JP2015199976A - Method for producing sintered ore, and method for evaluating coal char or anthracite coal or half-anthracite coal - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a method for producing sintered ore capable of increasing the kind of carbonaceous material usable as a flocculation material and evading exert influence exerted on the productivity of sintered ore, and a method for evaluating coal char or anthracite coal or half-anthracite coal.SOLUTION: Provided is a method for producing sintered ore using coal char or anthracite coal or half-anthracite coal as a carbonaceous material for sintering, characterized in that heating is performed at a velocity equal that of the temperature rising velocity of a sintering raw material upon sintering in a nitrogen atmosphere, a coal char or anthracite coal or half-anthracite coal in which the reduction amount of the volatile content at 650°C is desired value or lower (other than those whose volatile content in industrial analysis is 5 mass% or lower) is used as a carbonaceous material for sintering.

Description

  The present invention relates to a method for producing sintered ore, and a method for evaluating coal char or anthracite or semi-anthracite.

  Sinter ore manufacturing process includes iron ore and raw materials containing iron such as sieving powder, dust, mill scale, etc. generated inside and outside the sintering plant system, and limestone The material (sub-material) is used as a new raw material for sintering. Addition of carbonaceous material (condensation material) for sintering and return ore (sintered ore that did not satisfy the product particle size and circulated for re-sintering) to the new raw material And Currently, in the sinter ore manufacturing process of the Dwytroid (DL) type sintering machine that is generally performed, the lower part of the packed bed made of the above blended raw material is set to a negative pressure, and air is circulated from the upper part to the lower part in the blended raw material. Burn the condensed material. Sintered ore is produced by sintering the blended raw materials with the generated combustion heat. This sintered ore is used as the main raw material in the blast furnace.

At present, in the sinter manufacturing process, pulverized coke and anthracite are used as a coagulant. The volatile content of powder coke is 1% or less, and the volatile content of anthracite is about 5%.
Powdered coke is coke having a small particle size after sieving sized coke suitable for blast furnace production among coke produced at steelworks. However, the amount of powdered coke is small compared to the sized coke used by the blast furnace, which is insufficient as coke for producing sintered ore. If there is a shortage of coke breeze due to the balance in the steelworks, it is necessary to select and use anthracite. On the other hand, the reserves of anthracite with low volatile content have been depleted.

The use of coal such as semi-anthracite, bituminous coal, sub-bituminous coal, and lignite as a sintering carbonaceous material is being investigated as an alternative fuel for powdered coke and anthracite coal.
However, coal such as semi-anthracite, bituminous coal, sub-bituminous coal, and brown coal has a high volatile content of 10 to 50%. Cause troubles such as malfunction of exhaust gas blower and coloration of exhaust gas finally discharged from the chimney.
Therefore, in order to use these coals as sintering carbon materials, it is necessary to char by some means to reduce the volatile content to less than 10%, preferably about 5%.

Up to now, there has been a proposal to use char produced by pyrolyzing coal at 300 ° C. to 900 ° C. as a total amount or a part of a sintering carbon material (Patent Document 1).
In addition, there is a proposal of using char produced by pyrolyzing coal (subbituminous coal, lignite) at 600 ° C. to 900 ° C. using a circulating fluidized bed as a sintering carbon material (Patent Document 2).
Also, there is a proposal for producing char by heating and distilling coal to 300 to 1150 ° C. with an internal combustion type rotary kiln, and combusting and removing 250 μm fine powder particles generated from the coal, and then subjecting the coal to carbonization (patent) Reference 3).
Furthermore, the average combustion rate of char produced from coal having a volatile content of 30% by mass or more and 51% by mass or less is 1.05 times or more and 1.22 times or less of the powder coke. There is a proposal of a method for producing a sintered ore (Patent Document 4).

JP-A-5-230558 JP 2010-254929 A Japanese Patent No. 4842410 JP 2013-087342 A

  However, as a coagulant having a low volatile content replacing powder coke, not only the char described in Patent Documents 1 to 4 but also other options are desired.

  An object of the present invention is to provide a method for producing a sinter ore and a coal char which can increase the types of carbon materials that can be used as a coagulant and can avoid adverse effects on the productivity of the sinter. Or providing an evaluation method for anthracite or semi-anthracite.

Until now, the volatile matter in the carbonaceous material has been evaluated based on numerical values obtained by an analytical method defined by so-called industrial analysis (JIS-M8812). In the above analysis method, the volatile matter is calculated from the weight reduction when heated to 900 ° C. in a state where the air is shut off.
For this reason, the carbon material having a relatively large volatile content evaluated by the above analysis method has been considered to be unsuitable for the sintering carbon material because the volatile component flowing into the exhaust gas becomes a problem. Here, as the carbon material having a relatively large volatile content evaluated by the above analysis method, the raw material coal including semi-anthracite coal other than so-called anthracite coal, which is called a highly volatile coal material, or produced at a relatively low temperature is used. Examples include coal char.

