KR950012396B1 - Control method of blast f'ce gas distribution - Google Patents

Control method of blast f'ce gas distribution Download PDF

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KR950012396B1
KR950012396B1 KR1019930023737A KR930023737A KR950012396B1 KR 950012396 B1 KR950012396 B1 KR 950012396B1 KR 1019930023737 A KR1019930023737 A KR 1019930023737A KR 930023737 A KR930023737 A KR 930023737A KR 950012396 B1 KR950012396 B1 KR 950012396B1
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gas
flow rate
furnace
distribution
blast furnace
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KR1019930023737A
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KR950014319A (en
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최태화
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포항종합제철주식회사
조말수
재단법인산업과학기술연구소
백덕현
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    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B7/00Blast furnaces
    • C21B7/24Test rods or other checking devices
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B5/00Making pig-iron in the blast furnace

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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)
  • Blast Furnaces (AREA)

Abstract

The predicting method for gas distribution improves the usage of gases and the lifetime of a blast furnace by using the accurate information of gas distribution. The predicting method comprises(A) calculating several parameters of sinter, cokes and gas from the empirical equations; (B) obtaining mass velocity of gas from the pressure gradient equation substituting the calculated parameters; (C) calculating gas mole percentage.

Description

고로 노내 가스류 분포 추정방법Estimation method of blast furnace gas flow distribution

제1도는 고로 노경방향의 등면적 분할부분을 나타내는 참고도.1 is a reference diagram showing an isosphere divided part in the blast furnace direction.

제2도는 본 발명에 따라 추정되는 고로의 중심류, 중간류 및 주변류의 분포비를 나타내는 삼각형 그래프.2 is a triangular graph showing the distribution ratio of the central, intermediate and peripheral flows of the blast furnace estimated according to the present invention.

제3도는 본 발명에 따라 추정된 고로 노내 가스류 분포 추정결과도.3 is a blast furnace gas flow distribution estimation result estimated according to the present invention.

본 발명은 고로공정에서 괴상대의 노경방향 가스류 분포를 추정하는 방법에 관한 것으로써, 보다 상세하게는, 괴상대와 노정간의 노경방향의 압력손실 분포를 구하여 고로 노내 가스류 분포를 추정하는 방법에 관한 것이다.The present invention relates to a method for estimating the distribution of gas flow in the blast furnace in the blast furnace process, and more particularly, to a method for estimating the distribution of gas flow in the blast furnace by obtaining the pressure loss distribution in the blast furnace direction between the mass and the blast furnace. It is about.

고로조업에 있어서 노내의 장입물과 노하부에서 생성된 환원가스는 접촉을 잘하여 철광석의 환원과 용해가 적절히 잘 이루어지도록 유지하는 것이 중요하다.In the blast furnace operation, it is important to keep the charges in the furnace and the reducing gas produced at the bottom of the furnace in good contact so that the reduction and dissolution of iron ore is properly performed.

노내 가스의 편류가 발생하게 되면 철광석의 환원이 불균일하게 되어 노하부의 광석의 용융레벨이 균형을 잃게 되어 slip & drop등 장입물 강하의 이상이 발생한다.If the fluctuation of gas in the furnace occurs, the reduction of iron ore will be uneven, and the melting level of the ore at the bottom of the furnace will be unbalanced, causing abnormalities in charge dropping, such as slip & drop.

