JPS6289792A - Production of compressively formed coal - Google Patents

Production of compressively formed coal

Info

Publication number
JPS6289792A
JPS6289792A JP22902685A JP22902685A JPS6289792A JP S6289792 A JPS6289792 A JP S6289792A JP 22902685 A JP22902685 A JP 22902685A JP 22902685 A JP22902685 A JP 22902685A JP S6289792 A JPS6289792 A JP S6289792A
Authority
JP
Japan
Prior art keywords
coal
chamber
coke
wall side
divided
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.)
Pending
Application number
JP22902685A
Other languages
Japanese (ja)
Inventor
Heizou Mera
目羅 平藏
Yutaka Takahashi
裕 高橋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JFE Steel Corp
Original Assignee
Kawasaki Steel Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP22902685A priority Critical patent/JPS6289792A/en
Publication of JPS6289792A publication Critical patent/JPS6289792A/en
Pending legal-status Critical Current

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  • Coke Industry (AREA)

Abstract

PURPOSE:To obtain coke provided with uniformity, small in quality variation even at both low dry distrillation temperature and heating rate, by filling raw coal of mutually different grade into each compartment of the forming mold divided with partitioning plates followed by compressoin forming to make a layered structure by grade. CONSTITUTION:A forming mold 10 is so divided with partitioning plates 12 as to correspond to the central part 11b and wall-side part 11a along the walls in contact with the combustion chamber in a coke oven carbonizing chamber. Each of the resulting parts 11a and 11b is filled with raw coal of mutually different grade followed by compression forming of said coal in the absence of the partitioning plates 12 to make a layered structure, thus obtaining the objective coke.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、仕切板で分画された成形型の各室へ、それ
ぞれ品位の異なる原料炭を充填圧縮して成形する圧縮成
形炭の製造方法に関する。
[Detailed Description of the Invention] [Industrial Application Field] This invention relates to the production of compression molded coal by filling and compressing coking coal of different grades into each chamber of a mold separated by a partition plate. Regarding the method.

〔従来の技術〕[Conventional technology]

一般に、コークス炉に使用される原料炭とじての石炭の
品質は、良質炭と劣質炭又は低品位炭とに大別され、良
質炭には強粘結炭、単弦粘結炭。
In general, the quality of coal used in coke ovens, including coking coal, is roughly divided into high-quality coal and inferior-quality coal, or low-grade coal.High-quality coal includes strong caking coal and single string caking coal.

劣質炭には弱粘結炭、微粘結炭等がある。Inferior quality coal includes weakly caking coal and slightly caking coal.

これらの石炭を原料とするコークスの品質は、コークス
炉に装入される上記石炭の品質による影響が最も大きい
が、このほか、コークス炉炭化室に装入される石炭の嵩
密度および炭化室での熱の受は方にも影響される。
The quality of coke made from these coals is most influenced by the quality of the above-mentioned coal charged into the coke oven, but in addition, the bulk density of the coal charged into the coke oven carbonization chamber and the quality of the coke in the coke oven Heat reception is also affected by the direction.

