JP5833474B2 - Coke production raw material production method and coke production raw material produced by the production method - Google Patents

Description

  TECHNICAL FIELD The present invention relates to a method for producing a coke production raw material and a coke production raw material produced by the production method, and in particular, a method for producing a coke production raw material mainly composed of a blended coal in which low-grade coal is blended with raw coal. And a coke production raw material produced by the production method.

  Coal used as a raw material for metallurgical coke (hereinafter referred to as raw coal) is softened and melted when heated and then re-solidified to form strong coke, which is classified as bituminous coal and is generally referred to as caking coal. However, bituminous coal that can be used as a raw material for coke production has a problem of limited resources and high cost. Accordingly, there is a demand for an increase in the distribution of low-grade weakly caking coal or non-slightly caking coal or even lower grade coal. When low-grade coal is used as a raw material for coke production, since many coals having different properties exist, it is necessary to use coal having caking properties and a degree of coalification in an appropriate range. Therefore, attempts have been made to design a blended coal in which a plurality of types of coal having different properties are combined and blended.

  The cohesiveness of such coal is determined by properties such as fluidity, expansibility, and tackiness, but fluidity greatly affects the coke strength. For this reason, grasping the maximum fluidity of blended coal (hereinafter sometimes referred to as “MF (Maximum Fluidity)”) is an important factor for producing high-strength coke. Conventionally, the MF of blended coal has been estimated by the weighted average value of each MF of blended simple coal. However, the flow start temperature (ST), maximum flow temperature (MFT) and solidification temperature (FT) of each of the blended plain coals are different. Therefore, the weighted average value of each coal simple MF and the MF of blended coal do not match. The estimated value of the common logarithm (hereinafter sometimes referred to as “logMF”) of the maximum fluidity of the blended coal, which has been conventionally performed, is lower than the actually measured value. Such a tendency becomes more prominent as more MF coal is used, which has been a major cause of reducing the estimation accuracy of coke strength (for example, Patent Document 1 [Prior Art] and [Invention will be solved]. [See the problem to be considered]]).

  Moreover, about the preparation method of the coal blend which mixes and mixes several types of coal from which a property differs, a caking additive is used in combination with the non-slightly caking coal which has the property which can fully utilize the characteristic. Thus, even when using a blended coal in which the blending ratio of non-slightly caking coal is equal to or higher than before, a method that can produce coke that satisfies the recently required strength has been studied ( For example, see Patent Document 2). Specifically, in the preparation of the coke oven raw material, a step of further blending a low-volatile non-slightly caking coal having a volatile content of 25% or less and a maximum fluidity of 1 ddpm or more and 10 ddpm or less into the blended coal, and a binder A step of adding, wherein a mass ratio of the low volatility non-minor caking coal to the caking material (non-minor caking coal / caking material) is 1 or more and 3 or less, and / or the low volatility non-minor viscosity There has been proposed a coke production method characterized in that the mass ratio of coal to coal blend is 2 to 9% (see, for example, Patent Document 2 [Claims 1 to 3]).

Japanese Patent Laid-Open No. 02-20592 JP 2009-249596 A

However, in the above case, the following problems occur.
(I) In the method of Patent Document 1, when low-grade coal having no fluidity is blended with coking coal mainly composed of caking coal, logMF of low-grade coal to be blended cannot be detected, so MF or logMF of blended coal Is not different from MF or log MF of coking coal, and cannot be applied as a method of estimating MF or log MF of blended coal in which low-grade coal is blended with coking coal, and a blended coal having a desired MF or log MF It was difficult to produce.
(Ii) On the other hand, the estimated value of the weight average of each MF or log MF of each coal as in the past may cause a large deviation from the estimated value of MF or log MF of the actual blended coal. Therefore, it was difficult to produce a blended coal having desired MF or log MF.
(Iii) In particular, even when blending with low grade coal at the same ratio using the same raw coal, depending on the brand of low grade coal, the weight average of each MF or log MF of each coal The deviation from the estimated value may increase.
(Iv) When the low-grade coal and the high-fluidity binder are blended into the raw coal by the method of Patent Document 2, predetermined characteristics are obtained with respect to the low-grade coal to be blended. However, the ratio of raw coal / low-grade coal and low-grade coal / caking additive was limited, and the demand for increasing the amount of low-grade coal could not be fully met. Moreover, since the fluidity is different when the coal type of the raw coal is different, the blending ratio of the low-grade coal according to this is limited, and it is difficult to expand the application range. Furthermore, the fluidity of the blended coal in which the low-grade coal is blended with the raw coal is not only measured individually, but does not solve the above problems (i) to (iii).
(V) In addition, one of the technical effects expected by blending the binder is a function to compensate for a decrease in fluidity caused by blending low-grade coal with raw coal. However, when the caking agent is blended with the blended coal in which the raw coal and the low-grade coal are blended uniformly, such a filling function may vary. In particular, when the increase in low-grade coal is required, such variations cannot be ignored.

  In view of the above-mentioned problems of the prior art, an object of the present invention is to have a blended coal in which an excessive amount of low-grade coal is blended with coking coal as a main component, and to blend a high-fluidity coal or material into a desired one. When preparing raw materials for coke production with fluidity, the optimum blending conditions for the blended coal are efficiently estimated by a simple method, and the blending amount of highly fluid coal or binder is set. A method for producing a coke production raw material capable of producing a coke production raw material capable of stably ensuring excellent caking or fluidity, and a coke production raw material produced by the production method are provided. There is to do.

  As a result of intensive studies to solve the above problems, the present inventor has found that the above object can be achieved by a method for producing a coke production raw material shown below and a coke production raw material produced by the production method, The present invention has been completed.

The method for producing a raw material for coke production according to the present invention is a method for producing a raw material for coke production by blending low-grade coal with raw coal.
In order to compensate for the difference between the characteristics of the primary blended coal in which the low-grade coal is blended with the raw coal and the characteristics of the desired coke production raw material, Mixing in the vicinity of the low-grade coal to produce a precursor blended coal, blending the precursor blended coal with the raw coal and creating a secondary blended coal,
The blending ratio of the raw coal, the low grade coal, the high fluidity coal or the high fluidity material, and the precursor blended coal is set based on the maximum fluidity that is an index of each characteristic.

  When producing raw materials for coke production with desired characteristics by blending coal (primary blended coal) in which an excessive amount of low-grade coal is blended with raw coal into a main component and blending high-fluidity coal or materials. In coke production raw materials, since appropriate flowability or caking property based on fluidity is required, raw coal, low-grade coal, primary blended coal blended with these, blended with these High fluidity coal or high fluidity material (hereinafter sometimes referred to as “high fluidity material”), and the maximum fluidity (MF) of the precursor coal blended with high fluidity material blended with low grade coal It becomes important. One feature of the present invention is that the blending ratio of such raw coal is set using MF as an index. In addition, in the verification process, the function of compensating for the decrease in fluidity accompanying the blending of low-grade coal with the raw coal of the high-fluidity material is blended with the high-fluidity material close to the low-grade coal (hereinafter referred to as “ In other words, it was sometimes referred to as “proximity blending”, thereby obtaining a technical effect that a secondary blended coal with higher coke strength can be produced. In order to effectively utilize such a compensation function, the present invention produces a secondary coal blend by uniformly blending a high-flow coal with a primary coal blended with low-grade coal uniformly in the raw coal. Rather than doing (referred to as “simple blending”), a high-fluidity material is preliminarily blended with low-grade coal in advance to produce a precursor blended coal, and the precursor blended coal is blended with the raw coal to provide a secondary blend. By producing charcoal, it becomes possible to accurately compensate for the difference from the desired MF generated by blending an excessive amount of low-grade coal, and stably securing excellent caking or fluidity It has become possible to provide a method for producing a raw material for coke production.