However, assuming use as a carbon material for sintering, not all volatile components measured by the industrial analysis are scattered in the exhaust gas. Certainly, the volatile matter that volatilizes before the charcoal starts to burn is entrained in the exhaust gas. However, the volatile matter remaining after the charcoal starts to burn will be burned in the sintering bed as the charcoal burns. Therefore, such a volatile matter is not accompanied in the exhaust gas, and it is assumed that no problem occurs.
Based on the above inference, the inventor has focused on the volatile matter that is effectively used in the sintering bed and the volatile matter that is entrained in the exhaust gas. Then, by newly defining the volatile matter that volatilizes until the charcoal starts to burn, and selecting and using the charcoal according to the regulations, adverse effects on the productivity of sintered ore can be avoided, and condensation can be achieved. It was found that the types that can be used as materials can be increased. The present invention is based on these findings.

The gist of the present invention is as follows.
(1) A method for producing sintered ore using coal char, anthracite or semi-anthracite as a carbon material for sintering, and heating in a nitrogen atmosphere at a rate equivalent to the rate of temperature increase of the sintering raw material during sintering And burn charcoal with a percentage of mass loss at 650 ° C. relative to the initial mass (hereinafter referred to as “devolatilization rate”) or anthracite or semi-anthracite (except for volatile content of 5% by mass or less in industrial analysis). A method for producing a sintered ore characterized by being used as a coal for binding.
(2) In the nitrogen atmosphere, heating is performed at a rate equivalent to the rate of temperature rise of the sintering raw material during sintering, and the devolatilization rate at 650 ° C. of coal char or anthracite or semi-anthracite is measured, and the devolatilization is performed. The method for producing a sinter according to (1), wherein a coal char having a ratio equal to or less than a desired value, or anthracite or semi-anthracite is used as a carbon material for sintering.
(3) Evaluation method for coal char, anthracite or semi-anthracite, heated at a rate equivalent to the rate of temperature rise of the sintering raw material during sintering in a nitrogen atmosphere, and measured the devolatilization rate at 650 ° C. A method for evaluating coal char or anthracite or semi-anthracite.

  According to the present invention, it is possible to increase the types of carbonaceous materials that can be used as a coagulating material by using coal char having an devolatilization ratio within a predetermined range, or anthracite or semi-anthracite as a carbonaceous material for sintering. Adverse effects on the productivity of the ore can be avoided.

It is a figure which shows the relationship between the temperature increase rate of the carbonaceous material A, and a devolatilization rate. It is a figure which shows the relationship between the temperature increase rate of each carbon | charcoal material, and a devolatilization rate.

Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.
(Sinter ore manufacturing method)
The method for producing sintered ore of the present embodiment calculates the devolatilization ratio of coal char or anthracite or semi-anthracite, and selectively uses coal char or anthracite or semi-anthracite as a carbon material for sintering. It is what.
In the present invention, coal char is obtained by pyrolyzing coal (brown coal, subbituminous coal, bituminous coal) at 300 to 900 ° C. and used as a raw material for sintering. Anthracite and semi-anthracite are coals having a high degree of coalification and a relatively low volatile content, and are used as raw materials for sintering.
Here, coal with an volatile content (dry coal mass standard) of less than 10% in industrial analysis is defined as anthracite, and coal with a volatile content (dry coal mass standard) of 10% to 15% is defined as semi-anthracite. To do.

Here, the devolatilization ratio is calculated using the following evaluation method.
First, 10 mg of a measurement sample is placed on a thermobalance. Then, after the inside of the apparatus is sufficiently purged with nitrogen, the temperature is raised with a flow of nitrogen of 200 ml / min, and maintained at 120 ° C. for 30 minutes to sufficiently dry the measurement sample. Next, rapid heating is performed at a rate of temperature increase of 100 ° C./min, and the weight loss when the sample temperature reaches 650 ° C. is measured. The devolatilization ratio [mass%] is calculated from the following formula (1) based on the measurement result.

式中、Ａは１００℃／ｍｉｎ急速昇温開始時の試料重量（ｍｇ）であり、Ｂは６５０℃における試料重量（ｍｇ）であり、Ａ−Ｂは６５０℃までに揮発した揮発分である。

In the formula, A is a sample weight (mg) at the start of rapid heating at 100 ° C./min, B is a sample weight (mg) at 650 ° C., and A-B is a volatile component volatilized by 650 ° C. .

  The above-mentioned evaluation method measures the devolatilization behavior of carbonaceous materials at each temperature level by using a thermobalance capable of rapid temperature increase and rapidly heating in an inert gas atmosphere such as nitrogen. The carbonaceous material for sintering usually starts to burn in a temperature range of about 600 ° C to 650 ° C. For this reason, in the said evaluation method, the devolatilization ratio in 650 degreeC is made into the carbonaceous material evaluation parameter | index.

