw materials and fuel into a bell less type furnace, and more particularly, to control the amount of nitrogen flowing into the charging hopper so that the distribution of the charged material is stabilized. It relates to a charging control device in a blast furnace facility that can maintain the state of the furnace and improve the productivity of the molten iron.

도 1은 일반적인 고로설비를 개략적으로 도시한 공정도로서, 고로설비는 고로(1)와, 고로(1)로 장입될 연료 및 원료를 순차적으로 운반하는 운반장치(2)와, 상기 고로(1)의 노정에 설치되어 운반장치(2)로 운반된 연료/원료를 모아두었다가 압력조정에 의해 고로(1)내부로 장입시키는 장입호퍼(3)와, 상기 장입호퍼(3)내부의 장입물의 중량을 검출하는 로드셀(5)과, 상기 장입호퍼(3)와 고로(1)의 내부 압력차를 검출하는 차압거출기(6)와, 장입호퍼(3)로 질소를 공급하여 고로(1)와 균압을 이루기 위한 균압용 제어밸브(7)와, 상기 장입호퍼(3)의 하단부에 설치되고 설정된 경동각도 및 선회속도로 동작하여 장입물을 고로(1)내부에 분포시키는 분배장치(8)를 포함하고 있다.1 is a process diagram schematically showing a general blast furnace facility, the blast furnace facility is a blast furnace (1), a transport device (2) for sequentially transporting fuel and raw materials to be charged into the blast furnace (1), the blast furnace (1) Charge hopper (3) which is installed on the top of the hopper and collects the fuel / raw material conveyed to the conveying device (2) and charges it into the blast furnace (1) by pressure adjustment, and the weight of the charges inside the charge hopper (3). The load cell 5 to be detected, the differential pressure extractor 6 which detects the internal pressure difference between the charging hopper 3 and the blast furnace 1, and the charging hopper 3 are supplied with nitrogen to supply the nitrogen to the blast furnace 1 and the equal pressure. And a distribution device 8 for distributing the contents into the blast furnace 1 by operating at a set tilt angle and turning speed at a lower end of the charging hopper 3 to achieve a pressure equalizing control valve 7. Doing.

상기와 같은 고로설비에서의 장입과정을 설명하면, 원료인 철광석과 연료인 코크스가 미리 정해놓은 순서에 따라서, 운반장치(2)를 타고 장입호퍼(3)로 운반되고, 상기 장입호퍼(3)로부터 차례대로 고로(1)의 내부로 장입되어, 용선으로 생산되는데, 이때, 높은 압력을 갖는 고로(1)로의 장입이 용이하게 이루어지게 하기 위하여, 장입호퍼(3)의 내부 압력이 고로(1) 상부의 압력(대략 1.5 ~ 2.5 kg/㎠)과동일한 상태가 되도록, 장입호퍼(3)에 고로가스와 질소등을 충압한 후, 장입호퍼(3)와 고로(1)의 차압이 제로가 될때, 분배장치(8)를 통해 장입이 이루어진다.Referring to the charging process in the blast furnace installation as described above, in accordance with a predetermined order of the raw material iron ore and fuel coke, is carried to the charging hopper (3) by the transport device 2, the charging hopper (3) The internal pressure of the charging hopper (3) is charged into the blast furnace (1) in order to make it easy to charge into the blast furnace (1) in order from the inside of the blast furnace (1) in order to facilitate the charging into the blast furnace (1) having a high pressure from ) After charging the blast furnace gas and nitrogen to the charging hopper 3 so as to be in the same state as the upper pressure (approximately 1.5 to 2.5 kg / cm 2), the differential pressure between the charging hopper 3 and the blast furnace 1 becomes zero. When done, charging is done via the dispensing device 8.

