JPH09279152A - Grinding of coal charged into coke oven - Google Patents
Grinding of coal charged into coke ovenInfo
- Publication number
- JPH09279152A JPH09279152A JP9083396A JP9083396A JPH09279152A JP H09279152 A JPH09279152 A JP H09279152A JP 9083396 A JP9083396 A JP 9083396A JP 9083396 A JP9083396 A JP 9083396A JP H09279152 A JPH09279152 A JP H09279152A
- Authority
- JP
- Japan
- Prior art keywords
- coal
- less
- ratio
- coke
- total expansion
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Landscapes
- Coke Industry (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、同一石炭配合でコ
ークス強度の向上あるいは同一強度で安価な非微粘結炭
の増使用によるコークス素材費低減が可能となる配合石
炭の粉砕方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of pulverizing coal blends which can reduce coke material cost by improving coke strength with the same coal blend or by increasing the use of inexpensive non-caking coal of the same strength. is there.
【0002】[0002]
【従来の技術】高炉用コークス製造において、コークス
炉装入石炭の平均粒度を細かくすると石炭の均質化によ
りコークスのDI150 15 は向上するが、同時に石炭の嵩
密度の低下とCSR(CO2 反応後強度)の低下が生じ
る。このように単純に配合炭平均粒度のみを調整する場
合には、DI150 15 とCSRの両方を同時に向上させる
ことは困難である。2. Description of the Related Art In the production of blast furnace coke, when the average particle size of the coal charged in the coke oven is made finer, the homogenization of the coal improves the DI 150 15 of the coke, but at the same time, the bulk density of the coal decreases and the CSR (CO 2 reaction) After-strength) is reduced. Thus, it is difficult to simultaneously improve both DI 150 15 and CSR when simply adjusting the average particle size of the blended coal.
【0003】そこで、従来技術として、石炭粉砕時に不
活性成分は粗粒部分に、活性成分は細粒部分に集まる性
質を利用し、篩を用いた選択粉砕を行うことで嵩密度の
低下の防止と石炭の均質化を図る選択粉砕法がある。こ
の方法は、石炭を組織分析により活性成分(ビトリニッ
トおよびエグジニット)の多いグループと不活性成分
(イナーチニット)の多いグループとに分け、それぞれ
に適した篩い目で分級粉砕するものである。Therefore, as a conventional technique, when the coal is crushed, the property of collecting the inactive component in the coarse-grain portion and the active component in the fine-grain portion is utilized, and the selective pulverization using a sieve is performed to prevent the decrease of the bulk density. And there is a selective crushing method for homogenizing coal. According to this method, coal is divided into a group having a large amount of active components (vitrinite and exgenite) and a group having a large amount of inactive components (inertinite) by a structural analysis, and the particles are classified and pulverized by a sieve suitable for each group.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、従来の
選択粉砕方法は、篩い分けコストがかかるうえに、不活
性成分の少ない石炭ではその効果が小さく、CSRにつ
いては強度水準の低い場合しか効果がみられない。However, the conventional selective crushing method has a high sieving cost, and the effect is small with coal having a small amount of inert components, and the CSR is effective only when the strength level is low. I can't.
【0005】本発明の目的は、DI150 15 を維持しつ
つ、CSRの向上あるいは非微粘結炭の増使用によるコ
ークス素材費低減が可能となるような配合石炭の粉砕方
法を提供することにある。An object of the present invention is to provide a pulverizing method of blended coal which can improve the CSR or reduce the cost of the coke raw material by increasing the use of non-caking coal while maintaining DI 150 15. is there.