  Here, “low-grade coal” refers to coal or carbide that has not been softened and melted, such as anthracite, and sub-bituminous coal, lignite, or peat, etc. Coal has a relatively coarse structure with a large amount of moisture, oxygen and volatile components and a small amount of carbon. It has little fluidity and caking properties and does not coke itself. Further, “high-flow coal or high-fluidity material” refers to coal having higher fluidity than raw coal or a material that can be blended with coal (hereinafter also referred to as “high-fluidity material”). Specifically, caking coal with a high fluidity or coal extract obtained by modifying soluble components extracted from coal with a solvent (inorganics are removed and organics are the main components. And a caking agent such as coal-based pitch or petroleum-based pitch. Note that the actual fluidity index is generally compared not as MF but as its common logarithm log MF. “Proximity blending” refers to blending a specific material (high fluidity material) close to one of a plurality of blending materials (coking coal and low-grade coal) or a specific blending material (low-grade coal). It means to avoid proximity to other compounding materials (coking coal), and a specific processing method will be described later.

The present invention is a method for producing the above-mentioned raw material for producing coke, and in the production of the precursor blended coal, by any one of pressure bonding, molding, granulation, adhesion or kneading, or some combination of these treatments. The low-grade coal is mixed with the high-flow coal or the high-fluidity material.
As described above, it was found that the high-fluidity material supplementing function is effective not by simply blending the high-fluidity material with the low-grade coal but by the close blending with the low-grade coal. It is possible to prevent the blending effect of the high fluidity material from being reduced by bringing the blended high fluidity material close to the raw coal having the same high fluidity. Specifically, it is necessary to apply a process for fixing a high-fluidity material on the surface of low-grade coal with low fluidity, and as a process of proximity blending, a crimping process, a molding process, a granulation process, an adhesion process or A kneading process is mentioned. Such treatment makes it possible to accurately compensate for the difference from the desired MF caused by the blending of an excessive amount of low-grade coal. Details of each process will be described later.

The present invention is a method for producing the above-mentioned raw material for coke production, wherein one or two or more types of the raw coal are selected in advance as the reference coal, the range of the appropriate fluidity of the reference coal, and the reference coal A flowability characteristic curve with respect to temperature, and a maximum fluidity of the reference coal based on the flowability characteristic curve are obtained. Further, for one or two or more low-grade coals to be blended, the standard for the blending ratio of the low-grade coals Find the flow rate decline gradient for the low-grade coal based on the change in the maximum fluidity of the coal,
Based on the maximum fluidity of the raw coal actually used and the flow rate decrease gradient of the low-grade coal actually blended, the blending ratio of the low-grade coal blended with the raw coal Estimating the maximum fluidity of the primary coal blended with the low-grade coal in the coal,
Find the maximum fluidity of high-flow coal or high-fluidity material having a higher fluidity than the raw coal in advance,
In order to compensate for the difference between the maximum fluidity of the primary blended coal and the maximum fluidity of the desired coke production raw material, the blending ratio z of the high fluidity coal or the high fluidity material is based on the following formula 1. It is characterized by setting.
z = f (Y2, Y1, Yo, T, α) Equation 1
Where Y2: Maximum fluidity of desired secondary coal blend Y1: Maximum fluidity of primary coal blend Yo: Maximum fluidity of low grade coal T: Maximum fluidity of high fluidity coal or high fluidity material α : Primary blended coal composed of raw coal and low-grade coal as main components when low-grade coal is mixed with an excess amount of low-grade coal into low-grade coal MF is important. At this time, it is difficult to ensure a blended coal having a desired MF efficiently by the method of measuring the fluidity of the primary blended coal for each blending treatment as before. As a result of verifying the method of estimating the MF of the primary coal blend in which the low-grade coal is blended with the raw coal, the present invention estimates the MF of the primary coal blend from the knowledge that the following characteristics exist. Found that can be done.
(A) The fluidity decrease gradient accompanying the blending of low-grade coal does not depend on the coal type or characteristics of the raw coal (reference coal).
(B) The flow rate decrease gradient in which the low-grade coal is blended is unique to the brand of the low-grade coal and does not need to be obtained every time the blending is performed.
Specifically, one or two or more low-grade coals to be used are blended with reference coal (MF is obtained in advance), and a fluidity decrease gradient related to each low-grade coal is obtained in advance. It became possible to estimate the MF of the primary blended coal efficiently by a simple method from the blending ratio of the low-grade coal blended with the MF of the raw coal actually used and the flow rate decrease gradient. At this time, the blending rate z of the high fluidity material is determined based on the function using the secondary blended coal, the primary blended coal, the low grade coal, the MF of the high fluidity material or the flow rate decrease gradient of the low grade coal as an index. By setting as in the above formula 1, it becomes possible to accurately compensate for the difference from the MF of the desired raw material for coke production caused by the blending of an excessive amount of low-grade coal, and the fluidity in the appropriate range It has become possible to produce a coke production raw material having excellent caking or fluidity. A specific function in the above formula 1 will be described later for setting the blending ratio z.

The present invention is a method for producing the above-mentioned raw material for producing coke, wherein the fluidity reduction gradient according to the low-grade coal to be used is obtained by determining the fluctuation of the fluidity-decrease gradient with respect to the oxygen content of the low-grade coal to be blended. Is corrected by the oxygen content of the low-grade coal.
As a result of the above verification, the MF of the primary coal blend is dependent on the brand of the low-grade coal to be blended, and the fluidity tends to decrease as the oxygen content of the blended low-grade coal increases. We obtained the knowledge that Since these tendencies affect the flow rate gradient of low-grade coal, they can be corrected based on the oxygen content of the low-grade coal blended (shown in the characteristic chart of coal sold in general). It became possible to estimate the MF of the primary blended coal more accurately.

The present invention is a method for producing the above-mentioned raw material for producing coke, wherein the flow rate decrease gradient related to the low-grade coal to be used is determined by determining the fluctuation of the flow rate decrease gradient with respect to the volatile content of the low-grade coal to be blended. The correction is made according to the volatile content of the low-grade coal.
According to the results of the above verification, the MF of the primary coal blend shows that the fluidity tends to decrease as the volatile content of the low-grade coal increases in addition to the oxygen content of the blended low-grade coal. Obtained. These tendencies affect the flow rate gradient of low-grade coal as well as the oxygen content, and are therefore corrected based on the volatile content of the low-grade coal blended (also clearly indicated in the coal characteristics table). This makes it possible to estimate the MF of the primary coal blend more accurately.

Further, the present invention is a coke production raw material prepared by the above-described method for producing a coke production raw material, wherein low grade coal is blended with raw coal, the blending ratio of the low grade coal being 0.1 to 20%, It has a common logarithmic value 2-3 of the maximum fluidity of the secondary coal blend.
The secondary coal blend produced by the above production method has excellent caking properties or fluidity. Such characteristics are sufficient to ensure suitability as a coke production raw material, and it is useful to use the secondary blended coal thus produced as a coke production raw material.