이때, 고로(1)내부에서 코크스층, 광석층과 교대로 일정한 층을 형성하고, 그 장입물의 형상을 부분별로 분할한다. 상기 분할된 각 부분을 노치(notch)(10)라 한다. 그리고, 노치별로 장입되는 장입물의 량은 미리 선회수와 경동각이 정해진 테이블에 의해 분배장치(8)가 회전하는 동안 장입되며, 이때 발생되는 호퍼(3)의 무게변화는 중량검출장치(5)에 의해 검출되어 공정제어컴퓨터(도시생략)로 전달됨으로서, 운전자가 모니터를 통해 장입물의 변화추이를 확인할 수 있도록 하고 있다.At this time, a constant layer is formed alternately with the coke layer and the ore layer in the blast furnace 1, and the shape of the charge is divided into parts. Each divided part is referred to as a notch 10. In addition, the amount of the charged material for each notch is charged while the distribution device 8 is rotated by a predetermined number of turns and tilt angles, and the weight change of the hopper 3 generated at this time is the weight detection device 5. It is detected by the controller and transmitted to the process control computer (not shown), so that the driver can check the change of the charge through the monitor.

그러나, 이는 장입호퍼(3)의 무게만을 알수 있기 때문에, 장입의 진행상태만을 알 수 있는 것이지, 실제 장입물이 고루게 분포되어 고로(1)내부에 정확하게 각 노치별로 장입되었는지는 확인할 수 없다.However, since only the weight of the charging hopper 3 can be known, only the progress of the charging can be known, and it is not possible to confirm whether the actual charging is evenly distributed and the charging of each notch in the blast furnace 1 is accurate.

따라서, 상술한 기존의 방식으로 장입이 이루어지면, 고로설비에 다양한 이상조건들이 발생될 때, 고로(1)내부로 장입물이 일정하게 배출되지 못하게 되고 그 결과 각 노치(9)에 정확한 양이 분배될 수 없다는 문제점이 발생한다. 상기에서, 이상조건의 예를 들면, 첫째로, 장입과정에서 고로내부의 압력과 호퍼내부의 압력과의 차압이 불안정한 경우, 둘째로 장입물의 입도변화가 크게 발생되는 경우, 세번째로, 호퍼(3) 하단부를 개폐하는 밸브(11) 혹은 분배장치(8)에 기계적인 편차가 발생되는 경우 등이 있다.Therefore, when charging is made in the above-described conventional manner, when various abnormal conditions occur in the blast furnace installation, the contents of the filling cannot be constantly discharged into the blast furnace 1, and as a result, the exact amount of each notch 9 The problem arises that it cannot be distributed. In the above, for example, in the case of abnormal conditions, firstly, when the differential pressure between the pressure inside the blast furnace and the pressure inside the hopper in the charging process is unstable, and secondly, when the particle size change of the charge is largely generated, thirdly, the hopper 3 A mechanical deviation may occur in the valve 11 or the distribution device 8 that opens and closes the lower end.

또한, 종래에는 각 노치별로 미리 정해높은 선회수만큼 분배장치가 회전하면서 장입물을 뿌리고나면, 실제 장입량과 관계없이 다음 노치로 이동하여 정해진 만큼 회전하면서 장입을 하도록 되어있기 때문에, 호퍼(3)에서 배출되는 속도 및 장입량의 변동과는 무관하게 장입이 진행되고, 그 결과, 장입상태가 불량시 적절한 대처가 불가능하게 된다.In addition, in the hopper (3), conventionally, after dispensing the charge while the dispensing device is rotated by a high number of turns, which is predetermined for each notch, it moves to the next notch regardless of the actual charge amount and rotates by the predetermined amount. Charging proceeds irrespective of fluctuations in the discharge rate and the charging amount, and as a result, proper charging is impossible when the charging state is poor.

그리고, 장입물의 분포층이 변동되면, 가스가 고로(1) 내부에서 불규칙하게 흐르게 되기 때문에, 노황이 악화되어 생산성이 저하된다.And when the distribution layer of a charged material fluctuates, since gas will flow irregularly in the blast furnace 1, yellowing will worsen and productivity will fall.

그리고, 기존에는 슈트의 선회수와 실적수가 일치되지 않아 장입상태가 불량해지면, 호퍼(3)의 하부에 설치된 밸브(11)의 개도를 변경하여 조정하도록 되어 있는데, 상술한 다양한 이상조건이 유지되는 한, 이 것으로는 장입상태 불량을 해결할 수 없게 되는 문제점이 있었다.In the past, when the number of turns of the chute and the number of performances do not match, and the charging state becomes poor, the opening degree of the valve 11 installed in the lower portion of the hopper 3 is changed and adjusted, but the various abnormal conditions described above are maintained. However, this problem has a problem that can not solve the charging state defects.