그러므로 우선 노내의 가스류분포를 파악하는 것이 필요하다. 종래의 가스류 분포를 예측하는 방법은 노내의 온도가 고온이고 노내 가스중 분진이 많아서 가스유속을 직접 측정하는 것이 곤란하여 노내 가스의 온도나 가스성분분포를 이용하여 간접적으로 추정하는 방법을 많이 사용하고 있다. 또한 송풍시와 휴풍시의 장입표면의 경사비와 노내 가스 유속과의 관련성으로부터 노내 가스류 분포를 간접적인 추정방법[일본특허 공보 소60-39725]과 유체의 유동방정식에 의한 수식모델에 의한 수정방법[M. Kuwabara, I. Much, Tetsu-to-hagane, Vol.62, No.5, P3(1976)등이 있다. 전자의 경우에는 장입물의 경사각은 장입방식(장입모드)의 변경에 따라 크게 영향을 받아서 장입방식이 변경되면 정확한 가스류분포를 추정할 수 없으며, 후자의 경우에는 계산상 많은 데이터를 필요로 하고, 실제 고로상황이 충분히 고려되지 않은 유동방정식에 의해 계산이 되므로 역시 정확한 추정을 할 수 없는 문제점이 있다.Therefore, it is necessary to first understand the gas flow distribution in the furnace. Conventional methods for estimating the distribution of gas flows are difficult to measure the gas flow rate directly because the temperature in the furnace is high and there is a lot of dust in the gas. Therefore, many methods are used to estimate the gas flow indirectly by using the temperature or gas component distribution of the gas in the furnace. Doing. In addition, indirect estimation of the distribution of gas flow in the furnace from the relationship between the inclination ratio of the charged surface and the gas flow velocity during the blowing and in the absence of air flow (Japanese Patent Publication No. 60-39725) and the correction by the mathematical model using the fluid equation Method [M. Kuwabara, I. Much, Tetsu-to-hagane, Vol. 62, No. 5, P3 (1976). In the former case, the inclination angle of the charged material is greatly influenced by the change of the charging method (charging mode), so that the accurate gas flow distribution cannot be estimated when the charging method is changed, and the latter requires a lot of data for calculation. Since the actual blast furnace situation is calculated by a flow equation that is not sufficiently considered, there is also a problem that cannot be accurately estimated.

따라서, 본 발명은 괴상대에서 노경방향의 압력손실 분포를 구하고 이를 이용하여 노경방향 가스류 분포를 추정하므로써, 보다 정확하게 고로 노내 가스류 분포를 추정할 수 있는 방법을 제공하고자 하는데, 그 목적이 있다.Accordingly, an object of the present invention is to provide a method for more accurately estimating the gas flow distribution in a blast furnace by obtaining the pressure loss distribution in the furnace direction and estimating the gas flow distribution in the furnace using the same. .

이하, 본 발명에 대하여 상세히 설명하다.Hereinafter, the present invention will be described in detail.

본 발명은, 고로 노내 가스류 분포를 추정하는 방법에 있어서, 괴상대에서 노경방향으로 3등분하여 중심부, 중간부 및 주변부로 등면적 구획하는 단계; 소결광 및 코크스의 평균입경, 입도편석지수, 공극률, 및 형상계수와 노내 가스점도 및 가스밀도를 추정하는 단계; 상기와 같이 측정된 값을 압력손실식에 대입하여 상기와 같이 구획된 각 부분에 있어서의 가스 질량 유속을 구하는 단계; 상기 가스 질량 유속을 표준상태의 부피유량으로 환산한 후 노경방향의 가스유량분율을 구하여 노내 가스류 분포를 추정하는 단계를 포함하여 구성되는 고로 노내 가스류 분포 추정방법에 관한것이다.The present invention relates to a method for estimating the distribution of gas flow in a blast furnace, the method comprising: dividing an area into three parts in the direction of the furnace from the masses to the center, the middle part, and the periphery; Estimating the average particle diameter, particle size segregation index, porosity, shape factor, gas viscosity and gas density of the sintered ore and coke; Substituting the value measured as above into a pressure loss equation to obtain a gas mass flow rate in each of the partitioned sections as described above; The gas flow rate estimation method in the blast furnace comprising the step of estimating the gas flow distribution in the furnace by converting the gas mass flow rate into the standard flow volume flow rate and then obtaining the gas flow fraction in the furnace direction.

이하, 본 발명에 대하여 보다 상세히 설명한다.Hereinafter, the present invention will be described in more detail.

본 발명에 따라 고로 노내 가스류 분포를 추정하기 위해서는 괴상대에서 노경방향으로 3등분하여 중심부, 중간부 및 주변부로 등면적 구획하여야 하는데, 이러한 구획은 노내의 가스유량 분포 추정은 제1도와 같이 노내의 가스유량과 장입물 분포가 노의 중심축을 기준으로 대칭이라고 가정하여 이루어진 것이다.According to the present invention, in order to estimate the gas flow distribution in the blast furnace, the gas flow distribution in the furnace should be divided into three sections in the direction of the furnace from the bulkhead to the center, middle, and periphery. It is assumed that the gas flow rate and the charge distribution in the chamber are symmetric about the central axis of the furnace.