【0006】[0006]
【課題を解決するための手段】本発明は、上記の課題を
解決するために、 (1)全膨脹率が50%以上の銘柄の石炭を3mm以下
の割合が所定値より少なくなるように粗粉砕し、全膨脹
率が50%未満の銘柄の石炭を3mm以下の割合が所定
値より多くなるように微粉砕した後、配合して装入石炭
の3mm以下の割合を所定値に調整することを特徴とす
るコークス炉装入石炭の粉砕方法である。[Means for Solving the Problems] In order to solve the above problems, (1) Coal of a brand having a total expansion rate of 50% or more is coarsened so that a ratio of 3 mm or less is less than a predetermined value. After crushing and finely pulverizing the coal of the brand whose total expansion rate is less than 50% so that the ratio of 3 mm or less is more than the specified value, mix it and adjust the ratio of 3 mm or less of the charged coal to the specified value. A method for crushing coal charged in a coke oven, characterized by:
【0007】(2)全膨脹率が50%以上の銘柄の石炭
を3mm以下の割合が所定値より4重量%以上少なくな
るように粗粉砕し、全膨脹率が50%未満の銘柄の石炭
を3mm以下の割合が所定値より4重量%以上多くなる
ように微粉砕した後、配合して装入石炭の3mm以下の
割合を所定値に調整することを特徴とするコークス炉装
入石炭の粉砕方法である。(2) Coal of a brand having a total expansion rate of 50% or more is coarsely crushed so that a ratio of 3 mm or less is 4% by weight or more less than a predetermined value, and a brand of coal having a total expansion rate of less than 50% is Crushing of coke oven charged coal, characterized by finely pulverizing so that the ratio of 3 mm or less is 4% by weight or more above a predetermined value, and then blending to adjust the ratio of 3 mm or less of the charged coal to a predetermined value. Is the way.
【0008】ここで、全膨脹率はJIS−M8801に
したがって測定した。Here, the total expansion coefficient was measured according to JIS-M8801.
【0009】[0009]
【発明の実施の形態】図1に、単味炭の粉砕粒度と生成
するコークスのCSRの関係を示す。BEST MODE FOR CARRYING OUT THE INVENTION FIG. 1 shows the relationship between the crushed particle size of plain coal and the CSR of coke produced.
【0010】一般に石炭は粒度を粗くすると熱軟化時の
膨脹性が向上するため、生成コークス中の細かい気孔が
減少し、比表面積が小さくなる。したがって、コークス
のCO2 との反応率が低下することによりCSRが向上
する。Generally, when the particle size of coal is made coarse, the expandability at the time of thermal softening is improved, so that the fine pores in the produced coke are reduced and the specific surface area is reduced. Therefore, CSR is improved by decreasing the reaction rate of coke with CO 2 .
【0011】また、コークス炉装入石炭の平均の全膨脹
率は50%程度であり、全膨脹率50%未満の石炭では
上記の粗粒化によるコークスの比表面積減少の程度は相
対的に小さいため、CSRの向上効果は小さいが、全膨
脹率50%以上の石炭では粗粒化によるコークスの比表
面積減少の程度が相対的に大きいため、CSRの向上効
果は大きい。このことから、石炭粉砕時の粒度を分ける
境界指標として石炭の全膨脹率50%を設定する。Further, the average total expansion rate of the coal charged into the coke oven is about 50%, and in the case of coal having a total expansion rate of less than 50%, the degree of decrease in the specific surface area of the coke due to the above-mentioned coarsening is relatively small. Therefore, the effect of improving the CSR is small, but in the case of coal having a total expansion coefficient of 50% or more, the degree of decrease in the specific surface area of the coke due to the coarsening is relatively large, and therefore the effect of improving the CSR is large. From this, the total expansion coefficient of coal is set to 50% as a boundary index for dividing the particle size during coal crushing.
【0012】更に、各銘柄の石炭の3mm以下の割合の
所定値に対する増加幅あるいは減少幅については、4重
量%未満ではCSRの向上効果が小さいので、4重量%
以上とする。Further, with respect to the increase or decrease of the ratio of the coal of each brand of 3 mm or less with respect to the predetermined value, if the amount is less than 4% by weight, the effect of improving the CSR is small, so that 4% by weight.
Above.