본 발명은 상술한 종래의 문제점을 해결하기 위하여 제안된 것으로서, 코크스 장입시 분배장치가 회전하게 될 총시간을 계산하고 이를 장입호퍼의 무게변화로 연산하고 실제 장입물의 배출량과 비교하여 편차발생시 균압제어용 질소량을 조정함으로서 장입물 배출을 일정하게 조절하고자 한 고로설비에서의 장입제어장치를 제공하는데 그 목적이 있다.The present invention has been proposed in order to solve the above-mentioned conventional problems, and calculates the total time that the distribution device will rotate when charging the coke, calculates this as the weight change of the charging hopper and compares the discharge with the actual loading of the equalizer It is an object of the present invention to provide a charging control device in a blast furnace facility that is intended to control the discharge of the charge constantly by adjusting the amount of fish nitrogen.

도 1은 고로조업에서의 장입설비를 보인 공정구성도이다.1 is a process configuration diagram showing a charging facility in the blast furnace operation.

도 2는 본 발명에 따른 장입제어장치를 도시한 구성도이다.2 is a block diagram showing a charging control apparatus according to the present invention.

도 3은 본 발명에 따른 장입제어장치의 동작 흐름도이다.3 is an operation flowchart of a charging control apparatus according to the present invention.

도 4의 (a)는 장입시 시간별 장입호퍼의 중량 변화를 나타내는 그래프이고, (b)는 장입편차량과 질소변화량과의 관계를 보인 그리프이다.Figure 4 (a) is a graph showing the weight change of the charging hopper with the time of charging, (b) is a glyph showing the relationship between the amount of loading deviation and the nitrogen change.

*도면의 주요 부분에 대한 부호의 설명** Description of the symbols for the main parts of the drawings *

21 ~ 23 : 제1~3연산부21 ~ 23: 1st ~ 3rd operation part

24 : 감산부24: subtraction part

25 : 비율기25: proportioner

26 : 설정부26: setting unit

27 : 선택부27: selection unit

28 : 차압조절부28: differential pressure control unit

본 발명은 상술한 목적을 달성하기 위한 구성수단으로서, 고로상부에 위치하는 장입호퍼와 장입호퍼로 질소를 공급/차단하는 균압용 제어밸브를 포함하는 고로설비의 장입제어장치에 있어서,The present invention provides a charging control apparatus for blast furnace equipment comprising a charging hopper located in the upper part of the blast furnace and a pressure equalizing control valve for supplying / blocking nitrogen to the charging hopper as an element for achieving the above object.

장입호퍼의 중량을 검출값을 출력하는 중량지시부;A weight indicating unit for outputting a detection value of the weight of the charging hopper;

장입개시가 되면 선회횟수에 단위시간당 선회시간을 곱하여 선회시간을 실시간계산하는 제1연산부;A first calculation unit which calculates the turning time in real time by multiplying the turning number by the turning time per unit time when charging is started;

상기 중량지시부로부터 검출된 호퍼 중량값을 상기 제1연산부에서 계산된 총 선회시간으로 나누어 단위시간당 장입량 목표값을 산출하는 제2연산부;A second calculation unit which calculates a charging target value per unit time by dividing the hopper weight value detected from the weight indicating unit by the total turning time calculated by the first calculating unit;

상기 중량지시부로부터 출력되는 중량검출값을 입력받아 단위시간당 실제 장입량을 산출하는 제3연산부;A third calculation unit which receives a weight detection value output from the weight indicating unit and calculates an actual charging amount per unit time;

상기 제2,3연산부에서 산출된 단위시간당 실제 장입량과 목표값의 편차를 구하는 감산부;A subtraction unit for obtaining a deviation between the actual charge amount and the target value per unit time calculated by the second and third calculation units;

장입호퍼로 공급되는 질소량과 장입량과의 관계를 통해 상기 감산부로부터 출력되는 편차를 보상하는 질소값을 산출하는 비율기; 및A proportioner for calculating a nitrogen value for compensating for the deviation output from the subtracting unit through the relationship between the amount of nitrogen supplied to the charging hopper and the charging amount; And

장입시 상기 장입호퍼와 고로의 압력이 균일하도록 균압용 제어밸브를 조정하면서, 상기 비율기로부터 장입량편차를 보상하는 질소량 보상값에 따라 균압용 제어밸브의 개도를 조정하는 차압조절부를 포함하는 것을 특징으로 한다.And a differential pressure control unit for adjusting the opening degree of the equalizing control valve according to the nitrogen amount compensation value for compensating the charging amount deviation from the proportioner while adjusting the equalizing control valve so that the pressure between the charging hopper and the blast furnace is uniform during charging. It is done.