Moreover, although the devolatilization behavior of the carbonaceous material changes according to the temperature rising rate, the heat pattern (temperature rising rate of the sintering raw material) in a general sintering bed is about 100 to 300 ° C./min. For this reason, in the said evaluation method, the temperature increase rate is made into the speed equivalent to the temperature increase rate of the sintering raw material at the time of sintering.
In FIG. 1, the relationship between the temperature increase rate of the carbonaceous material A and a devolatilization rate is shown. As shown in FIG. 1, the result of heating at a lower temperature increase rate of 10 ° C./min is higher than the result of heating at a temperature increase rate of 100 ° C./min. . As is apparent from this result, it can be seen that when the heating rate is lower than 100 ° C./min, the devolatilization rate at 650 ° C. is apparently increased. Therefore, at a low temperature increase rate, the devolatilization behavior of the carbonaceous material in the sintering bed may not be accurately reproduced.
Among these, the heating rate is more preferably 100 ° C./min to 300 ° C./min, and particularly preferably 100 ° C./min. If the rate of temperature increase is less than 100 ° C./min, as described above, the devolatilization rate may be underestimated. On the other hand, if the rate of temperature rise exceeds 300 ° C./min, the devolatilization rate may be overestimated.

In the method for producing a sintered ore according to the present embodiment, coal char having an devolatilization ratio equal to or less than a desired value, or anthracite or semi-anthracite is used as a carbon material for sintering. The desired value may be determined and managed in consideration of various factors in the sintering operation management, but 5% by mass is preferable. Here, various factors to be taken into consideration are the amount of organic chlorine in exhaust gas, the amount of dust oil, the vibration of the blower, etc., and the desired value is determined so that these are within the control value.
By using coal char with an devolatilization rate less than the desired value, or anthracite or semi-anthracite as a sintering carbonaceous material, the volatile components contained in the carbonaceous material are not combusted in the sintering bed and are entrained in the exhaust gas. It becomes possible to reduce the ratio to do. For this reason, it is possible to avoid various equipment troubles caused by volatile components entrained in the exhaust gas. In addition, parts other than the volatile matter released before the start of combustion of the carbonaceous material are used for combustion in the sintering bed. As a result, a smaller amount of carbonaceous material is required for the sintering reaction. It becomes possible to cover the amount of heat. In addition, if the devolatilization ratio exceeds the desired value, the trouble accompanying the volatile components entrained in the exhaust gas may be increased, and the amount of volatile components that are combusted and used in the sintering bed is relatively reduced. The amount of heat required for sintering may not be covered.
The use of anthracite or coal char with a volatile content of 5% by mass or less in industrial analysis as a carbon material for sintering has been reported so far. However, the above devolatilization rate is also satisfied for anthracite, semi-anthracite, and coal char containing high volatile content that has been thought to be difficult to use as a carbon material for sintering. If the evaluation is obtained, it can be used as a carbon material for sintering. For this reason, according to this embodiment, the kind of carbonaceous material which can be used as a carbonaceous material for sintering can be increased.

(Evaluation method for coal char, anthracite or semi-anthracite)
The evaluation method of coal char of this embodiment, or anthracite or semi-anthracite, is characterized by measuring the devolatilization rate of coal char or anthracite or semi-anthracite up to 650 ° C. According to this evaluation method, whether or not it can be used as a carbon material for sintering, which has been vaguely determined based on the volatile content value defined in the industrial analysis, can be determined by a simple method.

  Next, the present invention will be described in more detail with reference to examples. Therefore, the grounds that the devolatilization ratio is preferably 5% by mass or less are shown. In addition, this invention is not restrict | limited at all by these examples.

(Characteristics and devolatilization rate of each charcoal)
The properties and devolatilization ratio of each carbon material are shown in Table 1 below. Moreover, the relationship between the temperature increase rate of each carbon | charcoal material and a devolatilization rate is shown in FIG.
The devolatilization ratio of each carbon material was measured by the following method.
First, 10 mg of a measurement sample (alumina sample container (depth 2.5 mm × diameter 5 mm)) was placed on a thermobalance (Rigaku Corporation / Thermo Plus Evo2 TG-DTA8120 / H-IR smart loader infrared heating type). Then, after the inside of the apparatus was sufficiently purged with nitrogen, the temperature was raised in a state where nitrogen was circulated at 200 ml / min, and maintained at 120 ° C. for 30 minutes to sufficiently dry the measurement sample. Next, rapid heating was performed at a rate of temperature increase of 100 ° C./min, the weight loss when the sample temperature reached 650 ° C. was measured, and the devolatilization rate was calculated from the above formula (1).
In FIG. 2, carbon materials (A, B, C, D, E) having a devolatilization rate up to 650 ° C. of 5% by mass or less, indicated by triangular symbols, are preferably used as sintering carbon materials. It is a range. Among these, although the carbon material E has a larger volatile content than the carbon material F, since it has a small devolatilization rate up to 650 ° C., it can be evaluated that the carbon material is a preferable carbon material for sintering.