Explanatory drawing showing the manufacturing process of metallurgical coke Schematic illustrating the flow characteristic curve with temperature of coking coal Schematic illustrating the production process of a raw material for coke production according to the present invention Explanatory drawing illustrating the outline of the production process of the raw material for coke production according to the present invention Schematic illustrating the variation in fluidity of blended coal corresponding to the blending ratio of low-grade coal Schematic illustrating the fluctuation of the flow rate decrease gradient of the blended coal corresponding to the coal type and fluidity of the raw coal Schematic illustrating the variation in flow rate decline gradient of blended coal corresponding to the oxygen content of low grade coal Schematic illustrating the variation in flow rate decline gradient of blended coal corresponding to the oxygen content of low grade coal Schematic illustrating the fluctuation of the flow rate decrease gradient of coal blends corresponding to the volatile content of low grade coal

The method for producing a coke production raw material according to the present invention (hereinafter referred to as “the present production method”) is a method for producing a coke production raw material by blending a low-grade coal with a raw coal.
High fluidity coal or high fluidity material (high fluidity) blended to compensate for the difference between the characteristics of the primary blended coal in which the low-grade coal is blended with the raw coal and the characteristics of the desired coke production raw material Premixed in advance in the vicinity of the low-grade coal to produce a precursor blended coal, blending the precursor blended coal with the raw coal to produce a secondary blended coal,
The blending ratio of the raw coal, the low-grade coal, the high fluidity material, and the precursor blended coal is set based on the maximum fluidity that is an index of each characteristic.

In other words, this production method is based on the blending conditions of raw coal, low-grade coal, and high fluidity material in the production process, using the MF of each material, primary blended coal, secondary blended coal and precursor blended coal as an index. The raw material for coke production with excellent caking or fluidity (secondary blending) is prepared by setting the characteristics without actually measuring, and preparing the precursor blended coal by preliminarily blending the low-grade coal with the high fluidity material. Charcoal). Coking coal, low-grade coal, and high-fluidity material are not simply blended, but secondary blending with higher coke strength is made by pre-blending high-fluidity material in close proximity to low-grade coal in advance. Charcoal can be made. This has validity from the following viewpoints in addition to the findings from various verifications described later.
(I) As mentioned above, MF of blended coal when blending high-grade coal with high-grade coking coal is close to the weighted average of both, and coke strength is high, but high-grade coking coal and low-grade coal When coal is blended, the MF of the blended coal is lower than the weighted average of both, and the coke strength is also lowered.
(Ii) Preliminary blended coal obtained by blending a high-fluidity material close to the low-grade coal in this production method apparently forms high-grade coal.
(Iii) Therefore, MF of blended coal (primary blended coal) when blending low-grade coal with high-grade coking coal is excessively lowered and coke strength is reduced, while The MF of the blended coal (secondary blended coal) in the case of blending a high-quality precursor blended coal does not cause an excessive decrease, and a high coke strength can be expected.
Hereinafter, embodiments of the present invention will be described with reference to the drawings.

<Coke production process>
The manufacturing process of metallurgical coke will be briefly described with reference to FIG. Coal is landed from the coal carrier 1 berthed at the quay and stored in the coal storage 2 for each property (brand) of the coal. Coal (including coking coal and low-grade coal) stored in the coal storage 2 is dispensed by a reclaimer for each brand and sent to the blending tank 3 by a belt conveyor. The blending tank 3 has a plurality of tanks, and one brand of coal is stored in one blending tank. Coal has high and low costs due to its properties, and in order to produce high quality coke at a low cost, coal with different properties is cut out from a plurality of blending tanks at an optimum blending ratio, and is introduced into the processing tank 8. By blending an appropriate amount of the high fluidity material 7 in close proximity to the low-grade coal and further blending with the raw coal, blending as a raw material for coke production (secondary blended coal) is completed. At this time, it is preferable not to pulverize the precursor blended charcoal blended in close proximity. There is a possibility that the effect of proximity blending such as the function of compensating for the decrease in fluidity may be reduced by fragmenting and dispersing the precursor blended coal. For coke production, various kinds (brands) of coal are imported from overseas and stored in the coal storage 2 for each brand. This is because coal mined in each coal mine has different properties depending on the coal mine, and the properties of coke produced differ depending on the properties, so by combining multiple coals and appropriate amount of high fluidity material, This is because it is necessary to satisfy the coke properties (quality) required by the user at a low cost.

  The pulverization equipment 4 is provided with a known pulverizer, and pulverizes the blended coal (secondary blended coal). The coal pulverized in the pulverization facility 4 is transferred to the coke oven 6 by a belt conveyor or the like. The transferred coal is temporarily stored in a coal bin (coal tower) 6a, and then charged into the coke oven 6 by a charging vehicle 6b and dry-distilled (steamed). The dry-distilled coal becomes coke and is pushed out of the coke oven by the extruder 6c. The obtained product coke is finally fed into the blast furnace.

[Characteristics of coal]
The quality of coal is usually evaluated by caking or fluidity as physical properties and by four industrial analysis values (water, ash, volatile, fixed carbon) as chemical properties. In this production method, among these characteristics, the suitability as a raw material for producing coke was evaluated based on the fluidity. The strength of the coal (coke strength) was evaluated by drum strength (DI ₁₅ ) and hot strength (RSI).

(I) Measuring method of fluidity The fluidity of coal and a high fluidity material is measured by the Gieseler plastometer measuring method standardized by JIS-M8801. Specifically, as illustrated in FIG. 2 (A), by using the temperature as an index, the fluctuation of the fluidity in the softened and melted state of the coal to be evaluated is traced, and the fluidity characteristic curve (Giesler fluidity) Curve) and the fluidity of the coal is evaluated with the maximum fluidity (MF) which is the maximum value. Note that, in actual evaluation, it is generally compared not as an MF value but as a common logarithm log MF. In the Gisela plastometer measurement method, coal or high fluidity material to be measured is loaded into a crucible equipped with a stirring rod, and in a metal bath (solder bath), for example, a rate of temperature increase of 3.0 ± 0.1. The temperature is raised at a rate of ° C / min. Conceptually, the softening of coal or high-fluidity material begins as the temperature rises, and the stirrer begins to rotate along with this (appearance of fluidity). Then, after the coal or high fluidity material exhibits the maximum rotation speed at a specific temperature (corresponding to MF), the resolidification of the coal or high fluidity material starts, and the rotation speed gradually decreases and stirring is performed at a predetermined temperature. The rod rotation stops completely. Such fluidity characteristic curves differ depending on the type of coal or high fluidity material.

(Ii) Characteristics of blended coal FIG. 2 (B) shows flow curves of raw coal, low-grade coal, and blended coal (primary blended coal) when blending low-grade coal with raw coal. The state where the maximum fluidity MFo of the raw coal is changed (decreased) to the maximum fluidity MFm of the primary coal blend produced by blending the low-grade coal (MF = 0) is shown. At this time, when comparing the log MFm value obtained by converting this MFm into a common logarithm, and the log MFm value estimated by weighted averaging of log MFo of raw coal and log MF (= 0) of low-grade coal, both It has been found that there may be large deviations in At the same time, it was found from several findings as described later that the MFm of the primary coal blend can be accurately estimated. One feature of this production method is to use estimation based on such knowledge. Here, “log MF” indicates a common logarithm of the maximum fluidity (MF), and is used in actual evaluation.