【0013】[0013]
【実施例】石炭を全膨脹率の範囲で2つのグループに分
け、それぞれのグループの粒度を変化させてコークスを
製造した時のコークス強度の値を第1表に示す。EXAMPLE Coal is divided into two groups within the range of total expansion coefficient, and the coke strength when coke is produced by changing the particle size of each group is shown in Table 1.
【0014】[0014]
【表1】 [Table 1]
【0015】比較例1は全配合炭を3mm以下の割合が
配合炭平均値と同じになるように粒度調整した場合を示
す。Comparative Example 1 shows a case in which the particle size of all blended coals is adjusted so that the ratio of 3 mm or less becomes the same as the blended coal average value.
【0016】比較例2は全膨張率50%以上の石炭は配
合炭平均粒度よりも−3mmの割合が4%以上小さくな
るように粗く、また全膨張率50%未満の石炭は配合炭
平均粒度とほぼ同一になるように粒度調整した場合であ
る。この場合には、比較例1に対しCSRは向上してい
るものの、DI150 15 は若干低下している。In Comparative Example 2, coal having a total expansion coefficient of 50% or more is coarse so that the ratio of -3 mm is 4% or more smaller than the average particle size of the coal blend, and coal having a total expansion coefficient of less than 50% has an average particle size of the coal blend. This is the case when the particle size is adjusted so that it becomes almost the same as. In this case, the CSR is improved as compared with Comparative Example 1, but the DI 150 15 is slightly decreased.
【0017】実施例1は全膨脹率が50%以上の石炭は
配合炭平均粒度に対し−3mmの割合が4%小さくなる
ように粗く、また全膨脹率が50%未満の石炭は配合炭
平均粒度に対し−3mmの割合が6%大きくなるように
細かく粒度調整した場合を示す。この場合には、DI
150 15 、CSRともに比較例1に対して向上している。In Example 1, coal having a total expansion rate of 50% or more is coarse so that the ratio of -3 mm to the average particle size of the blended coal is 4% smaller, and coal having a total expansion rate of less than 50% is the blended coal average. The case where the particle size is finely adjusted so that the ratio of -3 mm to the particle size is 6% larger is shown. In this case, DI
Both 150 15 and CSR are better than Comparative Example 1.
【0018】[0018]
【発明の効果】以上のように本発明によってDI150 15
を維持しつつ、CSRの向上あるいは非微粘結炭の増使
用によるコークス素材費低減を達成することができる。INDUSTRIAL APPLICABILITY As described above, according to the present invention, DI 150 15
While maintaining the above, it is possible to improve the CSR or reduce the cost of the coke material by increasing the use of the non-caking coal.
【図1】単味炭の粉砕粒度と生成コークスのCSRの関
係Fig. 1 Relationship between crushed particle size of plain coal and CSR of coke produced
Claims (2)
mm以下の割合が所定値より少なくなるように粗粉砕
し、全膨脹率が50%未満の銘柄の石炭を3mm以下の
割合が所定値より多くなるように微粉砕した後、配合し
て装入石炭の3mm以下の割合を所定値に調整すること
を特徴とするコークス炉装入石炭の粉砕方法。1. Coal of a brand having a total expansion rate of 50% or more is 3
Coarsely crushed so that the ratio of mm or less is less than the specified value, and finely pulverized coal of the brand whose total expansion rate is less than 50% so that the ratio of 3 mm or less is more than the specified value, and then blending and charging. A method for pulverizing a coal charged in a coke oven, which comprises adjusting a ratio of coal of 3 mm or less to a predetermined value.
