JPH06212164A - Method for blending coking coal - Google Patents

Abstract

PURPOSE:To rapidly determine such blending ratios, brands, etc., of coking coal as to give a coal blend with an expansion pressure in a tolerable range by calculating the pressure of the blend on the basis of the previously obtd. max. expansion pressures of several brands of coking coal. CONSTITUTION:Several brands of coking coal are blended to give a coal blend, which is fed into a coke oven. Before blending, the max. expansion pressure of each brand is obtd. On the basis of the max. expansion pressures above obtd. is calculated an arithmetic mean of expansion pressures of coking coals blended by equation I (wherein P0 is an arithmetic mean kPa of expansion pressures of coking coals blended; Xi is the max. expansion pressure kPa of each coking coal blended; Yi is a blending ratio (%) of each coking coal blended; and n is the number of brands of coking coal). Then, the expansion pressure of the blend is calculated by equation II (wherein P is the calculated expansion pressure kPa of the blend; and a and b are each a coefficient). The brands and/or blending ratios of coking coals are adjusted so that the calculated expansion pressure is in a tolerable range predetermined for the oven.

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for blending coking coal.

[0002]

2. Description of the Related Art A coal blend formed by blending a large number of brands of coal is charged into a carbonization chamber of a coke oven, and coke is produced from this coal. The pressure acting on the furnace wall is generally called the expansion pressure in the coal carbonization process. If the expansion pressure is high, the coke oven wall may be damaged and the operation may become impossible. In particular, in recent years, the number of coke ovens that have deteriorated has increased, the strength of the furnace body has declined, and coal in the carbonization chamber has been introduced by the introduction of coal pretreatment techniques such as the humidity control coal method, which has become popular recently. Since the bulk density of the charge rises and the expansion pressure tends to increase, the expansion pressure control is an important issue in furnace body management.

It is conventionally known that many coals having a high degree of coalification, which are represented by volatile matter, carbon content, average reflectance, etc., have a high expansion pressure. Therefore, until now, it has been attempted to control the expansion pressure of the coal blend in the carbonization chamber to an allowable limit pressure of the coke oven furnace body strength or lower by setting an upper limit on the degree of coalification used in the coke oven.

However, some coals having a high degree of coalification have a relatively low expansion pressure, and some coals having a relatively low degree of coalification have a relatively high expansion pressure. There is a case where the expansion pressure is not determined only by itself, and when the expansion pressure is controlled only by the degree of coalification, the expansion pressure becomes higher than the limit pressure and the expansion pressure may damage the coke oven.

[0005] In addition, although there have been cases where attempts were made to control the expansion pressure by parameters other than the degree of coalification, such as the total expansion coefficient and maximum fluidity, the expansion pressure can be adjusted by these caking parameters. There wasn't.

[0006] Thus, the expansion pressure of the blended coal is
Since it is not possible to predict from the coal properties such as the total expansion coefficient and the maximum fluidity, in order to avoid damage to the coke oven, the coal blend is actually carbonized in the test furnace each time it is used in the coke oven. There is a method to measure the expansion pressure of.

Further, as disclosed in Japanese Patent Laid-Open No. 4-132791, there is a method of preparing an expansion pressure estimation model for each coal blend and estimating the expansion pressure of the coal blend from this model.

[0008]

The expansion pressure of the coal blend is measured each time the coal blend composition of each brand forming the coal blend that is the raw material coal for the coke oven is changed or the operating conditions of the coke oven are changed. The above expansion pressure measurement method cannot provide a quick response. In addition, in order to respond promptly, having an expansion pressure map for each blended coal in advance requires a great deal of labor and time because there are a large number of types of blended coal.

In the expansion pressure estimation by the expansion pressure estimation model formula as disclosed in the above-mentioned Japanese Patent Laid-Open No. 4-132791, the ventilation resistance coefficient in the softening / melting layer used in the model formula is experimentally determined for each blended coal. Since it is necessary to obtain it, it is necessary to experimentally obtain the ventilation resistance coefficient for each blended coal in advance, which requires a lot of labor and time as in the above.

The present invention provides a method of blending each brand coal so that the expansion pressure of the blended coal becomes equal to or lower than an allowable limit pressure quickly and without much labor.

[0011]

The present invention has been made in order to solve the above-mentioned problems. This means forms a coal blend by blending a plurality of brands of coking coal and charges it into a coke oven. In this method, the maximum expansion pressure X _i of the raw coal of each brand is obtained in advance, and the phase of the blended coal is calculated according to equation (1) based on each maximum expansion pressure value X _i. The arithmetic mean expansion pressure P ₀ is calculated, and the calculated arithmetic mean expansion pressure P ₀ is used as a lower formula to calculate the compounded coal expansion pressure P by the formula (2).
Is calculated, and the blending brand and / or blending ratio of the raw coal is adjusted so that the calculated blended coal expansion pressure P is equal to or lower than a predetermined allowable limit pressure of the coke oven.

