JPH078985B2 - Method of charging raw material into coke oven - Google Patents
Method of charging raw material into coke ovenInfo
- Publication number
- JPH078985B2 JPH078985B2 JP5627287A JP5627287A JPH078985B2 JP H078985 B2 JPH078985 B2 JP H078985B2 JP 5627287 A JP5627287 A JP 5627287A JP 5627287 A JP5627287 A JP 5627287A JP H078985 B2 JPH078985 B2 JP H078985B2
- Authority
- JP
- Japan
- Prior art keywords
- charging
- raw material
- furnace
- coke oven
- bulk density
- 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.)
- Expired - Lifetime
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Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は、室炉式コークス炉でコークスを製造するに際
し、炉内の不均一乾留を改善できるコークス炉への原料
装入方法に関するものである。Description: TECHNICAL FIELD The present invention relates to a method for charging a raw material into a coke oven, which can improve non-uniform carbonization in the oven during the production of coke in a chamber coke oven. is there.
(従来の技術及びその問題点) 室炉式コークス製造法は周知のとおり、第6図に示すよ
うに通常4〜5個所の装入口1より装炭車を介して原料
炭(以下「原料」と略称する)2を炉上から炭化室3へ
落下装入し、炭化室3の両側の燃焼室からレンガ壁を通
して加熱し、コークスを製造する方法であるが、この方
法で製造されるコークスは炭化室3の炉長、炉高、炉幅
の3方向で大きな品質偏差、乾留温度偏差のあることが
知られている。(Prior art and its problems) As is well known in the chamber furnace coke manufacturing method, as shown in FIG. 6, coking coal (hereinafter referred to as “raw material”) is usually supplied from 4 to 5 charging ports 1 through a car. (Abbreviated) 2 is dropped into the carbonization chamber 3 from above the furnace and heated from the combustion chambers on both sides of the carbonization chamber 3 through brick walls to produce coke. The coke produced by this method is carbonized. It is known that there are large quality deviations and carbonization temperature deviations in the three directions of the furnace length, furnace height and furnace width of the chamber 3.
近時コークス炉の乾留効率化とコークス品質の安定化が
重要視されているに伴い、上記コークス炉内の品質およ
び乾留温度偏差の改善が大きな課題となっている。Along with the recent importance placed on improving the efficiency of carbonization of a coke oven and stabilizing the quality of coke, improvement of the quality of the coke oven and the deviation of the temperature of carbonization have become major issues.
これらの偏差原因の一つは、炉内に装入される原料が炉
長、炉高方向に極めて大きな嵩密度偏差を有することに
ある。すなわち一般的に言えば、炉高方向の偏差は炉の
下部に比較して炉上部の嵩密度が低く、炉長方向には装
入口直下に比較して装入口間および窯口部の嵩密度が低
い傾向にある。一例として本発明者らの調査では、平均
数密度735kg/m3の場合で約±50kg/m3もの大きな偏差を
有することが確認されている。このような装入原料の炉
内における嵩密度偏差は、当然のことながらコークス品
質のみならず乾留温度の偏差となって、コークス品質の
安定化を阻害するばかりでなく乾留効率の低下を招くこ
とになる。したがって装入原料を炉内に均一に装入する
技術の開発が極めて重要な課題となってきている。One of the causes of these deviations is that the raw material charged into the furnace has an extremely large bulk density deviation in the furnace length and furnace height directions. That is, generally speaking, the deviation in the furnace height direction is lower in the bulk density in the upper part of the furnace than in the lower part of the furnace, and in the furnace length direction, the bulk density between the charging ports and in the kiln port is lower than that just below the charging port. Is low. In the present inventors' investigation as an example, it has been confirmed to have about ± 50 kg / m 3 things large deviations in the case of the average number density 735kg / m 3. The deviation of the bulk density of the charging raw material in the furnace naturally causes not only the coke quality but also the carbonization temperature deviation, which not only hinders the stabilization of the coke quality but also causes the reduction of the carbonization efficiency. become. Therefore, the development of a technique for uniformly charging the charging raw material into the furnace has become an extremely important issue.