이하, 첨부한 도면을 참조하여 본 발명에 따른 고로설비에서의 장입제어장치에 대하여 설명한다.Hereinafter, with reference to the accompanying drawings will be described a charging control device in the blast furnace installation according to the present invention.

고로설비에 있어서, 실제 장입시에 철광석은 상당한 중량물이기 때문에 여러 장입조건이 변하더라도 크게 영향을 받지 않아 목표된 량만큼 정확하게 노치에 분포시킬 수 있으나, 코크스는 철광석에 비하여 가볍기 때문에, 작은 장입조건 변동에도 호퍼(3)에서 배출되는 량이 크게 변동한다.In blast furnace installations, iron ore is a considerable weight at the time of actual charging, so even if various charging conditions are not affected, it can be distributed to the notch exactly as the target amount, but because the coke is lighter than iron ore, Edo discharged from the hopper 3 greatly varies.

본 발명은 이러한 점을 감안하여 제안된 것으로서, 고로설비에 여러 이상요인이 발생되어도 코크스의 안정된 장입이 가능하도록, 코크스 순시 장입량을 검출하고, 이를 장입량 목표치와 비교하여, 그 편차에 비례하여 장입호퍼로 유입되는 질소량이 조절시키는 것이다. 상기 장입호퍼로 유입되는 질소량은 상술한 여러 이상요인들보다 코크스 장입에 더 큰 영향을 미치기 때문에, 이상요인이 발생되더라도 코크스 순시 장입량의 제어가 가능한 것이다.The present invention has been proposed in view of such a point, and detects the instantaneous coke loading amount, and compares it with the loading target value, so as to enable stable charging of coke even when various abnormalities are generated in the blast furnace equipment, and the charging hopper in proportion to the deviation It is to control the amount of nitrogen flowing into. Since the amount of nitrogen flowing into the charging hopper has a greater influence on the coke charging than the above-described various abnormal factors, the instantaneous loading of the coke can be controlled even if an abnormal factor is generated.

도 2는 본 발명에 따른 장입제어장치의 구성을 보인 블럭도로서, 본 장치(100)는 장입호퍼(3)의 중량을 검출하는 로드셀(5)의 출력신호를 중량검출값으로 변환출력하는 중량지시부(20)와, 장입개시가 되면 선회횟수에 단위시간당 선회시간을 곱하여 선회시간을 실시간계산하는 제1연산부(21)와, 상기 중량지시부(20)로부터 검출된 호퍼 중량값을 상기 제1연산부(21)에서 계산된 총 선회시간으로 나누어 단위시간당 장입량 목표값을 산출하는 제2연산부(22)와, 상기 중량지시부(20)로부터 출력되는 중량검출값을 입력받아 단위시간당 실제 장입량을 산출하는 제3연산부(23)와, 상기 제2,3연산부(22,23)에서 산출된 단위시간당 실제 장입량과 목표값의 편차를 구하는 감산부(24)와, 호퍼(3)로 공급되는 질소량과 장입량과의 관계를 통해 상기 감산부(24)로부터 출력되는 편차를 보상하는 질소값을 산출하는 비율기(25)와, 호퍼(3)로 공급되는 질소량을 설정하는 설정부(26)와, 상기 설정부(26)의 질소량설정값 또는 상기 비율기(25)로부터 출력된 장입편차를 보상하는 질소량설정값중 하나를 선택하여 목표값으로 출력하는 선택부(27)와, 상기 선택부(27)의목표값과 차압검출기(6)의 호퍼와 고로상부간의 차압을 입력받아 PID연산에 의해 차압이 보상되는 한에서 목표값만큼의 질소가 공급되도록 균압용제어밸브(7)의 개도를 조절하는 차압조절부(28)를 포함하여 이루어진다.2 is a block diagram showing a configuration of a charging control device according to the present invention, in which the apparatus 100 converts and outputs an output signal of a load cell 5 that detects the weight of the charging hopper 3 into a weight detection value. The first calculation unit 21 and the first calculation unit 21 for calculating the turning time in real time by multiplying the turning number by the turning time per unit time when the charging is started, and the hopper weight value detected by the weight indicating unit 20. A second calculation unit 22 for calculating a target amount of charge per unit time divided by the total turning time calculated in (21) and a weight detection value output from the weight indicating unit 20 to calculate an actual charge amount per unit time; The calculation unit 23, the subtraction unit 24 for calculating the deviation between the actual charge amount and the target value per unit time calculated by the second and third calculation units 22 and 23, the amount of nitrogen supplied to the hopper 3, Is outputted from the subtractor 24 through The proportioner 25 which calculates the nitrogen value which compensates a difference, the setting part 26 which sets the amount of nitrogen supplied to the hopper 3, the nitrogen amount setting value of the said setting part 26, or the said proportioner 25 Selector 27 for selecting one of the nitrogen amount set value to compensate the charging deviation output from the output as a target value, between the target value of the selector 27 and the hopper of the differential pressure detector 6 and the upper part of the blast furnace It includes a differential pressure control unit 28 for adjusting the opening degree of the pressure equalizing control valve 7 so that the nitrogen as much as the target value is supplied as long as the differential pressure is compensated by the PID operation.