(Iii) Measurement of coke strength Raw coal or produced coal is charged into a small test furnace (width 430 mm, width 380 mm, 350 mm) at 730 kg / m ³ , dry-distilled at a furnace temperature of 1070 ° C., and a center temperature of 1030 ° C. After reaching, the steel was cooled in a nitrogen atmosphere, and the resulting coke was evaluated for coke strength by measuring drum strength (DI ₁₅ ) and hot strength (RSI) by the following measurement method.
(Iii-1) Drum strength measurement method About the coke obtained by the above process, a coke lump on a 25 mm sieve is collected from a sample subjected to a shutter test based on the drop strength test method standardized in JIS-K2151 twice. These were used to measure the drum strength index (DI ₁₅ ) according to JIS-K2151.
(Iii-2) Hot strength measurement method Coke obtained by the above treatment is sized to an average particle size of 19 to 21 mm, and 200 g of a coke lump of 21 mm or less from a 19 mm sieve is used from this sample at 1100 ° C. React with time CO ₂ (5 L / min). After the reaction, the reaction residual sample was placed in a cylindrical type I drum tester (manufactured by Hasegawa Seisakusho) having an inner diameter of 132 mm and a height of 700 mm, and rotated at 20 rpm for 30 minutes. Then, it sieved with the 9.56 mm sieve, the sample weight which remained on the sieve was measured, and the residual sample ratio on the sieve with respect to the reaction residual sample was made into hot strength (RSI).

<Method for producing raw material for coke production according to the present invention>
An outline of a basic manufacturing process of this manufacturing method is illustrated in FIG. Desired fluidity (for example, log MF ranges from 2 to 3) and coke strength (for example, DI ₁₅ is 85.0 or more, RSI is 38.0 or more) for the secondary blended coal used as a raw material for coke production In this case, secondary blended charcoal is produced by the production processes of the following steps (1) to (7).
(1) Selection of coking coal, low grade coal and high fluidity material (2) Estimation of MF of primary coal blend (3) Confirmation of difference between MF of primary coal blend and desired MF (4) High fluidity (5) Preparation of precursor blended coal: blend of low-grade coal and high fluidity material (6) Preparation of secondary blended coal: blend of precursor blended coal and raw coal (7) 2 Confirmation of coke strength of next blended coal: Confirmation within the range of desired coke strength

  When various raw coals and low-grade coals are used, even when an excessive amount of low-grade coals is used, the MF of the primary blended coal can be estimated with high accuracy and high fluidity with a known MF. By supplementing with the material, the MF of the secondary blended coal can be adjusted appropriately. In addition, the low-grade coal and the high-fluidity material are blended in close proximity, and then blended uniformly with the raw coal, so that the low-grade coal and the high-fluidity material are softened and melted close to each other during heating, and then re-solidified to form a precursor. Coke strength of blended coal can be increased. That is, it is possible to form a state where “low-grade coal” having high fluidity with respect to the raw coal is blended. Granular or pulverized coal used as a raw material for coke production functions as individual particles or powders, and each particle or powder has high-grade characteristics. It is estimated that it is possible to ensure the same function as Hereinafter, the details of the steps (1) to (7) will be described. In addition, about estimation of MF of a process (2) primary coal blend, it mentions in full detail in the separate item mentioned later.

(1) Step of selecting coking coal, low grade coal and high fluidity material Coal coal, low grade coal and high fluidity material are selected to produce the desired raw material for coke production (secondary blended coal). The Normally, raw coal and low-grade coal having known or actually measured MF are selected, and the respective blending amounts are set. For example, when the desired MF of the secondary coal blend is logMF = 3 [logddpm], caking coal having a high fluidity of logMF = 2 to 4 [logddpm] is selected as the raw coal, and logMF is selected as the low-grade coal. = 0.1-1 [logddpm] low flow rate lignite is selected, and information on the flow rate of each coal actually blended in advance is verified or measured. Specifically, a fluidity characteristic curve as shown in FIG. 2A is obtained or measured. At the same time, tar pitch is selected as a high-fluidity material excellent in blendability of the selected raw coal and low-grade coal, and information relating to the fluidity is verified or measured. In addition, when the information regarding the fluidity of coking coal and low-grade coal is available in advance and the MF of the primary blended coal at an arbitrary blending ratio can be estimated based on such information, these blending ratios are As an index, raw coal, low-grade coal, and blending ratio constituting the primary blended coal can be selected. At this time, each coal is not limited to one coal type, and coal in which a plurality of coal types are blended can be used.

(2) Step of estimating the MF of the primary blended coal Based on the flow characteristics curve of the raw coal and the low-grade coal obtained in the above (1), the raw coal and the low-grade coal are shown in FIG. Such maximum fluidity (MF) is set. Further, a reference coal having the same or different fluidity as that of the selected raw coal is set, and a fluidity characteristic curve of the reference coal is obtained or measured. Based on the MF of the raw coal, the low-grade coal and the reference coal, the MF of the primary coal blend at a plurality of blend ratios is estimated. Details of the estimation method will be described later.

(3) The step of confirming the difference between the MF of the primary blended coal and the desired MF The difference between the estimated MF of the primary blended coal and the desired (secondary blended) MF is confirmed. In other words, the MF of the primary coal blend estimated in (2) above confirms the difference from the desired MF produced by blending an excessive amount of low-grade coal with the raw coal, and has a high fluidity necessary for compensation. Determine the amount of ingredients.

(4) Step of calculating the blending amount of the high fluidity material The blending amount of the high fluidity material is calculated in order to compensate for the difference between the estimated MF of the primary coal blend and the desired MF. The blending ratio z of the high fluidity material to the primary blended coal is the maximum fluidity of the primary blended coal based on the desired maximum fluidity (MF or log MF) of the secondary blended coal as shown in the following formula 1. (MF or log MF), the highest fluidity of the low-grade coal to be blended (MF or logMF), the highest fluidity of the high-fluidity material (MF or logMF), or the lowering of the fluidity of the low-grade coal, or Some are set as indicators. Specifically, it can be set based on the following expressions 2-1 and 2-2 as exemplified below.
z = f (Y2, Y1, Yo, T) Equation 1
Where Y2: Maximum fluidity of desired secondary coal blend Y1: Maximum fluidity of primary coal blend Yo: Maximum fluidity of low grade coal T: Maximum fluidity of high fluidity coal or high fluidity material α : Low-grade coal fluidity gradient

Specifically, the blending ratio z is expressed, for example, by using MF (log MF) of the desired secondary blended coal, MF (log MF) of the primary blended coal, and MF (log MF) of the high fluidity material as indexes. -1 can be set.
z = (Y2-Y1) / T ... Formula 2-1.
Where Y2: logMF of desired secondary coal blend
Y1: log MF of primary coal blend
T: log MF of high flow charcoal or high flow material
It becomes possible to accurately compensate for the difference from the desired MF generated by blending an excessive amount of low-grade coal by blending an appropriate amount of a high fluidity material, and a secondary blended coal having an appropriate range of fluidity. Can be produced.