従来、第5図に示すように品位の異なる石炭を混合して
から各炭化室1へ、炭化室頂部に設けられた装入孔2よ
り装入車によって落下せしめて装入するトップチャージ
方式が広く採用されているが、この方式によって製造さ
れたコークス3は品質のバラツキが大きい。そこで、石
炭のコークス化性を向上する目的で、石炭のコークス化
過程における膨張性を利用して粉炭部分を圧密化するこ
とにより、トップチャージされた原料炭の嵩密度を高め
る方法が行われている。これは、具体的には、原料炭を
予め成形型でブリケット状に成形し、その30%を非成
形炭である装入炭と混合して全体としての嵩密度を10
%高くする成形炭一部装入法である。この方法は、原料
炭の嵩密度を高め且つコークス強度の向上を図るもので
はあるが、トップチャージ法で製造されるコークスでは
、その炉内における高さ方向、長さ方向の位置によって
嵩密度に差が生じ、これがコークス強度のバラツキの原
因の一つとなっている。そしてこの嵩密度のバラツキを
減少させるための一つの方法として、石炭をコークス炉
外で成形してブロックを作り、このブロックを炉内(炭
化室内)へ装入するブロック装入法がある。この方法に
よれば、原料炭は一定の嵩密度で成形されるため、前記
炉内位置での嵩密度の差に起因するコークス強度の差は
なくなる。
Conventionally, as shown in Fig. 5, there is a top charge method in which coals of different grades are mixed and charged into each carbonization chamber 1 by being dropped by a charging vehicle through a charging hole 2 provided at the top of the chamber. Although it has been widely adopted, the quality of coke 3 produced by this method varies widely. Therefore, in order to improve the coking properties of coal, a method has been used to increase the bulk density of top-charged coking coal by compacting the pulverized coal part by utilizing the expansibility of coal during the coking process. There is. Specifically, raw coal is formed into briquettes using a mold in advance, and 30% of the briquettes are mixed with charging coal, which is non-briquette coal, to reduce the overall bulk density to 10%.
This is a partial charging method of briquette coal to increase the amount of coal. This method aims to increase the bulk density of coking coal and coke strength, but the bulk density of coke manufactured by the top charge method varies depending on its position in the height and length directions in the furnace. This difference is one of the causes of variation in coke strength. One method for reducing this variation in bulk density is a block charging method in which coal is formed into a block outside the coke oven and this block is charged into the furnace (inside the carbonization chamber). According to this method, since the raw coal is molded to have a constant bulk density, there is no difference in coke strength caused by a difference in bulk density at the position in the furnace.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかしながら、コークスの品質は、原料炭のコークス化
過程における熱の受は方によっても影響を受けるため、
このような従来の方法にあっては、ブロック装入法であ
っても、両側を燃焼室4で挟まれた炭化室1の燃焼室に
近い側と中央部分とではコークスの品質が均一にならな
いという問題点があった。
However, the quality of coke is also affected by the way the coking coal receives heat during the coking process.
In such conventional methods, even in the block charging method, the quality of coke is not uniform between the side near the combustion chamber and the center of the coking chamber 1, which is sandwiched between combustion chambers 4 on both sides. There was a problem.

この発明は、このような従来の問題点に着目してなされ
たもので、原料炭のプロ・ツクを品位の異なる石炭で層
状に成形して炉に装入することにより、上記問題点を解
決することを目的としている。
This invention was made by focusing on these conventional problems, and it solves the above problems by molding coking coal into layers with coal of different grades and charging it into a furnace. It is intended to.

〔問題点を解決するための手段〕[Means for solving problems]

この発明は、原料炭である石炭を成形するための成形型
内を、コークス炉炭化室の燃焼室に接する壁に沿った壁
側部と、この両方の壁側部の間の中央部とにそれぞれ相
当するごとく仕切板で分割し、分割して画成された壁側
室と中央室とにそれぞれ品位の異なる原料炭を充填し、
仕切板が介在しない状態においてこれを圧縮層成する製
造方法を提供するものである。
In this invention, the inside of the mold for forming coal, which is coking coal, is divided into a wall side part along the wall in contact with the combustion chamber of a coke oven carbonization chamber and a central part between these two wall side parts. It is divided into corresponding partition plates, and the divided wall side chambers and central chamber are filled with different grades of coking coal, respectively.
The present invention provides a manufacturing method in which this is compressed and layered without intervening partition plates.

〔作用〕[Effect]

成形型の仕切板によって画成された壁側室と中央室とに
、それぞれ互に品位の異なる原料炭を充填し、充填され
たこの原料炭を圧縮することにより、品位側に層状をな
す圧縮成形炭を得ることができる。
The wall side chamber and the central chamber, which are defined by the partition plate of the mold, are filled with raw coal of different grades, and the filled raw coal is compressed to create compression molding that forms layers on the quality side. You can get charcoal.