도 3은 본 발명에 따른 장입제어장치의 동작을 순서에 따라 도시한 플로우챠트로서, 도 3의 플로우챠트를 참조하여 상기 장치의 동작을 설명한다.3 is a flowchart showing the operation of the charging control apparatus according to the present invention in order, and the operation of the apparatus will be described with reference to the flowchart of FIG.

장입호퍼(3)에 코크스가 채워지면, 균압용 제어밸브(7)이 오픈되어 질소가 장입호퍼(3)로 공급된다. 이에, 상기 장입호퍼(3)의 압력이 고로(1) 상부의 압력과 같아지면, 공정제어컴퓨터(도시생략)의 제어에 의해 코크스가 장입호퍼(3)에서 고로(1)로 장입되기 시작한다.When coke is filled in the charging hopper 3, the equalizing control valve 7 is opened and nitrogen is supplied to the charging hopper 3. Therefore, when the pressure of the charging hopper 3 is equal to the pressure of the upper part of the blast furnace 1, coke starts to be charged from the charging hopper 3 to the blast furnace 1 by control of a process control computer (not shown). .

이때, 본 발명에 따른 장입제어장치(100)의 동작도 시작된다.At this time, the operation of the charging control device 100 according to the present invention is also started.

즉, 장입호퍼(3)로부터 고로(1)로 장입이 시작되면서, 장입호퍼(3)의 장입물 중량변화가 로드셀(5)에서 검출되어 중량지시부(20)로 전달되고, 중량지시부(20)는 로드셀(5)의 신호에 따라 장입호퍼(3)내의 장입물 현재 중량값을 실시간 출력한다(S302). 상기 중량지시부(20)의 검출값은 제3연산부(23)로 입력되고, 상기 제3연산부(23)는 t초전의 중량값과 현재의 중량값의 차를 t초로 나누어 된, 단위시간당 실제 장입중량을 계산한다(S303). 도 4의 (a)는 장입시 시간별 장입호퍼의 중량 변화를 나타내는 그래프로서, 도시된 바와 같이, 본 단계에서는 단위시간에 대한 단위중량변화를 검출한다.That is, as charging is started from the charging hopper 3 to the blast furnace 1, the change in the weight of the charging hopper 3 is detected by the load cell 5 and transmitted to the weight indicating unit 20, the weight indicating unit 20 In accordance with the signal of the load cell 5 outputs the current weight value of the charge in the charging hopper (3) (S302). The detection value of the weight indicating unit 20 is input to the third operation unit 23, and the third operation unit 23 is the actual charging per unit time, divided by t seconds, the difference between the weight value before t seconds and the current weight value. The weight is calculated (S303). Figure 4 (a) is a graph showing the weight change of the charging hopper for each time at the time of charging, as shown, in this step, the unit weight change with respect to the unit time is detected.