こうした背景から、近年装入原料の嵩密度偏差を改善す
る方法がいくつか提案され開示されている。例えば炉の
上部における装入原料の嵩密度を向上する方法として、
特公昭59−18434号公報、同59−18435号公報、同59−18
437号公報が開示されている。これら公報に開示された
発明は、炉内に装入された原料の上面を加圧、加振機構
を備えたレベラーを用いて圧密することにより装入原料
の上部嵩密度を向上する方法である。しかし、これらの
方法では加振による炉壁レンガの目地切れや損傷が懸念
され、長期間継続使用できる技術かどうか疑問がある。
さらに加振による嵩密度改善効果が上部1〜2mに限定さ
れ、炉内の嵩密度偏差を全面的に改善するには十分とは
言えない。Against this background, some methods have recently been proposed and disclosed for improving the bulk density deviation of the charging raw material. For example, as a method of improving the bulk density of the charging material in the upper part of the furnace,
JP-B-59-18434, 59-18435, 59-18
Japanese Patent No. 437 is disclosed. The inventions disclosed in these publications are methods for improving the upper bulk density of the charged raw material by pressing and consolidating the upper surface of the raw material charged in the furnace using a leveler equipped with a vibrating mechanism. . However, with these methods, there is a concern that the brick wall of the furnace wall may be broken or damaged due to vibration, and it is doubtful whether the technique can be used continuously for a long time.
Furthermore, the effect of improving the bulk density by vibration is limited to the upper part of 1 to 2 m, which is not sufficient to completely improve the deviation of the bulk density in the furnace.
また、装入原料を高速装入することにより嵩密度の向上
と嵩密度偏差の改善が図られることから、装炭車と装入
口との間に対向するベルトを設置して装入原料を加速さ
せて高速装入を達成する方法も例えば特開昭59−122582
号公報に提案され開示されている。Further, since the bulk density and the bulk density deviation can be improved by charging the charging raw material at a high speed, an opposing belt is installed between the coal charging vehicle and the charging inlet to accelerate the charging raw material. A method for achieving high-speed charging by means of, for example, JP-A-59-122582
It is proposed and disclosed in Japanese Patent Publication No.
この特開昭59−122582号公報に開示された方法は、高速
装入の有効な手段と考えられるものの、装炭車の大幅な
改善を必要とするばかりでなく対向ベルトによる巻込み
空気のためキャリーオーバーの増大を招くおそれがあ
り、実用上解決すべき課題も多いと推定される。Although the method disclosed in Japanese Patent Application Laid-Open No. 59-122582 is considered to be an effective means for high-speed charging, it not only requires a significant improvement of the coal car but also carries air due to the air entrained by the opposing belt. It is presumed that there are many problems that need to be solved in practice, as this may lead to an increase in overload.
このように嵩密度偏差改善対策としての公知方法には実
用上必ずしも十分なものとは言えないのが現状である。As described above, at present, it cannot be said that the known method for improving the bulk density deviation is practically sufficient.
本発明者らはこうした背景を踏まえ、従来のコークス炉
への原料装入法のどこに問題があるのかを明らかにする
ため、装入中の原料が炭化室内で示す挙動についてアク
リル模型を使って調査した。その結果、第6図に示すよ
うに、原料2を炭化室3に装入しはじめると炭化室3内
の残留気体(空気)は装入原料2によって排除され、第
6図に破線矢印で示す如く上昇流となって装入原料2の
流れとは逆に装入口1および上昇管4の方へ流れること
を確認した。当然のことながらこの排除される気体は微
粉の原料(粉じん)を随伴するため、実操業のコークス
炉では発じん対策として上昇管および各装入口から炭化
室内の気体を装入中に吸引処理している。Based on such a background, the present inventors investigated the behavior of the raw material during charging in the carbonization chamber using an acrylic model in order to clarify where the problem is in the conventional method for charging the raw material into the coke oven. did. As a result, as shown in FIG. 6, when the raw material 2 begins to be charged into the carbonization chamber 3, the residual gas (air) in the carbonization chamber 3 is removed by the charged raw material 2 and is shown by a dashed arrow in FIG. As a result, it was confirmed that the flow became an upward flow and flowed toward the charging port 1 and the rising pipe 4 contrary to the flow of the charging raw material 2. As a matter of course, this removed gas is accompanied by a fine powder raw material (dust), so in a coke oven in an actual operation, suction treatment is performed during charging of the gas in the carbonization chamber from the riser and each inlet as a dust countermeasure. ing.
ここで重要なことは、装入口で炭化室内の気体を吸引処
理すれば、第7図に示す実操業コークス炉の装入口1ま
わりの模式図から理解されるとおり、装入中の原料2は
炭化室3内から上昇してくる気体により浮力を受け装入
速度を減ずるため、結果的に装入嵩密度の低下と嵩密度
偏差を助長する要因になっていることが指摘された。What is important here is that if the gas in the carbonization chamber is suctioned at the charging port, as can be understood from the schematic diagram around the charging port 1 of the actual coke oven shown in FIG. It was pointed out that the gas rising from the inside of the carbonization chamber 3 receives buoyancy and reduces the charging speed, resulting in a decrease in the charging bulk density and an increase in the bulk density deviation.