다음에 , 하기식(1)∼(10)에 의해 소결광 및 코크스의 평균입경, 입도편석지수, 공극률, 및 형 상계수와 노내 가스점도 및 가스밀도를 추정한다.Next, the average particle diameter, particle size segregation index, porosity, shape factor, gas viscosity and gas density of the sintered ore and coke are estimated by the following formulas (1) to (10).

상기 식(1)∼(10)에서,In the above formulas (1) to (10),

DPS: 소결광의 평균입점(Average dineter of sinter)(mm)D PS : Average dineter of sinter (mm)

ISPS:소결광의 입도편석지수(Particle segregation index of sinter)I SPS : Particle segregation index of sinter

εS: 소결광의 공극율(Voidage of sinter)ε S : Voidage of sinter

ΦS:소결광의 형상계수(Shape factor of sinter)Φ S : Shape factor of sinter

DPC: 코크스의 평균입경( Average diameter of coke)D PC : Average diameter of coke

ISPC: 코크스의 입도편석지수(Particle segregation index of coke)I SPC : Particle segregation index of coke

εC:코크스의 공극율(Voidage of coke)ε C : Voidage of coke

ΦC: 코크스의 형상계수(Shape factor of coke)Φ C : Shape factor of coke

ρg: 가스밀도(Density of gas)(Kg/m3)ρ g : Density of gas (Kg / m 3 )

x : 노경방향거리(Length of radial direction)x: Length of radial direction

θ: 장입선회슈트의 기울기(Tilting degree of rotating chute)(radian)θ: Tilting degree of rotating chute (radian)

: 가스의 압력(Pressure of gas(Kgf/m2) : Pressure of gas (Kgf / m 2 )

: 가스의 평균분자량(Average molar mass)(Kg/Kg-mode) : Average molar mass of gas (Kg / Kg-mode)

R : 기체상수(Gas constant)(atm Nm3/K Kg-mole)R: Gas constant (atm Nm 3 / K Kg-mole)

: 가스온도(Temperature of gas)(K) : Temperature of gas (K)

μ: 가스 노내 점도μ: viscosity in gas furnace

다음에 상기와 같이 추정된 값들을 하기식(11)로 표시되는 입력손실식에 대입하여 각 구획부분의 가스류 즉, 중심류, 중간류, 주변류에 있어서의 질량유속을 구한다.Subsequently, the estimated values as described above are substituted into the input loss equation represented by the following equation (11) to find the mass flow rates in the gas flows, that is, the central flow, the intermediate flow, and the periphery of each compartment.

상기식(11)에서,In the formula (11),

△P/L : 압력 손실(Pressure drop)(Kg/m2m)△ P / L: Pressure drop (Kg / m 2 m)

ε1: 공극률(Void fraction)ε 1 : void fraction

μ1: 가스점도(Viscosity)(Kg/m/sec)μ 1 : Viscosity (Kg / m / sec)

G1: 가스질량유속(Mass velocity of gas(Kg/m2/sec)G 1 : Mass velocity of gas (Kg / m 2 / sec)

gC: 중력환산계수(Gravitational conversion factor)g C : Gravitational conversion factor

Φ1: 노내장입물의 평균형상계수(Auerage shape factor of all solid particles)Φ 1 : Auerage shape factor of all solid particles

dPI: 장입물의 평균입경(Auerage diameter of solid particle)(m)d PI : Aureage diameter of solid particle (m)

ρg: 가스밀도(Density of gas)(Kg/m3)ρ g : Density of gas (Kg / m 3 )

i : 중심부, 중간부, 주변부를 나타내는 지수i: exponent representing the center, middle and periphery

상기식(11)에서, ε1, μ1, Φ1, dP1는 다음과 같이 구해진다.In the formula (11), ε 1 , μ 1 , Φ 1 , d P1 are obtained as follows.