그리고, 본 장치(100)에서 장입편차를 실시간으로 계산하기 위한 연산과정이 실행되는데, 먼저, 제1연산부(21)에서 분배장치(8)의 선회수 및 경동각도를 셋팅해논 설정테이블(미도시)로부터 분배장치(8)의 선회수를 읽어들여, 현재 총 선회횟수에 1회선회시간을 곱하여, 총 선회시간을 계산한다(S304).In addition, a calculation process for calculating the charging deviation in real time in the apparatus 100 is executed. First, a setting table for setting the number of revolutions and the tilt angle of the distribution apparatus 8 in the first calculation unit 21 (not shown) The number of turns of the distribution device 8 is read from the time), and the total number of turns is multiplied by one turn time to calculate the total turn time (S304).

그 다음, 제2연산부(22)는 상기 중량지시부(20)로부터 출력된 장입물 중량을 상기 제1연산부(21)에 의해 산출된 총 선회시간으로 나누어 단위시간당 목표 장입중량값을 계산한다(S306).Next, the second calculation unit 22 calculates a target charging weight value per unit time by dividing the weight of the charge output from the weight indicating unit 20 by the total turning time calculated by the first calculation unit 21 (S306). ).

이상과 같이 구해진, 단위시간당 실제 장입량과 단위시간당 목표장입량의 편차는 감산부(24)에서 계산되고(S307), 비율기(25)는 목표장입량에 대한 실제 장입량의 증감정도에 따라서, 그 만큼을 보상하여 장입량을 증감시킬 수 있는 질소량을 출력한다(S308).The deviation between the actual charge amount per unit time and the target charge amount per unit time obtained as described above is calculated by the subtractor 24 (S307), and the proportioner 25 is adjusted according to the degree of increase or decrease of the actual charge amount with respect to the target charge amount. Compensation outputs an amount of nitrogen that can increase or decrease the amount of loading (S308).

즉, 도 4의 (b)에 도시한 바와 같이, 목표장입량에 대한 실제장입량의 편차에 대한 편차보상가능한 질소량 변화량과의 관계가 나타나는데, 이는 장입호퍼(3)와 고로(1)의 압력이 균압된 상태에서, 단위시간당 장입량이 소정치일때, 장입호퍼(3)의 압력을 고로(1)보다 소정치 높이면, 그만큼 단위시간당 장입량이 증가하고, 장입호퍼(3)의 압력이 고로(1)보다 낮아지면 단위시간당 장입량이 감소하는 관계를 이용한 것이다. 도 4b의 그래프에서, 장입량편차값은 -30kg/sec ~ 30kg/sec의 범위로 나타나 있는데, 이 범위를 벗어나는 편차량은 제어가능한 범위를 벗어나므로, 본 장치(100)의 제어범위에서 제외시킨다. 상기 범위의 입력에 대한 출력(보상질소량)은 -0.03 ~ 0.1kg/㎠이다. 그리고, 상기 그래프에서 질소량 변화량이 0인 장입물 편차량 0.023kg/㎠ 은 앞서 설명한 고로설비의 여러 이상요인이 발생하지 않은 정상상태에서, 안정된 장입상태를 유지할 수 있는 값으로서, 반복적인 테스트를 통해서 얻어진 값이며, 상기 값(0.023kg/㎠)을 기준으로 편차량이 증감하여 그 만큼 질소량이 가변시킨다.That is, as shown in (b) of FIG. 4, the relationship between the variation of the amount of nitrogen that can be compensated for the deviation of the actual loading with respect to the target loading is shown, which means that the pressure between the charging hopper 3 and the blast furnace 1 is equalized. In the state where the charging amount per unit time is a predetermined value, when the pressure of the charging hopper 3 is higher than the blast furnace 1 by a predetermined value, the charging amount per unit time increases by that amount, and the pressure of the charging hopper 3 is higher than that of the blast furnace 1. If it is lowered, the amount of charge per unit time decreases. In the graph of Figure 4b, the charge amount deviation value is shown in the range of -30kg / sec ~ 30kg / sec, the deviation amount out of this range is out of the controllable range, and therefore excluded from the control range of the apparatus 100. The output (compensated nitrogen amount) for the input in the above range is -0.03 to 0.1 kg / cm 2. In addition, in the graph, 0.023kg / cm2 of the loading amount of change of nitrogen amount of 0 is a value capable of maintaining a stable charging state in a steady state in which various abnormalities of the blast furnace facility described above do not occur, and through repeated tests. This value is obtained, and the amount of deviation is increased or decreased based on the value (0.023 kg / cm 2), and the amount of nitrogen is varied accordingly.