なお、第7図中5は給炭ホッパー、6はテーブルフィー
ダ、7は補助ホッパー、8は給炭内筒、9は移動フリー
ブ、10は集じんフードである。In FIG. 7, 5 is a coal feeding hopper, 6 is a table feeder, 7 is an auxiliary hopper, 8 is a coal feeding inner cylinder, 9 is a moving fleece, and 10 is a dust collecting hood.
本発明はかかる問題点に鑑みて成されたものであり、コ
ークス炉内の不均一乾留を改善するために、不均一乾留
の一つの原因である炭化室内における装入原料の嵩密度
偏差を解消できるコークス炉への原料装入方法を提供す
るものである。The present invention has been made in view of such problems, and in order to improve the non-uniform carbonization in the coke oven, eliminate the bulk density deviation of the charging raw material in the carbonization chamber is one cause of the non-uniform carbonization The present invention provides a method for charging a raw material into a coke oven.
(問題点を解決するための手段) 本発明は、室炉式コークス炉へ原料を装入する方法にお
いて、前記コークス炉に設けられた複数の装入口に加え
てこれら装入口間及び窯口側炉上に適宜の開口を設置
し、装入口からの原料装入時に前記開口より炉内の気体
及びこれに隋伴する粉塵を吸引処理することを要旨とす
るコークス炉への原料装入方法である。(Means for Solving Problems) The present invention relates to a method for charging a raw material into a chamber furnace type coke oven, in addition to a plurality of inlets provided in the coke oven, between these inlets and a kiln side. A method for charging a raw material into a coke oven, in which an appropriate opening is installed on the furnace, and the gas in the furnace and dust accompanying it are sucked through the opening when charging the raw material from the charging port. is there.
すなわち、本発明は装入嵩密度の向上と嵩密度偏差の改
善に効果のある高速装入を達成する方法であり、前記し
た本発明者らが実験で得た知見に基づき、原料装入によ
って排除される炭化室内の気体が装入原料に与える浮力
の影響を取り除く方法として発明されたものである。That is, the present invention is a method for achieving high-speed charging effective in improving the charging bulk density and improving the bulk density deviation, and based on the findings obtained by the inventors of the present invention through experiments, by charging raw materials. It was invented as a method for removing the influence of buoyancy exerted on the charging raw material by the gas in the carbonization chamber to be eliminated.
(実 施 例) 以下、本発明方法を第1図及び第2図に示す一実施例に
基づいて説明する。なお、第1図及び第2図中、第6図
及び第7図と同一番号は同一部分あるいは相当部分を示
し詳細な説明を省略する。(Example) Hereinafter, the method of the present invention will be described based on an example shown in FIGS. 1 and 2. In FIGS. 1 and 2, the same reference numerals as those in FIGS. 6 and 7 indicate the same or corresponding parts, and detailed description thereof will be omitted.
第1図は本発明を示す概略図であるが、前記した第1図
と比較して理解されるとおり、本発明方法は従来の装入
口1での集じんに代え、装入口1と装入口1との間に設
けた炉上の開口11および窯口側に設けた炉上の開口12よ
り集じんするのである。FIG. 1 is a schematic view showing the present invention, but as will be understood by comparing with FIG. 1 described above, the method of the present invention replaces the conventional dust collection at the loading inlet 1 with the loading inlet 1 and the loading inlet. The dust is collected from the opening 11 on the furnace provided between the opening 1 and the opening 1 on the kiln.
従って、原料装入によって排除される気体は、装入原料
の流れを阻害することなく炉外に吸引処理されるため、
原料2の装入速度を向上させることが可能となる。第2
図は本発明方法を適用した場合の実操業コークス炉の装
入口まわりの模式図を示したものであるが、前記した従
来法の第7図に比較して本発明方法における原料装入中
の集じん方法の差が良く理解されよう。Therefore, the gas removed by charging the raw material is sucked out of the furnace without disturbing the flow of the charged raw material.
It is possible to improve the charging speed of the raw material 2. Second
The figure shows a schematic diagram around the charging port of an actual coke oven when the method of the present invention is applied. Compared with FIG. 7 of the conventional method described above, during the charging of raw materials in the method of the present invention, The difference in dust collection method will be well understood.