In addition, the blending ratio z is expressed by the following equation 2-2 using, for example, the low-grade coal fluidity decrease gradient (ΔlogMF), the low-grade coal MF (logMF), and the high-fluidity material MF (logMF). Can be set based on.
z = α × Yo / T (Formula 2-2)
Here, α: Flow rate decreasing gradient of low-grade coal (ΔlogMF)
Yo: low-grade coal logMF
T: log MF of high flow charcoal or high flow material
It is possible to accurately compensate for the difference from the MF of raw coal generated by blending low-grade coal by blending an appropriate amount of high-fluidity material estimated from the characteristics of low-grade coal, and flow in an appropriate range A secondary blended coal having the same grade and strength as the raw coal having a high degree can be produced. Here, “Δlog MF” indicates a slope of the common logarithm log MF (fluidity lowering slope) of the maximum fluidity (MF), and is used in the actual evaluation.

(5) Step of preparing the precursor blended coal The low grade coal and the high fluidity material selected in the above (1) are blended so that the high fluidity material has the blending ratio z calculated in the above (4). A precursor blended charcoal is produced. Specifically, the blending ratio x: y (x + y + z = 1) of the raw coal and the low grade coal constituting the primary blended coal is blended so that the blending ratio y: z of the low grade coal and the high fluidity material is obtained. To do. A high-flowability material is used for low-grade coal, rather than a simple blending method in which high-flowability coal is uniformly blended with primary-mixture coal in which low-grade coal is uniformly blended with raw coal. After preparing the precursor blended coal by blending close together, the precursor blended coal is blended uniformly with the raw coal to compensate for the decrease in fluidity due to the blending of the low-grade coal into the raw coal and coke. A secondary blended charcoal with higher strength can be produced.

Here, examples of the process of proximity blending include a pressure bonding (molding) process, a granulation process, an adhesion process, and a kneading process. By such treatment, the blended high fluidity material is prevented from approaching the raw coal and reducing the blending effect of the high fluidity material, and the difference from the desired MF generated by blending an excessive amount of low grade coal is eliminated. Can be compensated with high accuracy. The specific contents of each process are as follows.
(I) The pressure bonding (molding) process refers to a process in which a mixture of powder or particulate low-grade coal and a high fluidity material is pressure-bonded under pressure and molded into a predetermined shape. The fluidity can be increased by heating treatment to increase the impregnation rate. For example, an inert gas is used to form a pressurizing condition of a press pressure of 1 to 30 MPa.
(Ii) The granulation treatment refers to granulating a powder or fine particulate low grade coal using a high fluidity material as a binder to produce a granular precursor blended coal. By covering the surface of the precursor blended coal with a high fluidity material, it can have high fluidity characteristics similar to high-grade coal.
(Iii) Adhesion treatment refers to preparing a precursor blended charcoal of a predetermined size using a low-grade coal in the form of powder or fine particles and a high fluidity material as a binder. Similarly to the above (ii), the surface of the precursor blended coal is coated with a high fluidity material, so that it can have high fluidity characteristics similar to high-grade coal.
(Iv) Kneading treatment refers to molding by molding powder or fine particle low-grade coal using a high fluidity material as a binder. Precursor coal with high uniformity can be produced and can have high fluidity characteristics similar to higher grade coal.

(6) Step for producing secondary blended coal The raw coal selected in (1) above is blended with the precursor blended coal to produce a secondary blended coal. In this way, coking coal, low-grade coal, and high fluidity material are not simply blended, but low-grade coal and high-fluidity material are blended in close proximity, and then blended uniformly with coking coal, resulting in low grade during heating. The charcoal and the high fluidity material are softened and melted in close proximity, and then resolidified to increase the coke strength of the precursor blended coal.

(7) Step of confirming the coke strength of the secondary blended coal The coke strength of the prepared secondary blend (extracted) is measured, and within a predetermined range of the desired coke strength (hereinafter sometimes referred to as “allowable range”). Make sure that When the allowable range is exceeded, the coal extracted again from the prepared secondary coal is measured, and the MF variation of the raw coal, the low grade coal, and the high fluidity material is estimated in the above (2). The difference from the MF of the primary coal blend is verified, and each element is corrected to determine the MF of the primary coal blend. Formulation of high fluidity material so that the estimated MF of the secondary coal blend is within the predetermined range of the desired MF (hereinafter sometimes referred to as “acceptable range”) from the determined MF of the primary coal blend The amount is set, and the production steps (4) to (6) are performed again. In addition, when the estimated MF of the secondary coal blend is different beyond the allowable range of the desired MF, the production steps (1) to (6) are performed again. Secondary blended coal within the desired MF tolerance is used as a raw material for coke production.

[Raw material for coke production produced by this production method]
The secondary blended coal produced by this production method has excellent caking properties or fluidity and is used as a raw material for coke production. Accurately estimate the MF of the primary blend with increased distribution of low-grade coal, and reduce the consumption of expensive high-grade coal by making it a secondary blend with the desired fluidity using a high fluidity material In addition, it has become possible to increase the consumption by expanding the range of use of low-grade coal that could only be used in small quantities as surplus. At the same time, a high-fluidity material is preliminarily blended with low-grade coal in advance to produce a precursor blended coal, and then the precursor blended coal is blended with raw coal to produce a secondary blended coal. A raw material for coke production having excellent cohesiveness or fluidity having high coke strength with MF can be produced.

  Specifically, as in the examples described later, the blending ratio of the low-grade coal to be blended is 0.1 to 10% with respect to the raw coal MF having normal log MF = 2 to 3 or characteristics close thereto. By this, logMF = 2-3 or the characteristic close | similar to this can be ensured about MF of secondary coal blend. In addition, when using a coal type or blended coal with a log MF exceeding 3, log MF = 2 to 3 or close to the MF of the secondary blended coal by setting the blending ratio of the low-grade coal to 10 to 20%. Characteristics can be secured. Such a production method can increase the consumption of low-grade coal, which has been limited to conventional use, and at the same time, can secure a low-cost coke production raw material with excellent coke strength and excellent caking properties. It became.

FIG. 4 illustrates the change in MF of the raw coal and the produced secondary blended coal in the blending process of the production process of the secondary blended coal in the above production process. Here, the solid line represents the case where the raw coal has MF having a desired (within tolerance) MF, the broken line represents the case of coal having fluidity exceeding this, and the alternate long and short dash line represents the case of coal having fluidity below that. Sort by. In the figure, when the blending amount of coking coal, low grade coal and high fluidity material is fixed,
(A) change in MF of a precursor blended coal in which a high fluidity material is blended close to a low-grade coal;
(B) A high fluidity material is preliminarily blended with a low-grade coal in advance so as to indicate a change in MF of the secondary blended coal obtained by blending the precursor blended coal with the raw coal, and a desired (within an allowable range). ) By producing a precursor blended coal having MF, a secondary blended coal having a desired MF and higher coke strength can be produced. on the other hand,
(C) Change in MF of primary blended coal by blending low-grade coal with raw coal,
(D) As shown by a thin line, the change in the MF of the secondary coal blend due to the blending of the high fluidity material into the primary coal blend is produced as a primary coal blend that is less than the desired MF by blending the excess low-grade coal. In such a case, the characteristics of the secondary coal blend are affected by the MF of the raw coal at the fixed blend amount. However, in this production method, as shown in steps (1) to (4) of the production process, the blending amount of the high fluidity material is calculated and set according to the MF of the raw coal, so that Secondary blended coal within an allowable range such as d1 and d2 can be produced. In the figure, d2 is the log MF supplementation ratio (the blending ratio of the high fluidity material / the blending ratio of the low-grade coal). The case where it is 1.0 or more is shown, and the MF of the secondary blended coal can be improved, and the coke quality including the coke strength can be improved.