상기와 같이, 장입량 편차를 보정하는 질소량보정치가 계산되면, 이는 선택부(27)를 통해 차압조절부(28)로 입력되며, 차압조절부(28)는 PID제어에 의해 상기 보정치 만큼의 질소량이 증/감되도록 균압용 제어밸브(7)의 개도를 조절한다(S308). 상기 차압조절부(28)의 작용은 이미 적용되는 것으로서, 일반적으로 잘 알려져 있으므로 그 구체적인 설명은 생략한다.As described above, when the nitrogen amount correction value for correcting the loading amount deviation is calculated, it is input to the differential pressure control unit 28 through the selection unit 27, the differential pressure control unit 28 is the amount of nitrogen as the correction value by the PID control The opening degree of the equalization control valve 7 is adjusted to increase / decrease (S308). The action of the differential pressure control unit 28 is already applied, and since it is generally known, a detailed description thereof will be omitted.

상기 도 2의 구성에서, 설정부(26)는 상술한 이상요인이 발생하지 않는 정상상태에서, 목표하는 단위장입량이 정상적으로 장입되도록 하는 질소량 설정값을 설정하고 있으며, 선택부(27)에 의하여 정상상태에서는 상기 설정부(26)의 설정값이 질소량 설정값으로 차압조절부(28)에 인가되다다가, 이상요인 발생시에는 설정부(26)의 값이 차단되고, 비율기(25)로부터 출력되는 보정된 질소량이 목표값으로서 차압조절부(28)에 인가된다.In the configuration of FIG. 2, the setting unit 26 sets a nitrogen amount setting value so that the target unit charging amount is normally charged in the normal state in which the above-described abnormal factors do not occur, and is selected by the selecting unit 27. In the state, the setting value of the setting unit 26 is applied to the differential pressure control unit 28 as the nitrogen amount setting value, and when an abnormal factor occurs, the value of the setting unit 26 is cut off and outputted from the proportioner 25. The corrected nitrogen amount is applied to the differential pressure control unit 28 as a target value.

상술한 바에 의하면, 본 발명은 장입물의 실제 배출량을 순시계산하여 편차값을 안정시키도록 장입호퍼로 유입되는 질소량을 조정함으로서, 고로설비에서 장입량의 편차발생 원인이 되는 여러 이상요인들이 발생하더라도, 질소량 증감을 통하여 장입물의 즉시보상이 이루어져 편차폭을 최소화시킬 수 있는 효과가 있으며, 그로부터 코크스의 안정된 장입을 이룩하여 노황악화 및 생산성저하를 개선시킬 수 있는 우수한 효과가 있다.According to the above description, the present invention adjusts the amount of nitrogen flowing into the charging hopper to stabilize the deviation value by forward-calculating the actual discharge amount of the charged product, and thus, even if various abnormalities causing the deviation of the charged amount occur in the blast furnace equipment, Immediate compensation of the charges through the increase and decrease has the effect of minimizing the width of the deviation, there is a good effect to improve the deterioration and degradation of productivity by achieving a stable charging of coke from there.

Claims (2)