[0012]

[Equation 1]

[0013]

[Number 2] _{P = a × P 0 + b} ......... (2)

However, P ₀ : arithmetic average expansion pressure (kPa) of blended coal P: estimated expansion pressure (kPa) of blended coal X _i : maximum expansion pressure (kPa) of various brands of coal to be blended Y _i : brand raw material Blending ratio (%) by charcoal a, b: Coefficient (-) n: Number of blending brands.

[0015]

The function of the present invention will be described below.

As mentioned above, the present inventors have a large number of types of coal blends, and therefore have a relatively small number of types (in one steel mill, at most about 30 types are used as coke oven coal). ) The maximum expansion pressure of each brand coal is measured, and as a result of diligent research to predict the expansion pressure in the carbonization chamber of the blended coal based on each measured maximum expansion pressure, a plurality of brands as shown in Fig. 1 are obtained. It was found that the expansion pressure of the blended coal formed by blending the above coal has a strong correlation with the arithmetic mean expansion value of each brand coal constituting the blended coal.

That is, in FIG. 1, the maximum expansion pressure of each brand coal used for blending is measured, and the arithmetic mean expansion pressure calculated from the maximum expansion pressure of each brand coal is plotted on the horizontal axis. The measured values of the expansion pressure of the blended coal blended are plotted on the vertical axis.

As can be seen from FIG. 1, the two show a strong correlation, and if this relation (correlation formula) is obtained, the expansion of the blended coal in the carbonization chamber is calculated from the arithmetic mean expansion pressure of each brand coal. The pressure can be easily estimated.

When it is difficult to measure the maximum expansion pressure of all the brand coals charged into the coke oven, attention is paid to high expansion pressure coals. That is, the maximum expansion pressure of each type of coal considered to be a high expansion pressure coal is measured, and the expansion pressures of several types of combination coal with different mixing ratios containing one or more types of high expansion pressure coal are measured to obtain a high expansion pressure. Fig. 2 shows the relationship between the arithmetic mean value of the expansion pressures of coals of each brand calculated assuming that the expansion pressure of coals other than charcoal, that is, low expansion pressure coals, is 0, and the measured value of the blended coal expansion pressures. It was also found that there is a strong correlation between the two as in the above.

The present invention is based on the above findings. The expansion pressure in the carbonization chamber of the coal blend is estimated from the arithmetic mean expansion pressure of each brand coal by the above correlation equation, and this estimated coal expansion pressure is By changing the combination of coal brands and their blending ratio so that the coke oven pressure is below the allowable limit pressure, and operating the coke oven, damage to the furnace body can be prevented and stable coke oven operation can be continued. is there.

[0021]

EXAMPLES Examples 1 to 3 of the present invention will be described below together with comparative examples with reference to Tables 1 and 2 and FIGS.

In Examples 1 to 3, each brand coal A was used.
~ O and the expansion pressure of the blended coal are described in JP-A-4-272.
It is estimated by the method proposed in Japanese Patent No. 992.

That is, as a device for measuring the pressure of the gas generated by the coal, the coal to be measured is charged in a metal box which can be sealed, and a coal charging device equipped with a probe for measuring the internal pressure. A container and this coal charging container are accommodated, and the temperature is 800 ° C to 110 ° C from the side of the coal charging container.
A test furnace composed of a heating furnace capable of heating to 0 ° C. is used.

Then, the gas pressure peak value of the coal is measured by the probe, and the expansion pressure P _{Q of the} coal is estimated by the correlation between the expansion pressure and the gas pressure which is previously obtained from the measured gas pressure peak value. The maximum expansion pressure P _i of each brand coal thus obtained is shown in Table 1, and the expansion pressure P _{y of the} coal blend is shown in Table 2.
Shown in.

[0025]

[Table 1]

[0026]

[Table 2]

The arithmetic mean expansion pressure P ₀ of the blended coal was calculated by the formula 3 (A) based on the maximum expansion pressure P _i of each brand coal and the blending ratio Y _i of the brand coal.

[0028]

[Equation 3]

Further, the expansion pressure P _x of the blended coal in Table 2 was calculated from the arithmetic average expansion pressure P ₀ by using FIG. 1 or FIG. 2, that is, the equation (B).

[0030]

Equation 4] _{P x = a × P 0 +} b ......... (B)

Further, the coal blend 27 thus blended
Ton is charged into a carbonization chamber with an allowable limit pressure of 10 [KPa],
After carbonization at a furnace temperature of 1120 ° C. for 18 hours, extrusion was performed by an extrusion ram of the extruder, and the extrusion load peak current of the extrusion ram of the extruder at that time was measured. The peak load current of the extrusion ram of this extruder is 250 when the stable operation is performed without adversely affecting the furnace wall of the carbonization chamber.
(A).

Example 1 Example 1 is an example of blended coal in which A to L coals were used so that the expansion pressure P _x of the blended coal was below the allowable limit pressure (10 [KPa]) of the coke oven.

The arithmetic mean expansion pressure P ₀ of the blended coal at this time is 12.0 [KPa] when calculated by the above formula (A) using the maximum expansion pressures P _i of the A to L coals. Based on Fig. 1, that is, the expansion pressure P _{x of the} coal blend calculated by the above formula (B) is the allowable limit pressure (10 [KP
a]) The following 3.2 [KPa] was substantially the same as the expansion pressure P _y (= 2.6 [KPa]) estimated in advance using the test furnace.