〔実施例〕〔Example〕

以下、この発明を図面に基づいて説明する。第1〜4図
はこの発明の一実施例を示す図である。
The present invention will be explained below based on the drawings. 1 to 4 are diagrams showing an embodiment of the present invention.

先ず構成を説明すると、10は成形型であって、原料炭
を圧縮成形してブロック化するための金型である。この
金型10の内部は仕切板12によって壁側室11a、l
laと中央室11bとに分画されている。この壁側室1
1aと中央室11bとは、コークス炉の炭化室1の両側
にある燃焼室4にそれぞれ接する壁5に沿った壁側部1
a、1aと、この両壁側部1aの間の中央部1bとにそ
の長さ、幅、高さ等が相当するようになっている。
First, the structure will be described. Reference numeral 10 is a mold for compression molding raw coal to form blocks. The interior of this mold 10 is partitioned by a partition plate 12 into wall-side chambers 11a, l.
la and a central chamber 11b. This wall side room 1
1a and the central chamber 11b are wall side portions 1 along the walls 5 that are in contact with the combustion chambers 4 on both sides of the coking chamber 1 of the coke oven.
a, 1a and the central portion 1b between the two wall side portions 1a in terms of length, width, height, etc.

13a、13bは原料炭の貯炭槽であって、13aと1
3bには互に品位の異なる石炭が貯炭されている。14
はホッパ、15はこのホッパを開閉するゲートダンパで
ある。16は押圧板であって、金型11内へ装入された
石炭を横方向から押圧してブロック化するとともに、こ
のブロック化された成形炭を受台17へ押し出すもので
ある。
13a and 13b are coal storage tanks for raw coal, and 13a and 1
Coal of different grades is stored in 3b. 14
1 is a hopper, and 15 is a gate damper that opens and closes this hopper. Reference numeral 16 denotes a pressing plate that presses the coal charged into the mold 11 from the side to form blocks, and also pushes out the formed coal blocks to the pedestal 17.

次に作用を説明する。Next, the action will be explained.

貯炭槽13a、13aには劣質炭を、貯炭槽13bには
良質炭が貯炭されている。
Poor quality coal is stored in the coal storage tanks 13a, 13a, and high quality coal is stored in the coal storage tank 13b.

金型10とホッパ14は仕切板12によって第1図に示
すように、壁側室11aと中央室11bとに分画する。
The mold 10 and the hopper 14 are divided into a wall chamber 11a and a central chamber 11b by a partition plate 12, as shown in FIG.

次に貯炭槽13a、13bから分画されたホッパ14内
へ上記原料炭を品位側に入れ、ゲートダンパ15を開く
と、劣質炭は壁側室11a、11aへ、良質炭は中央室
11bへそれぞれ装入される。次いで、仕切板12を引
き上げた後、押圧板16を第2図において右方へ駆動す
ると、前記互に品位の異なる原料炭は層別されたまま押
圧されてブロック化した圧縮成形炭M、となる。
Next, the raw coal is put into the hopper 14 separated from the coal storage tanks 13a and 13b on the high quality side, and when the gate damper 15 is opened, the poor quality coal goes into the wall side chambers 11a and 11a, and the high quality coal goes into the central chamber 11b. charged. Next, after pulling up the partition plate 12, the press plate 16 is driven to the right in FIG. Become.