고로상부에 위치하는 장입호퍼와 장입호퍼로 질소를 공급/차단하는 균압용 제어밸브를 포함하는 고로설비의 장입제어장치에 있어서,In the charging control device of the blast furnace installation comprising a charging hopper located in the upper part of the blast furnace and a pressure equalizing control valve for supplying / blocking nitrogen to the charging hopper, 장입호퍼의 중량을 검출값을 출력하는 중량지시부;A weight indicating unit for outputting a detection value of the weight of the charging hopper; 장입개시가 되면 선회횟수에 단위시간당 선회시간을 곱하여 선회시간을 실시간계산하는 제1연산부;A first calculation unit which calculates the turning time in real time by multiplying the turning number by the turning time per unit time when charging is started; 상기 중량지시부로부터 검출된 호퍼 중량값을 상기 제1연산부에서 계산된 총 선회시간으로 나누어 단위시간당 장입량 목표값을 산출하는 제2연산부;A second calculation unit which calculates a charging target value per unit time by dividing the hopper weight value detected from the weight indicating unit by the total turning time calculated by the first calculating unit; 상기 중량지시부로부터 출력되는 중량검출값을 입력받아 단위시간당 실제 장입량을 산출하는 제3연산부;A third calculation unit which receives a weight detection value output from the weight indicating unit and calculates an actual charging amount per unit time; 상기 제2,3연산부에서 산출된 단위시간당 실제 장입량과 목표값의 편차를 구하는 감산부;A subtraction unit for obtaining a deviation between the actual charge amount and the target value per unit time calculated by the second and third calculation units; 장입호퍼로 공급되는 질소량과 장입량과의 관계를 통해 상기 감산부로부터 출력되는 편차를 보상하는 질소값을 산출하는 비율기; 및A proportioner for calculating a nitrogen value for compensating for the deviation output from the subtracting unit through the relationship between the amount of nitrogen supplied to the charging hopper and the charging amount; And 장입시 상기 장입호퍼와 고로의 압력이 균일하도록 균압용 제어밸브를 조정하면서, 상기 비율기로부터 장입량편차를 보상하는 질소량 보상값에 따라 균압용 제어밸브의 개도를 조정하는 차압조절부를 포함하는 것을 특징으로 하는 고로설비에서의 장입제어장치.And a differential pressure control unit for adjusting the opening degree of the equalizing control valve according to the nitrogen amount compensation value for compensating the charging amount deviation from the proportioner while adjusting the equalizing control valve so that the pressure between the charging hopper and the blast furnace is uniform during charging. Charge control device in blast furnace equipment. 제 1 항에 있어서, 상기 비율기는 장입량 편차입력은 -30 ~ 30kg/sec 의 범위이고, 출력되는 보상질소량은 -0.03~0.1 kg/㎠인 것을 특징으로 하는 고로설비에서의 장입제어장치.The charging control apparatus of the blast furnace installation according to claim 1, wherein the proportional input amount of the deviation is in the range of -30 to 30 kg / sec, and the amount of compensated nitrogen output is -0.03 to 0.1 kg / cm 2.
KR1020010069129A 2001-11-07 2001-11-07 Cokes input control apparatus in blast furnace KR20030038922A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100784135B1 (en) * 2006-12-15 2007-12-12 주식회사 포스코 Basis weight detection device of coke in the bucket
KR100858898B1 (en) * 2007-06-20 2008-09-17 주식회사 포스코 Cokes detection device of coke in the bucket
KR20160019389A (en) 2014-08-11 2016-02-19 다이오코리아(주) Weighing method using a pressure correction in accordance with the mineral species

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59229407A (en) * 1983-06-09 1984-12-22 Kawasaki Steel Corp Method for controlling opening degree of flow regulating gate of bell-less blast furnace
JPH0711313A (en) * 1993-06-29 1995-01-13 Kawasaki Steel Corp Control method for blowing of pulverized coal
JPH0892616A (en) * 1994-09-21 1996-04-09 Kawasaki Steel Corp Operation of coke packed bed type smelting reduction furnace
KR19990038977A (en) * 1997-11-08 1999-06-05 이구택 Charge distribution device of blast furnace
KR20010061636A (en) * 1999-12-28 2001-07-07 이구택 Apparatus for controlling pressure in hopper of blast furnace

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59229407A (en) * 1983-06-09 1984-12-22 Kawasaki Steel Corp Method for controlling opening degree of flow regulating gate of bell-less blast furnace
JPH0711313A (en) * 1993-06-29 1995-01-13 Kawasaki Steel Corp Control method for blowing of pulverized coal
JPH0892616A (en) * 1994-09-21 1996-04-09 Kawasaki Steel Corp Operation of coke packed bed type smelting reduction furnace
KR19990038977A (en) * 1997-11-08 1999-06-05 이구택 Charge distribution device of blast furnace
KR20010061636A (en) * 1999-12-28 2001-07-07 이구택 Apparatus for controlling pressure in hopper of blast furnace

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100784135B1 (en) * 2006-12-15 2007-12-12 주식회사 포스코 Basis weight detection device of coke in the bucket
KR100858898B1 (en) * 2007-06-20 2008-09-17 주식회사 포스코 Cokes detection device of coke in the bucket
KR20160019389A (en) 2014-08-11 2016-02-19 다이오코리아(주) Weighing method using a pressure correction in accordance with the mineral species

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