[Method for estimating MF of primary coal blend according to the present invention]
The primary blended coal MF estimation method (hereinafter referred to as “the present estimation method”) according to step (2) of the production process selects one or more types of raw coal as reference coals, While determining the fluidity decreasing gradient of the low-grade coal based on the characteristics of the coal and the MF of the reference coal relative to one or more low-grade coal to be blended, and the MF of the raw coal actually used Based on the flow rate decrease gradient of the low-grade coal that is actually blended, the primary blended coal in which the low-grade coal is blended with the raw coal from the blending ratio of the low-grade coal blended with the raw coal Is estimated. In other words, the present estimation method estimates the MF of the primary coal blend with high accuracy simply and efficiently by the “procedure of the present estimation method” to be described later obtained in advance with reference coal based on the following knowledge. can do.
(A) The fluidity decrease gradient (hereinafter sometimes referred to as “Δlog MF”) accompanying the blending of low-grade coal is less dependent on the coal type and characteristics of the raw coal (reference coal). That is, Δlog MF when the same low-grade coal is blended with different raw coal (reference coal) does not depend on the characteristics of the raw coal (reference coal), such as the type of coal and MF. Therefore, a common estimated value can be set for the same low-grade coal.
(B) Δlog MF of low grade coal is unique to the brand of low grade coal. That is, Δlog MF when different low-grade coal is blended with the same raw coal (reference coal) is determined by the brand of the low-grade coal to be blended. Therefore, different estimated values can be set for the same raw coal (reference coal) by blending different low-grade coals.
Here, “log MF” indicates a common logarithm of the maximum fluidity (MF), and is used in actual evaluation. “Δlog MF” indicates the gradient (fluidity decreasing gradient).
Hereinafter, the verification process for obtaining the knowledge will be described in detail.

(I) Procedure of this estimation method This estimation method basically includes the following five steps.
(I-1) Step of actually measuring a fluidity characteristic curve of reference coal prepared in advance (for example, the characteristic illustrated in FIG. 2A) (i-2) The flowability characteristic curve obtained in the above (1) Step (i-3) of setting the MF of the reference coal Based on the low-grade coal prepared in advance to the reference coal and measuring the MF from the flow characteristic curve of the primary coal (i-4) Step (i-5) Estimating MF of Primary Coal Coal that is actually used Step of setting Δlog MF for each low-grade coal from MF of Primary Coal Coal The MF of the primary blended coal (log MF) is estimated using MF and Δlog MF set for the low-grade coal that is actually blended (planned). The fluidity of the primary coal blend accompanying the blending of the low-grade coal can be expressed by the following formula 3 as a general formula.
Y = S + α × X Equation 3
Where Y is the log MF of the primary blended coal
S is logMF of coking coal
α is △ logMF [1 /%] of low-grade coal
X is low-grade coal blending ratio [%]
In addition, when the range of MF (log MF) of the primary blended coal is set in advance, the desired primary blended coal is set by setting the blending ratio of the low-grade coal that is actually blended (planned). The MF (log MF) of can be estimated. In addition, if it is difficult to set the desired primary blended coal MF (log MF) for the low-grade coal to be blended, the appropriate one of the other low-grade coals for which Δlog MF is set in (4) above. A low-grade coal with Δlog MF set is selected, and the MF (log MF) of the primary blended coal is estimated. Furthermore, when it is difficult to select low-grade coal, part of the caking coal used in the raw coal is transferred to caking coal with different fluidity, and the log MF at the time of blending the low-grade coal is set within an appropriate range. It is also possible.

(Ii) Verification of characteristics of coking coal, low-grade coal and primary blended coal (ii-1) Coal used for verification Coking coal (reference coal), low-grade coal and primary blend used for verification of this estimation method The characteristics of charcoal are shown in Table 1 below. In the following, this estimation method including examples was used for verification.

(Ii-2) Verification of fluidity of coking coal (standard coal), low-grade coal, and primary blended coal Using the raw coal (standard coal), low-grade coal and primary blended coal in Table 1 above, the flow A degree characteristic curve was obtained, and MF and log MF of coking coal (reference coal) and low-grade coal were set. Table 2 below illustrates the flow rate measurement results when low grade coal A or low grade coal B is blended with raw coal J or raw coal K, and is illustrated in FIGS. 6 and 7. The values in () below show the weighted average value of log MF = 0 for low-grade coal.

Based on the measurement results in Table 2 above, ΔlogMF of the primary blended coal blended with the low-grade coal is obtained. 6 and 7, ◆ indicates the log MF of the primary coal when 1% or 3% of the low-grade coal A is blended with the coking coal (reference coal) J, L, K, and ■ indicates the coking coal. (Reference coal) The log MF of the primary blended coal when 1% or 3% of the low-grade coal B is blended with L and K is shown. As illustrated in FIGS. 6 and 7, when the fluidity log MF of the primary coal blend corresponding to the blending ratio of the low-grade coal is compared with each coal type and the low-grade coal, the above findings (a) and (b ) Can be verified quantitatively.
(A) As shown in FIG. 6 and FIG. 7, ΔlogMF when low grade coal A is blended with different raw coals (reference coals) J, L, and K is the raw coal (reference coal). It can be said that it does not depend on characteristics such as charcoal type and MF. Further, Δ when low grade coal B is blended with different coking coals (reference coals) L and K having MF of 949 [ddpm] (log MF 2.98) and 226 [ddpm] (log MF 2.35). The log MF was -0.130 and -0.128, respectively, and similar results were obtained. A common estimate can be set for the same low-grade coal.
(B) As shown in FIG. 6, the low grade coal B was blended with respect to the same raw coal (reference coal) with respect to ΔlogMF of −0.099 when blended with the low grade coal A. ΔlogMF in the case is −0.128, and ΔlogMF is determined by the brand of the low-grade coal to be blended. By blending different low-grade coals, different estimated values can be set for the same raw coal (reference coal).

[Verification of correction factors in estimation of MF of primary coal blend according to the present invention]
By the method as described above, the MF of the primary blended coal can be efficiently estimated by an unprecedented simple method. On the other hand, it was found that the MF of the primary blended coal depends on the brand of the low-grade coal to be blended, and there is a difference between the estimated value and the actual measurement value due to the characteristics of the blended low-grade coal. . Specifically, when five types of low-grade coals A to E as shown in Table 3 below were blended with raw coal (reference coal) and ΔlogMF of the primary blended coal was verified, estimated values shown in the same table And the measured value was obtained.