さらに言えば、従来の原料装入方法では前述したよう
に、原料装入によって排除される炭化室3内の気体が装
入口1を通って炉外に流出する場合、装入口1が絞られ
ているため装入原料に逆行して流れる炉内気体は流速が
大となって装入中の原料2の一部を巻き込んで炉外に出
る。そのために発じん量は多くなるが、本発明方法では
炉内気体の流れが装入口1を通らないため発じん量は大
幅に低下するという効果がある。Furthermore, in the conventional raw material charging method, as described above, when the gas in the carbonization chamber 3 removed by the raw material charging flows out of the furnace through the charging port 1, the charging port 1 is narrowed. Because of this, the gas in the furnace that flows counter to the charged raw material has a high flow velocity and entrains a part of the raw material 2 being charged and goes out of the furnace. Therefore, the amount of dust generated is large, but the method of the present invention has an effect that the amount of dust is significantly reduced because the gas flow in the furnace does not pass through the charging port 1.
次に本発明方法を実施した結果にもとづいて説明する。Next, description will be given based on the results of carrying out the method of the present invention.
コークス炉の炭化室寸法が高さ7.125m、炉幅467mm、長
さ16.5mの実操業の炉長のみ1/2とした鋼性模型炉を製作
し、実操業炉の炉団の端に設計し、本発明方法の効果を
確認する原料挿入実験を実施した。鋼性模型炉の概略
は、第3図に示すとおりで、装入原料の崇高度を測定す
るために、サンプリング孔13を炉底より0.75、1.5、
3、4、5、6mの位置6点について、また炉長方向には
2つの装入口1直下および装入口1と窯口まで2点、装
入口1と装入口1との間2点の計36孔設置した。また、
模型炉には通常の装入口2ケ所の他に装入口1と装入口
1との間および窯口側の炉上に開口11、12を設け、原料
の装入は通常の装炭車より行った。A coke oven with a height of 7.125 m, a furnace width of 467 mm, and a length of 16.5 m was used to manufacture a steel model furnace with half the length of the actual furnace and designed at the end of the furnace group of the actual furnace. Then, a raw material insertion experiment was conducted to confirm the effect of the method of the present invention. The outline of the steel model furnace is as shown in Fig. 3, and in order to measure the altitude of the charged raw material, the sampling hole 13 was opened from the bottom of the furnace at 0.75, 1.5,
There are 6 points at 3, 4, 5 and 6 m, and 2 points directly below the two inlets 1 in the furnace length direction, up to the inlet 1 and the kiln, and 2 points between the inlet 1 and the inlet 1. 36 holes were installed. Also,
In the model furnace, in addition to the two normal charging ports, openings 11 and 12 were provided between the charging port 1 and the charging port 1 and on the furnace side of the kiln, and the charging of raw materials was carried out by a normal coal car. .
実験は通常操業の配合炭(原料粒度3mm以下、83重量
%、全水分9.2重量%)を用い、本発明方法による装入
口1での集じんに加え、炉上に設けた各開口11、12より
集じんしながら原料を装入した。なお比較として炉上の
開口11、12を密閉し、従来方法どおり装入口1から集じ
んしながら原料を装入した。The experiment was carried out by using normally operated blended coal (raw material particle size of 3 mm or less, 83% by weight, total water content of 9.2% by weight), in addition to the dust collection at the charging port 1 according to the method of the present invention, the openings 11 and 12 provided on the furnace. The raw materials were charged while collecting more dust. For comparison, the openings 11 and 12 on the furnace were closed, and the raw material was charged while collecting dust from the charging port 1 as in the conventional method.
各実験毎に各サンプリング孔13から所定体積中の原料を
ドリルサンプリングし、重量測定後嵩密度を算出した。
また、原料の装入中に集じんダクトよりガスサンプリン
グし、ガス中のダスト量を測定した。The raw material in a predetermined volume was drill-sampled from each sampling hole 13 for each experiment, and the bulk density was calculated after the weight measurement.
Further, gas sampling was performed from the dust collection duct during charging of the raw materials, and the amount of dust in the gas was measured.
この結果は、まず第4図に示すとおり、炉底より1.5m位
置における炉長方向の嵩密度は、従来方法(●印)に比
較して本発明方法(○印)が高く、かつ、装入口直下と
窯口または装入口間の嵩密度差も本発明方法が小さく有
効な方法であると理解されよう。また第5図に示すとお
り、装入口直下における炉高方向の嵩密度も、従来方法
(●印)に比較して本発明方法(○印)が高く、かつ嵩
密度偏差も本発明方法が小さいと理解されよう。これら
の結果の要点を下記表に示すが、本発明方法は従来方法
より数密度で約25kg/m3向上し嵩密度偏差で約15kg/m3の
低減が図られ、かつ発じん量も約4割に低減するなど極
めて有効な方法であることが明らかである。This result shows that, as shown in FIG. 4, the bulk density in the furnace length direction at the position 1.5 m from the bottom of the furnace is higher in the method of the present invention (○) than in the conventional method (●), and It will be understood that the difference in bulk density between directly below the inlet and the kiln or charging port is also a small and effective method of the present invention. Further, as shown in FIG. 5, the bulk density in the furnace height direction just below the charging port is higher in the method of the present invention (marked with ○) than in the conventional method (marked with ●), and the deviation of the bulk density is also small in the method of the present invention. It will be understood. Shows the point of these results in the following Table, the present method reduces to about 15 kg / m 3 at about 25 kg / m 3 increase the number density than conventional methods bulk density deviation is achieved, and particle emissions amount about It is clear that this is an extremely effective method, such as reducing it to 40%.