(Sintering experiment)
Using the charcoal materials (powder coke, anthracite, semi-anthracite, coal char) shown in Table 1 above, a firing pot test was carried out, and the sinter productivity and the amount of volatile matter (tar) contained in the exhaust gas were confirmed. .
The raw material composition used in the baking pot test is shown in Table 2 below. Table 3 shows the particle size distribution of the carbonaceous materials used. In all tests, the particle size distribution of the charcoal was the same. The amount of the carbon material used is 4.5% by mass (outside number) of the dried coke boiled base (reference example). When using the carbon materials A to G, the weight of the carbon material after drying is the same as that of the base. The total amount of coke was replaced with carbonaceous materials A to G.

  In the sintering pot test, the blended raw materials were mixed for 1 minute using a drum mixer having a diameter of 1 m, and then granulated for 4 minutes to prepare a pseudo particle raw material. A sintering pot test apparatus (diameter: 300 mm, layer height: 600 mm) And was fired under the conditions of ignition for 90 seconds and suction negative pressure of 15 kPa. Evaluation items were combustion progress rate, product yield, production rate, and volatile content in exhaust gas. The method for measuring the volatile content in the exhaust gas is shown below.

(Measurement method of volatile content in exhaust gas)
(1) Suction is performed at 1.0 to 3.0 L / min into an absorption bottle filled with dichloromethane using the exhaust gas during the pot test (from ignition to completion of sintering) as an absorption liquid.
(2) The absorption liquid after gas suction is filtered to remove dust. If there is clearly a lot of water, the water is removed by decantation.
(3) After evaporating dichloromethane by heating the absorbing solution on a hot plate at 80 ° C. or lower, the residual weight at the time when the amount becomes constant is defined as the volatile content (tar) content in the exhaust gas. The concentration of volatile matter (tar) in the exhaust gas is calculated by dividing by the amount of gas sucked into the absorbent.

The results of the sintering pot test are shown in Table 4.
Carbon material B is anthracite which has already been widely used for sintering, and its volatile content in the exhaust gas was 0.07 g / Nm ³ . Compared with this, the carbonaceous materials A and C to E are almost equal to or less than that, and thus determined to be usable in sintering. On the other hand, that of carbon materials F and G was more than twice that of carbon material B. Based on these results, the desired value of the devolatilization ratio is preferably 5% by mass.
In addition, although Examples 1-5 compared with the reference example using a powder coke, it became a result from which combustion progress speed FFS and a product yield varied, respectively, originated in the combustibility etc. of a carbonaceous material differing. The production rate was not significantly below the reference example. On the other hand, in Comparative Examples 1 and 2 using the carbonaceous materials F and G, the product yield was significantly reduced as compared with the Reference Example. This was clearly a lack of heat.
The content of volatile components contained in the exhaust gas is the highest in Comparative Examples 1 and 2, and the carbonaceous materials F and G of Comparative Examples 1 and 2 are volatilized released without burning in the sintering bed. The amount was suggested to be large.

  By using coal char with an devolatilization ratio within a specified range, or anthracite or semi-anthracite as a sintering carbon material, the types of carbon materials that can be used as agglomerated material can be increased, and the productivity of sintered ore can be increased. The adverse effects can be avoided.

Claims (3)

A method for producing sinter using coal char or anthracite or semi-anthracite as a carbon material for sintering,
In a nitrogen atmosphere, heating is performed at a rate equivalent to the temperature increase rate of the sintering raw material at the time of sintering, and a coal char whose an amount of mass reduction at 650 ° C. is less than a desired value, anthracite or semi-anthracite (industrial A method for producing a sintered ore characterized in that a volatile content in the analysis is less than 5% by mass) as a carbon material for sintering.   In the nitrogen atmosphere, heated at a rate equal to the rate of temperature increase of the sintering raw material during sintering, and measured the percentage of the mass loss at 650 ° C. of coal char or anthracite or semi-anthracite to the initial mass, 2. The method for producing a sinter according to claim 1, wherein a coal char whose percentage is equal to or less than a desired value, or anthracite or semi-anthracite is used as a sintering carbonaceous material. A method for evaluating coal char or anthracite or semi-anthracite,
In a nitrogen atmosphere, the mixture is heated at a rate equivalent to the rate of temperature rise of the sintering raw material during sintering, and the percentage of the mass reduction amount at 650 ° C. with respect to the initial mass is measured. Anthracite evaluation method.

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