[Characteristic correction by oxygen content of low-grade coal]
From the verification results shown in Table 3 above, the fluidity of the primary blended coal depends on the brand of the low-grade coal to be blended, and the higher the oxygen content of the low-grade coal, the lower the fluidity. I understand that. Specifically, as illustrated in FIG. 8, as the oxygen content of the low-grade coal increases, the ΔlogMF for the low-grade coal that is closer to the final stage of the fluidity estimation process of the primary blend coal is set. It has an influence. At this time, as an actual correction curve, as illustrated in FIG. 8, a curve having a predetermined width (0.046 in the drawing) of the characteristic line is used. Table 4 below illustrates the median, upper limit, and lower limit when the blending ratio of low-grade coal is 10 to 30%. Different predetermined widths are set depending on the coal type. This is because the low grade coal may not be the same brand when the oxygen content is different. That is, depending on the specific low-grade coal, the oxygen content rate is different, which may be one of the factors of fluctuation of Δlog MF due to the difference in brands.

This estimation method obtains the fluctuation of Δlog MF with respect to the oxygen content shown in FIG. 8 and corrects Δlog MF related to low-grade coal set in advance by the brand, thereby more accurately as in the examples described later. It became possible to estimate the MF of the primary blended coal.
Specifically, in the case of the oxygen content rate a, ΔlogMF is calculated based on the following formula 4, and is inserted into the above formula 3 to be corrected.
ΔlogMF = −0.0061 × a + 0.0135 Formula 4
Here, since the oxygen content is normally specified in the characteristic table of coal, actual measurement is not particularly required, and there is no inconvenience associated with correction. Further, when there is a coal quality notation as the industrial analysis value as described above, the oxygen content can be calculated by the following formula 5.
Oxygen content [%] = 100-elements C, H, N, S [%] ... Formula 5

[Characteristic correction due to volatile content of low-grade coal]
The volatile matter is an important factor in chemically evaluating the quality of coal as described above. From the verification results shown in Table 3 above, it can be seen that the greater the volatile content of the low-grade coal, the lower the fluidity of the primary blended coal. Also in this estimation method, it was found that this tendency affects the low-log coal of Δlog MF of the blended primary coal. Specifically, as illustrated in FIG. 9, the greater the volatile content of the low-grade coal, the more the ΔlogMF of the primary coal blend is affected. This estimation method obtains a change in Δlog MF with respect to the volatile content shown in FIG. 9 and corrects Δlog MF related to low-grade coal that is set in advance by the brand, thereby more accurately 1 It became possible to estimate the MF of the next blended coal. Note that the volatile content of the low-grade coal to be blended is normally specified in the characteristic table of the coal, so that no actual measurement is required, and there is no inconvenience associated with the correction.
Specifically, in FIG. 9, in the case of the volatile content b [%], ΔlogMF is calculated based on the following formula 6, inserted into the above formula 3, and corrected.
ΔlogMF = −0.000313 × b2 + 0.0216 × b−0.413 Equation 6

<Example 1>
With regard to proximity blending, which is a feature of this production method, a demonstration test was conducted on the difference in effectiveness due to the difference in effectiveness and processing content. As sample charcoal, preliminarily crushed low-grade charcoal and high fluidity material were blended at a predetermined weight ratio, a mixed sample was prepared, and each treatment was performed by the following implementation method.
(I) Crimping (molding) treatment Using a cylindrical molder (BUEHLER, SIMPLIMET-II), the sample charcoal was crimped at a pressure of about 20 to 30 MPa for about 10 to 20 minutes. A molded product having an apparent density of about 1.1 to 1.5 g / cm ³ was obtained. At this time, when a pressure-bonding treatment was performed while heating, a strong molded product was obtained. In addition, when the pressure-bonding process is performed while heating, the detachment from the molding machine is facilitated by performing the slow cooling process.
(Ii) Granulation treatment Sample charcoal was put into a Sato-type vibrating screen (400-D, manufactured by Sakae Sangyo Co., Ltd.) and subjected to vibration treatment for about 10 to 20 minutes to produce a granulated product. As another method, a cylindrical rolling device (manufactured by Tanaka Tech Co., Ltd., RPB-3) was filled with sample charcoal, and rolled for about 1-2 hours at a rotational speed of about 20-30 rpm to produce a granulated product.
(Iii) Adhesion treatment Sample charcoal was put into a V-type blender (Nishimura Seisakusho, NV-10), mixed at a rotation speed of about 20-30 rpm for about 10-20 minutes, and a predetermined amount of PVA aqueous solution prepared to about 5% was prepared. After adding and mixing for 10 to 20 minutes at a rotational speed of about 20 to 30 rpm, the mixture is left to dry in a dryer.
(Iv) Kneading treatment Sample charcoal is put into a double-arm kneader (manufactured by Toshin, TK1-5M), heated to about 250 ° C. with a blade rotation of about 10 to 20 rpm and a nitrogen injection amount of about 2 L / min, After kneading for 30 minutes, it is cooled to obtain a kneaded product. When heated to 150 ° C. or higher, air in the atmosphere is taken in and combusted, so that the treatment was performed in a nitrogen atmosphere, and a kneaded material having good fluidity was obtained.

[Example 1-1]
A demonstration test was conducted on the effectiveness of proximity blending, which is a feature of this production method.
(I) Experimental condition measured value log MF: 2.1 relative to raw coal N, Δlog MF: -0.14 [logddpm] low grade coal F The condition of blending ratio 2.5 to 5%, and estimation Log MF: logMF in the case where the caking material P is blended close to the low-grade coal F when the secondary raw material coal blended with the caking material P which is a high fluidity material having a value log MF: 13 And the coke strength was estimated or measured and compared. As the close blending, a kneading process was performed at 250 ° C. for 30 minutes in a nitrogen atmosphere.
(Ii) Experimental results As shown in Table 5 below, Reference Example 1-1a, 1 in which the decrease in fluidity due to the low-grade coal blending can be compensated with the high fluidity binder and the proximity blending was not performed. Compared to -1b, it was found that high coke strength was obtained for Examples 1-1a and 1-1b which were kneaded. The excellent function of this fabrication method was proved.

[Example 1-2]
Next, a verification test was conducted on the difference in effectiveness due to the difference in the processing content of the proximity blending.
(I) Experimental condition measured value log MF: 2.0 relative to raw coal Na, Δlog MF: -0.10 [logddpm] low-grade coal F condition of 2.5% blending ratio, and estimated value log MF In the case of producing secondary raw coals containing caking materials P and Q, which are high fluidity materials of 13 and 6, it was not the case where caking materials P and Q were blended close to low-grade coal F. In some cases, log MF and coke strength were estimated or measured and compared. As the proximity blending, the following three treatments were performed.
(I-1) Kneading treatment of low-grade coal F and binder P for 30 minutes at 250 ° C. in a nitrogen atmosphere (i-2) 5% PVA with respect to low-grade coal F and binders P and Q (I-3) A mixture of low-grade coal F and caking additive P is placed in a φ32 cylindrical container and pressure-bonded at 29 MPa for 20 minutes. Molding process for processing (ii) Experimental results As shown in Table 6 below, Examples 1-2a to 1 in which proximity processing was performed in comparison with Reference Examples 1-2a and 1-2b in which proximity mixing was not performed With respect to -2d, high coke strength was obtained, and the effect of the proximity treatment was such that pressure treatment (molding treatment)> kneading treatment> granulation treatment. In addition, about the difference of Example 1-2d and Reference Example 1-2b, although an effect is not seen in DI, it turns out that there is a difference in RSI. The excellent function of this fabrication method was proved. In addition, as with the kneading process ([Example 1-1] above), also in the granulation process, the larger the log MF supplementation ratio (the blending ratio of the high fluidity material / the blending ratio of the low-grade coal), the more improved the coke strength. It was.