次に、正規な形状となった成形炭M、を第2図における
金型10の右端部に残したまま、押圧板16を作動し、
仕切板12を下降させて、再び壁側室11aと中央室1
1bを画成する(第2図(a)参照)。次いでゲートダ
ンパ15を開とし、前回と同様に品位の異なる原料炭を
それぞれ壁側室■la、中央室11bへ装入し、装入が
終了したら仕切板I2を再び引き上げ、しかる後に押圧
板16を右動すると、前回の成形炭M1と押圧板16と
の間で原料炭は圧縮されてM+ と同様に層成された成
形炭M2となる(第2図(b)参照)。次いで成形炭M
、は受台17へ押出され、成形炭M2は金型10の右端
部に残される(第2図(C)参照)。
Next, the pressing plate 16 is operated while leaving the briquette M, which has become the regular shape, at the right end of the mold 10 in FIG.
Lower the partition plate 12 to separate the wall side chamber 11a and the central chamber 1 again.
1b (see FIG. 2(a)). Next, the gate damper 15 is opened, and raw coals of different grades are charged into the wall side chamber 1a and the central chamber 11b, respectively, as in the previous case. When the charging is completed, the partition plate I2 is pulled up again, and then the press plate 16 is When it moves to the right, the raw coal is compressed between the previous briquette M1 and the press plate 16, and becomes briquette M2 which is stratified in the same way as M+ (see FIG. 2(b)). Next, briquette M
, is extruded to the pedestal 17, and the briquette M2 is left at the right end of the mold 10 (see FIG. 2(C)).

以下、上記操作を繰返す、ことにより、層成されてブロ
ック化した成形炭を連続的に製造することができる。そ
の後、コークス炉幅に応じた所定の寸法に切断して炭化
室l内へ装入される。
Thereafter, by repeating the above-mentioned operation, stratified and block-shaped briquette coal can be continuously produced. Thereafter, it is cut into a predetermined size according to the width of the coke oven and charged into the carbonization chamber l.

次に、本実施例によって製造された成形炭によるコーク
スの品質改善結果について説明する。このコークスを室
炉試験炉(炉幅40cm、装入量250に+r)へ装入
し、乾留温度1150℃で乾留してコークス性状を調べ
たものである。
Next, the results of improving the quality of coke using the briquette produced according to this example will be explained. This coke was charged into an indoor furnace test furnace (furnace width: 40 cm, charge amount: 250 + r), and carbonized at a carbonization temperature of 1150° C. to examine coke properties.

表−1装入原料の性状 表−1は原料炭の性状を示し、第3図は上記コークスの
引張強度の試験結果を、第4図はマイクロストレングス
の試験結果をそれぞれ示したものである。第3゜4図か
ら単一原料Aに比べて品位別に層成した分割原料Bは引
張強度と同様にマイクロ強度も炭中側(中央部1b)が
改善されてコークス全体として均一化されている。
Table 1 Properties of Charged Raw Materials Table 1 shows the properties of the coking coal, FIG. 3 shows the test results for the tensile strength of the coke, and FIG. 4 shows the test results for the microstrength. Figure 3.4 shows that compared to the single raw material A, the split raw material B, which is stratified by grade, has improved micro strength as well as tensile strength in the middle part of the coal (center part 1b) and is made more uniform throughout the coke. .