여기서, Wc: 코크스의 장입량Where W c : loading of coke

Ws: 소결광의 장입량W s : Loading amount of sintered ore

다음에 상기식(11)에 의해서 구해진 각 구획부에서의 가스질량 유속(G1)을, 하기식(12)∼(14)에서와 같이, 표준상태의 부피 유량(V1)로 환산한 후 노경방향의 가스유량 분율(X1)을 구하여 노내 유량분포를 추정한다.Next, after converting the gas mass flow rate (G 1 ) in each compartment obtained by the above formula (11) into a volume flow rate (V 1 ) in a standard state as in the following formulas (12) to (14), The flow rate distribution in the furnace is estimated by calculating the gas flow rate fraction X 1 in the furnace direction.

여기서 V1: i구역 표준상태의 부피유량(Nm3/min)Where V 1 : Volumetric flow rate at zone i standard condition (Nm 3 / min)

G1: i구역 질량유속(Kg/sec/m2)G 1 : i-zone mass flow rate (Kg / sec / m 2 )

A1: i구역 단면적(m2)A 1 : Area i cross section (m 2 )

P1: i구역 평균압력(atm)P 1 : Zone i average pressure (atm)

T1: i구역 평균온도(℃)T 1 : Zone i average temperature (℃)

VT: 표준상태의 총 부피유량(Nm3/min)VT: total volume flow rate in standard condition (Nm 3 / min)

ε1: i구역공극율ε 1 : i-zone porosity

ρgi: i구역 평균가스밀도(Kg/Nm3)ρ gi : mean gas density in zone i (Kg / Nm 3 )

상기와 같은 절차를 수행하므로써 고로 노내 가스류 분포를 본 발명에 따라 정확하게 추정할 수 있게 된다.By carrying out the above procedure it is possible to accurately estimate the blast furnace gas flow distribution according to the present invention.

본 발명은 주기적으로 샤프트 존데(Shaft Sonde; 고로 내부온도 측정장치)에 의해 고로 괴상대의 온도, 압력, 가스조성이 측정될 때마다 전산기에 의해 가스류 분포 추정계산이 이루어지며 제2도와 같이 삼각형 그래프 형태로 그 결과를 화면에 나타낼 수 있다. 삼각형 그래프의 3좌표 측은 각각 중심류, 중간류, 주변류이며, 퍼센트로 나타낸다.According to the present invention, the gas flow distribution estimation calculation is periodically performed by a computer whenever the temperature, pressure, and gas composition of the blast furnace mass are measured by a shaft sonde. The result can be displayed on the screen. The three coordinate sides of the triangular graph are the central flow, the middle flow, and the peripheral flow, respectively, and are expressed in percent.

결과화면은 단기간(3일간)과 장기간(10일간)의 추정결과를 나타내는 2개의 화면으로 나타낼 수 있다.The result screen may be displayed as two screens showing the estimation results of the short term (3 days) and the long term (10 days).

한편, 가장 최근 추정결과의 좌표위치를 ①로, 그 이전은 ②등으로 차례로 번호를 부여하여 표시함으로써 시계열적인 노내 가스분포의 변동추이를 용이하게 파악할 수 있다.On the other hand, the position of the coordinates of the most recent estimation result is indicated by (1), and the previous one is indicated by (2), etc. in order to easily identify the change in time-series fluctuations in the gas distribution.

이하, 실시예를 통하여 본 발명을 보다 구체적으로 설명한다.Hereinafter, the present invention will be described in more detail with reference to Examples.

[실시예]EXAMPLE

본 발명에 따라 추정된 추정결과를 고로의 크로스 존데 및 샤프트 존데에 의한 측정치와 비교하여 제3도에 나타내었다.The estimation result estimated according to the present invention is shown in FIG. 3 in comparison with the measurements by blast furnace cross sonde and shaft sonde.

제3도에 나타난 바와 같이, 고로 괴상대에서 노경방향을 비교해 볼 때 노내온도가 높은 쪽이 낮은 쪽에 비해 가스유량이 많으며, 가스이용율은 낮은 쪽이 광석/코크스비가 낮아 공극율이 높아서 가스유량이 많다고 할 수 있다. 따라서 노내 가스류 추정결과는 샤프트 존데나 크로스 존데의 측정결과와 잘 일치함을 알수 있다.As shown in FIG. 3, in the blast furnace mass zone, when comparing the direction of the furnace, the gas flow rate is higher than the one with the higher furnace temperature, and the gas utilization rate is higher because the porosity is higher because the ore / coke ratio is lower. can do. Therefore, it can be seen that the gas flow estimation results in the furnace agree well with the measurement results of shaft and cross sonde.