mm以下の割合が所定値より4重量%以上少なくなるよ
うに粗粉砕し、全膨脹率が50%未満の銘柄の石炭を3
mm以下の割合が所定値より4重量%以上多くなるよう
に微粉砕した後、配合して装入石炭の3mm以下の割合
を所定値に調整することを特徴とするコークス炉装入石
炭の粉砕方法。2. Coal of a brand having a total expansion rate of 50% or more is 3
Coarsely crushed so that the ratio of mm or less is 4% by weight or more less than the predetermined value, and 3 brand coals with a total expansion rate of less than 50%
Milling of coke in a coke oven characterized by finely pulverizing so that the proportion of mm or less is 4% by weight or more above a predetermined value and then blending to adjust the proportion of 3 mm or less of the charging coal to a predetermined value. Method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9083396A JPH09279152A (en) | 1996-04-12 | 1996-04-12 | Grinding of coal charged into coke oven |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9083396A JPH09279152A (en) | 1996-04-12 | 1996-04-12 | Grinding of coal charged into coke oven |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH09279152A true JPH09279152A (en) | 1997-10-28 |
Family
ID=14009596
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9083396A Withdrawn JPH09279152A (en) | 1996-04-12 | 1996-04-12 | Grinding of coal charged into coke oven |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH09279152A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000303075A (en) * | 1999-04-23 | 2000-10-31 | Nippon Steel Corp | Production of coke |
JP2007112941A (en) * | 2005-10-21 | 2007-05-10 | Nippon Steel Corp | Method for producing coke |
JP2013001873A (en) * | 2011-06-20 | 2013-01-07 | Nippon Steel & Sumitomo Metal Corp | Method for producing coke |
JP2013001895A (en) * | 2011-06-21 | 2013-01-07 | Nippon Steel & Sumitomo Metal Corp | Estimation method of coke strength after hot reaction |
-
1996
- 1996-04-12 JP JP9083396A patent/JPH09279152A/en not_active Withdrawn
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000303075A (en) * | 1999-04-23 | 2000-10-31 | Nippon Steel Corp | Production of coke |
JP4669094B2 (en) * | 1999-04-23 | 2011-04-13 | 新日本製鐵株式会社 | Coke production method |
JP2007112941A (en) * | 2005-10-21 | 2007-05-10 | Nippon Steel Corp | Method for producing coke |
JP2013001873A (en) * | 2011-06-20 | 2013-01-07 | Nippon Steel & Sumitomo Metal Corp | Method for producing coke |
JP2013001895A (en) * | 2011-06-21 | 2013-01-07 | Nippon Steel & Sumitomo Metal Corp | Estimation method of coke strength after hot reaction |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP5741246B2 (en) | Coke oven charging method and coke manufacturing method | |
CN108117879A (en) | The blending method that a kind of part moisture-control grading crushes | |
JPH09279152A (en) | Grinding of coal charged into coke oven | |
CN110982548B (en) | Coal preparation method for coking coal material | |
JP5151490B2 (en) | Coke production method | |
JP6198640B2 (en) | Petroleum coke blowing blast furnace operation method | |
JPH04309592A (en) | Production of blast furnace coke | |
JP5686052B2 (en) | Coke production method | |
JP4617814B2 (en) | Coke production method | |
CN111778048B (en) | Method for regulating and controlling granularity of matched coal | |
JP3971615B2 (en) | Method for adjusting the particle size of coal for coke oven charging | |
JP2001181650A (en) | Method for preparing coal for charging into coke oven | |
JPH11181441A (en) | Production of coke for metallurgy | |
JP3620386B2 (en) | Coke oven charging coal | |
JPH09279151A (en) | Grinding of coal charged into coke oven | |
JP4102015B2 (en) | Method for adjusting the particle size of coal for coke production | |
KR890002352B1 (en) | Method for controlling density of coal for producing cokes | |
JPS61126199A (en) | Preparation of powder coke for sintered fuel | |
JPH10130653A (en) | Method for pretreating coal for coke making and production of coke | |
JP2009270104A (en) | Coke manufacturing method | |
JPS62190284A (en) | Production of coke | |
JPH0120680B2 (en) | ||
JP2000303075A (en) | Production of coke | |
JPH04335093A (en) | Method for treating coal | |
JPH0260711B2 (en) |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A300 | Withdrawal of application because of no request for examination |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20030701 |