The extruded load peak current when extruded by an extruder after carbonizing the blended coal in a coke oven is 25
It was 0 (A), which was the same as when stable operation was performed.

Example 2 Example 2 is an example in which a blended coal blended with the same brand of coal as in Example 1 was used, and the arithmetic mean expansion pressure P ₀ of this blended coal is each expansion of coals A to E. Only pressure P _i (expansion pressure P of F charcoal to L charcoal
Calculating with equation (A) using _i (assuming 0) is 9.5.
It becomes [KPa].

Further, in FIG. 2, that is, the expansion pressure P _x of the blended coal calculated by the formula (B) is 2.0 [KPa].

As a result, the expansion pressure P _x and the expansion pressure P _y (= 2.6 [K
It is understood that it is sufficient to adjust the composition of only the brand coal having a relatively large maximum expansion pressure P _i .

Example 3 In Example 3, coals A to E and coals K to O were blended so that the expansion pressure P _x of the blended coal was not more than the allowable limit pressure (10 [KPa]) of the coke oven. This is an example of using blended coal.

The arithmetic mean expansion pressure P ₀ of the blended coal at this time is calculated by the formula (A) using the maximum expansion pressures P _i of the A coal to E coal and the K coal to O coal. KPa], and further, the expansion pressure P _{x of the} coal blend calculated in FIG. 1, that is, the formula (B), is the allowable limit pressure (10 [KPa]) of the coke oven.
The value was 4.4 [KPa] below, which was substantially equivalent to the expansion pressure P _y (= 5.2 [KPa]) estimated using the test furnace.

The extruded load has a peak current of 25 when extruded by an extruder after carbonizing the blended coal in a coke oven.
In the case of 5 (A), it was almost the same as in the case of stable operation.

[0041] Comparative Example Comparative Example is an example of using a coal blend obtained by blending the A coal ~L coal, the maximum inflation pressure P _i of the arithmetic mean inflation pressure P ₀ of the coal blend is the A charcoal ~L Charcoal It is 22.0 [KPa] when calculated by the above formula (A) using, and the expansion pressure P _x calculated from FIG. 1, that is, the above formula (B) using this arithmetic mean expansion pressure P ₀ is It was 17.8 [KPa], which was equal to or higher than the allowable limit pressure (10 [KPa]) of the coke oven.

The expansion pressure P _y of the blended coal estimated using the test furnace is 15.8 [KPa], and the difference between the expansion pressure P _y and the expansion pressure P _x is +2.0 [KPa]. It was a big one.

The extruding load peak current when the compounded coal was dry-distilled in a coke oven and then extruded by an extruder was 285 (A).
Therefore, it is estimated that a large load is applied to the furnace wall of the carbonization chamber as compared with the case where stable operation is performed.

From the above Examples 1 to 3 and Comparative Example, it is understood that the expansion pressure P _x of the blended coal can be easily estimated from the arithmetic average expansion pressure P ₀ of each brand coal.

[0045]

As described above, according to the present invention, it is possible to easily predict the expansion pressure of the coal blend that occurs in the coal carbonization process, estimate the expansion pressure of the coal blend from the correlation equation, and If the coal blending ratio is controlled so that the value becomes less than the allowable limit value and the operation is performed, stable coke oven operation can be continued while avoiding damage to the furnace body due to expansion pressure.

[Brief description of drawings]

FIG. 1 is a diagram showing a relationship between an arithmetic mean value of plain coal expansion pressure and a measured value of blended coal expansion pressure.

FIG. 2 is a diagram showing the relationship between the arithmetic mean value of plain coal expansion pressures calculated assuming that the expansion pressures of coals other than high expansion pressure coals are 0 and the measured values of blended coal expansion pressures.

 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Seiji Nomura 20-1 Shintomi, Futtsu City, Chiba Shin Nippon Steel Co., Ltd. Technology Development Division

Claims (1)

[Claims] 1. By blending a plurality of brands of coking coal
In the method of forming the coal blend and charging it into the coke oven,
The maximum expansion pressure of raw coal of each of the above brands was obtained in advance.
Based on these maximum expansion pressure values, Equation 1
Calculate the arithmetic mean expansion pressure of the blended coal according to (1)
Formula 2 based on the arithmetic mean expansion pressure calculated by formula (2)
The coal expansion pressure was calculated, and the calculated blended coal expansion pressure was set in advance.
In order to keep the coke oven pressure below the allowable limit,
Characterized by adjusting the blending brand and / or blending ratio
Method of blending coking coal. [Equation 1] ## EQU00002 ## P = a.times.P₀+ B ……… (2) However, P₀: Arithmetic mean expansion pressure (kPa) of blended coal P: estimated expansion pressure (kPa) of blended coal X_i: Maximum expansion pressure (kPa) Y of various brands of coal blended_i: Blend ratio (%) for each brand of raw material coal a, b: Coefficient (-) n: Number of blend brands.