<Example 2>
About the effectiveness of the above estimation method, the following content was verified.
[Example 2-1] Estimation of fluidity of primary blended coal when log MF of coking coal is set high [Example 2-2] Primary blended coal when log MF of coking coal is set low Estimation of fluidity [Example 2-3] Estimation of fluidity of primary blended coal when blended with non-fluid coal

[Example 2-1]
The fluidity of the primary coal blend was estimated when the log MF of the raw coal was set high.
(I) Experimental conditions log MF: For coking coal L of 2.98, low grade coals A, B, and C are blended at a ratio of 5 to 10%, and log MF and Δlog MF of coking coal are measured and set. Compared with the estimated value.
(Ii) Experimental results As shown in Table 7 below, it was found that for log MF of the primary blended coal, the estimated value and the actually measured value are very consistent and the correlation is high. The excellent function of this estimation method is proved.

[Example 2-2]
The estimation of the fluidity of the primary blended coal when the log MF of the raw coal was set to a low value was performed in the same manner as in Example 2-1 above (i) Low experimental condition log MF (around 2.00) Using coking coal M and coking coal N, low-grade coal D, low-grade coal E, and low-grade coal F as the coal grade of low-grade coal, logMF and ΔlogMF Was measured, set, and compared with the estimated value.
(Ii) Experimental results As shown in Table 8 below, even when the log MF of the raw coal is set low, the estimated value of the log MF of the primary coal blend is consistent with the actual measurement value.

[Example 2-3]
In place of the low-grade coal in the above Examples 2-1 and 2-2, the fluidity of the primary blended coal was estimated when blending non-fluid coal into the raw coal (i) of the experimental condition logMF Low (around 2.00) raw coal M and raw coal N, low-grade coal G and low-grade coal H as coal types of non-fluid coal, under the conditions of a blending ratio of 10%, Log MF and Δlog MF were actually measured, set, and compared with the estimated values.
(Ii) Experimental results As shown in Table 9 below, the log MF of the primary blended coal is estimated even when using low-grade coal G and low-grade coal H such as anthracite that have advanced coalification and do not soften and melt. The values and the measured values were very consistent, and it was found that the fluidity of the primary coal blend could be estimated.

DESCRIPTION OF SYMBOLS 1 Coal carrier 2 Coal storage yard 3 Mixing tank 4 Crushing equipment 6 Coke oven 6a Coalbin 6b Loading car 6c Extruder 7 High fluidity material 8 Processing tank

Claims (5)

When making raw materials for coke production by blending low-grade coal with raw coal,
In order to compensate for the difference between the characteristics of the primary blended coal in which the low-grade coal is blended with the raw coal and the characteristics of the desired coke production raw material, Mixing in the vicinity of the low-grade coal to produce a precursor blended coal, blending the precursor blended coal with the raw coal and creating a secondary blended coal,
Coking coal, low-grade coal, high fluidity of coal or high fluidity material, and the blending ratio of the precursor blend coal, a method for manufacturing a setting to Turkey Kusu raw material for producing on the basis of the maximum fluidity degree is indicative of respective characteristics And
One or more types of the coking coal are selected in advance as the reference coal, the appropriate fluidity range of the reference coal, the fluidity characteristic curve with respect to the temperature of the reference coal, and the fluidity characteristic curve based on the above The maximum fluidity of the reference coal is obtained, and the flow of the low-grade coal based on the change in the maximum fluidity of the reference coal with respect to the blending ratio of the low-grade coal for one or more low-grade coals to be blended Find the slope of the degree of decline,
Based on the maximum fluidity of the raw coal actually used and the flow rate decrease gradient of the low-grade coal actually blended, the blending ratio of the low-grade coal blended with the raw coal Estimating the maximum fluidity of the primary coal blended with the low-grade coal in the coal,
Find the maximum fluidity of high-flow coal or high-fluidity material having a higher fluidity than the raw coal in advance,
In order to compensate for the difference between the maximum fluidity of the primary blended coal and the maximum fluidity of the desired coke production raw material, the blending ratio z of the high fluidity coal or high fluidity material is expressed by the following formula 2-1. A method for producing a raw material for coke production, which is set based on the above.
z = (Y2-Y1) / T ... Formula 2-1.
Here, Y2: Common logarithm of the maximum fluidity of the desired secondary coal blend (log MF)
Y1: Common logarithm of the highest fluidity of primary blended coal (logMF)
T: Common logarithm of the highest fluidity of high flow coal or high fluidity material (logMF) When making raw materials for coke production by blending low-grade coal with raw coal,
In order to compensate for the difference between the characteristics of the primary blended coal in which the low-grade coal is blended with the raw coal and the characteristics of the desired coke production raw material, Mixing in the vicinity of the low-grade coal to produce a precursor blended coal, blending the precursor blended coal with the raw coal and creating a secondary blended coal,
This is a method for producing raw materials for coke production, in which the blending ratio of coking coal, low grade coal, high fluidity coal or high fluidity material, and precursor blended coal is set based on the maximum fluidity that is the index of each characteristic. ,
One or more types of the coking coal are selected in advance as the reference coal, the appropriate fluidity range of the reference coal, the fluidity characteristic curve with respect to the temperature of the reference coal, and the fluidity characteristic curve based on the above The maximum fluidity of the reference coal is obtained, and the flow of the low-grade coal based on the change in the maximum fluidity of the reference coal with respect to the blending ratio of the low-grade coal for one or more low-grade coals to be blended Find the slope of the degree of decline,
Based on the maximum fluidity of the raw coal actually used and the flow rate decrease gradient of the low-grade coal actually blended, the blending ratio of the low-grade coal blended with the raw coal Estimating the maximum fluidity of the primary coal blended with the low-grade coal in the coal,
Find the maximum fluidity of high-flow coal or high-fluidity material having a higher fluidity than the raw coal in advance,
In order to compensate for the difference between the maximum fluidity of the primary blended coal and the maximum fluidity of the desired coke production raw material, the blending ratio z of the high fluidity coal or high fluidity material is expressed by the following formula 2-2. A method for producing a raw material for coke production, which is set based on the above.
z = α × Yo / T (Formula 2-2)
Here, α: Flow rate decreasing gradient of low-grade coal (ΔlogMF)
Yo: Common logarithm of the highest fluidity of low grade coal (logMF)
T: Common logarithm of the highest fluidity of high flow coal or high fluidity material (logMF) In the production of the precursor blended coal, the high-flow coal or the high-fluidity material is added to the low-grade coal by any one of pressure bonding, molding, granulation, adhesion, and kneading, or some combination of these treatments. The method for producing a raw material for producing coke according to claim 1 or 2, wherein the ingredients are blended close to each other.   Fluctuation of the fluidity lowering gradient with respect to the oxygen content of the low-grade coal to be blended is obtained, and the fluidity-decreasing gradient according to the low-grade coal used is corrected by the oxygen content of the low-grade coal. The manufacturing method of the raw material for coke manufacture in any one of Claims 1-3.   Fluctuation of the flow rate decrease gradient with respect to the volatile content of the low-grade coal to be blended is obtained, and the fluidity decrease gradient according to the low-grade coal used is corrected by the volatile content of the low-grade coal The manufacturing method of the raw material for coke manufacture in any one of Claims 1-4.

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