〔発明の効果〕〔Effect of the invention〕

以上説明したように、この発明においては、その構成を
、原料炭を成形するための成形型内を、炭化室の燃焼室
に接する壁に沿った壁側部と、この両方の壁側部の間の
中央部とにそれぞれ相当するごとく仕切板で分画し、画
成された壁側室と中央室とにそれぞれ品位の異なる原料
炭を充填し、これを圧縮層成する製造方法としたために
、壁側に低品位炭を装入しても乾留温度が高く加熱速度
が大きくなるため、コークス品質の低下は小さく、また
炭中側(中央部)に高品位炭を装入して圧縮成形炭にし
ているため、乾留温度が低く加熱速度が小さくても均質
化されたバラツキの小さい良質のコークスを製造できる
という効果が得られる。
As explained above, in the present invention, the inside of the mold for forming coking coal is divided into a wall side part along the wall in contact with the combustion chamber of the coking chamber, and a wall side part of both of these wall sides. The manufacturing method is to divide the raw coal into sections corresponding to the central part between the two using partition plates, fill the wall side chambers and the central chamber with coking coal of different grades, and stratify the coal by compression. Even if low-grade coal is charged on the wall side, the carbonization temperature is high and the heating rate is high, so the deterioration in coke quality is small, and high-grade coal is charged on the inside (center) side of the coal to produce compression-molded coal. Therefore, even if the carbonization temperature is low and the heating rate is low, it is possible to produce high-quality coke that is homogenized and has small variations.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明に係る実施例の断面図、第2図は第1図
におけるA−A断面図であって、その(al、 fb)
、 fc1図は成形炭製造法の各工程の説明図、第3.
4図は本実施例によって製造された成形炭を原料とする
コークスの品質の説明図、第5図は従来例の説明図であ
る。 1・・・・・・炭化室、1a・・・・・・壁側部、■b
・・・用中央部、4・・・・・・燃焼室、5・・・・・
・壁、1o・・・・・・成形型、Ila・・・・・・壁
側室、llb・・・・・・中央室、12・・・・・・仕
切板特許出願人  川崎製鉄株式会社 代理人 弁理士 森   哲 也 代理人 弁理士 内 藤 嘉 昭 代理人 弁理士 清 水   正 2  第3図 ; 第4図
FIG. 1 is a sectional view of an embodiment according to the present invention, and FIG. 2 is a sectional view taken along line A-A in FIG.
, fc1 is an explanatory diagram of each step of the briquette manufacturing method, and 3.
FIG. 4 is an explanatory diagram of the quality of coke made from the briquette coal produced according to this embodiment, and FIG. 5 is an explanatory diagram of the conventional example. 1...Carbonization chamber, 1a...Wall side part, ■b
...Central part, 4...Combustion chamber, 5...
・Wall, 1o...Mold, Ila...Wall side chamber, llb...Central chamber, 12...Partition plate Patent applicant Kawasaki Steel Co., Ltd. agent Person Patent attorney Tetsuya Mori Agent Patent attorney Yoshiaki Naito Attorney Patent attorney Masaaki Shimizu 2 Figure 3; Figure 4

Claims (1)

【特許請求の範囲】[Claims] コークス炉用の原料炭を成形型内へ充填し、該原料炭を
圧縮して成形する圧縮成形炭の製造方法において、前記
成形型内を前記コークス炉炭化室の燃焼室に接する壁に
沿った壁側部と中央部とにそれぞれ相当するごとく仕切
板で分割し、分割して画成された壁側室と中央室とにそ
れぞれ品位の異なる原料炭を充填し、充填した原料炭を
、前記仕切板が介在しない状態において圧縮層成するこ
とを特徴とする圧縮成形炭の製造方法。
In a method for producing compressed briquette coal in which coking coal for a coke oven is filled into a mold, and the coking coal is compressed and molded, the interior of the mold is lined along a wall in contact with a combustion chamber of the coke oven carbonization chamber. The wall side chamber and the central chamber are divided by a partition plate so as to correspond to the wall side portion and the central portion, respectively, and raw coal of different grades is filled into the divided wall side chamber and the central chamber. A method for producing compression briquette coal, characterized by carrying out compression stratification without intervening plates.
JP22902685A 1985-10-15 1985-10-15 Production of compressively formed coal Pending JPS6289792A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22902685A JPS6289792A (en) 1985-10-15 1985-10-15 Production of compressively formed coal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22902685A JPS6289792A (en) 1985-10-15 1985-10-15 Production of compressively formed coal

Publications (1)

Publication Number Publication Date
JPS6289792A true JPS6289792A (en) 1987-04-24

Family

ID=16885582

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22902685A Pending JPS6289792A (en) 1985-10-15 1985-10-15 Production of compressively formed coal

Country Status (1)

Country Link
JP (1) JPS6289792A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2503752A (en) * 2012-07-05 2014-01-08 Midpit Pty Ltd Split colour manufacture of lawn bowling balls

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2503752A (en) * 2012-07-05 2014-01-08 Midpit Pty Ltd Split colour manufacture of lawn bowling balls

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