상술한 바와 같이, 본 발명은 고로 노내 가스류 분포를 정확히 추정함으로써, 단지 샤프트 존데에 의한 온도측정에 의해 가스분포를 추정한 종래의 방법에 비하여 노내 환원가스 이용율을 향상시키고 고로 노벽에 과다한 열부하를 막아 노체를 장수명화하여 고로의 생산원가 절감과 노내 가스류 분포 불안정에 의한 고로 노황 악화를 방지할 수 있는 효과가 있는 것이다.As described above, the present invention accurately estimates the distribution of gas flow in the blast furnace, thereby improving utilization of the reducing gas in the furnace compared to the conventional method of estimating the gas distribution only by measuring the temperature by the shaft sonde, and applying excessive heat load to the blast furnace furnace wall. By preventing the long life of the furnace body, it is possible to reduce the production cost of the blast furnace and prevent deterioration of the blast furnace due to instability in the gas flow distribution.

Claims (1)

고로노내 가스류 분포를 추정하는 방법에 있어서, 괴상대에서 노경방향으로 3등분하여 중심부, 중간부 및 주변부로 등면적 구획하는 단계; 하기식(1)∼(10)에 의해 소결광 및 코크스의 평균입경(DPS및 DPC), 입도편석지수(ISPS및 ISPC), 공극률(εS및 εC)및 형상계수(ΦS및 ΦC)와 노내 가스점도(μ)및 가스밀도(ρg)을 추정하는 단계;A method for estimating the distribution of gas flow in a blast furnace, the method comprising: dividing an equal area into three parts in a furnace direction in a block zone, and isolating the central area, the middle part, and the peripheral part; According to the following formulas (1) to (10), the average particle diameters (D PS and D PC ), particle size segregation index (I SPS and I SPC ), porosity (ε S and ε C ), and shape coefficient (Φ S) And estimating Φ C ), in-vehicle viscosity (μ) and gas density (ρ g ); (여기서, x : 노경 방향거리Where x is the street length θ : 장입선회슈트의 기울기θ: Slope of the charging swiveling suit p : 가스의 압력p: pressure of gas M : 가스의 평균분자량M: average molecular weight of gas R : 기체상수R: Gas constant T : 가스온도)T: gas temperature) 상기에서 추정된 값을 하기식(11)의 압력손실식(△P/L)에 대입하여 상기와 같이 구획된 각 부분(i)에서의 가스질량 유속(GS)를 구하는 단계 ;Substituting the estimated value above into the pressure loss equation (ΔP / L) of the following formula (11) to obtain the gas mass flow rate G S in each of the sections (i) partitioned as above; Wc: 코크스의 장입량W c : Charge of coke Ws: 소결광의 장입량W s : Loading amount of sintered ore 상기에서 구한 각 구획부(i)에서의 가스질량 유속(G1)을, 하기식(12)∼(14)에서와 같이, 표준상태의 부피 유량(V1)으로 환산한 후 노경방향의 가스유량 분율(X1)을 구하는 단계;After converting the gas mass flow rate G 1 in each partition section i obtained as described above into the volumetric flow rate V 1 in the standard state, as shown in the following equations (12) to (14), the gas in the street-direction direction Obtaining a flow rate fraction X 1 ; 상기와 같은 구해진 가스유량분율(X1)에 의해 고로 노내 가스류 분포를 추정하는 단계를 포함하여 구성됨을 특징으로 하는 고로 노내 가스류 분포 추정방법.And estimating the gas flow distribution in the blast furnace according to the obtained gas flow rate (X 1 ).
KR1019930023737A 1993-11-09 1993-11-09 Control method of blast f'ce gas distribution KR950012396B1 (en)

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Publication number Priority date Publication date Assignee Title
KR101368555B1 (en) * 2012-06-28 2014-02-28 현대제철 주식회사 Judgment method of condition of blast furnace

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101368555B1 (en) * 2012-06-28 2014-02-28 현대제철 주식회사 Judgment method of condition of blast furnace

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