(発明の効果) 以上説明したように本説明方法は、室炉式コークス炉へ
原料を装入する方法において、前記コークス炉に設けら
れた複数の装入口に加えてこれら装入口間及び窯口側炉
上に適宜の開口を設置し、装入口からの原料装入特に前
記開口より炉内の気体及びこれに隋伴する粉塵を吸引処
理するものである為、原料が装入速度が向上し、結果と
して装入嵩密度の向上と装入嵩密度偏差を改善できる。
また、本発明方法によれば流出してくる残留空気が隋伴
する粉じん量も大幅に低減できる。これらの効果は、コ
ークス品質の改善安定、均一乾留に有効であるばかりで
なく、集じん効率を改善にもつながる。 (Effects of the Invention) As described above, the present description method is a method for charging a raw material into a chamber furnace type coke oven, in addition to the plurality of inlets provided in the coke oven, between these inlets and the kiln port. An appropriate opening is installed on the side furnace, and the charging of the raw material from the charging inlet is particularly performed by suctioning the gas in the furnace and dust accompanying it from the opening, so the charging speed of the raw material is improved. As a result, it is possible to improve the charging bulk density and the charging bulk density deviation.
Further, according to the method of the present invention, the amount of dust that accompanies the residual air flowing out can be greatly reduced. These effects are not only effective for improving the stability of the coke quality and uniform dry distillation, but also improve the dust collection efficiency.
第1図は本発明方法の概略説明図、第2図は本発明方法
を適用した場合の実操業コークス炉の装入口まわりの模
式図、第3図は本発明方法の実験設備の説明図、第4図
は炭化室の各部における装入原料の嵩密度の実験結果を
示す図、第5図は炉底からの高さの変化による嵩密度の
実験結果図、第6図及び第7図は従来方法の第1図及び
第2図と同様の図である。 1は装入口、2は原料、3は炭化室、11、12は開口。FIG. 1 is a schematic explanatory view of the method of the present invention, FIG. 2 is a schematic diagram around a charging port of an actual operating coke oven when the method of the present invention is applied, and FIG. 3 is an explanatory view of experimental equipment of the method of the present invention, FIG. 4 is a diagram showing an experimental result of the bulk density of the charging raw material in each part of the carbonization chamber, FIG. 5 is an experimental result diagram of the bulk density due to a change in height from the furnace bottom, and FIGS. 6 and 7 are FIG. 3 is a view similar to FIGS. 1 and 2 of a conventional method. 1 is a charging port, 2 is a raw material, 3 is a carbonization chamber, and 11 and 12 are openings.
Claims (1)
おいて、前記コークス炉に設けられた複数の装入口に加
えてこれら装入口間及び窯口側炉上に適宜の開口を設置
し、装入口からの原料装入時に前記開口より炉内の気体
及びこれに隋伴する粉塵を吸引処理することを特徴とす
るコークス炉への原料装入方法。1. A method for charging a raw material into a chamber furnace type coke oven, wherein in addition to a plurality of inlets provided in the coke oven, appropriate openings are provided between these inlets and on the kiln side furnace. A method for charging a raw material into a coke oven, wherein a gas in the furnace and dust accompanying it are sucked from the opening when charging the raw material from the charging port.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5627287A JPH078985B2 (en) | 1987-03-11 | 1987-03-11 | Method of charging raw material into coke oven |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5627287A JPH078985B2 (en) | 1987-03-11 | 1987-03-11 | Method of charging raw material into coke oven |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63223088A JPS63223088A (en) | 1988-09-16 |
| JPH078985B2 true JPH078985B2 (en) | 1995-02-01 |
Family
ID=13022453
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5627287A Expired - Lifetime JPH078985B2 (en) | 1987-03-11 | 1987-03-11 | Method of charging raw material into coke oven |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH078985B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP7715109B2 (en) * | 2022-09-21 | 2025-07-30 | Jfeスチール株式会社 | Manufacturing method and manufacturing device for blast furnace raw materials |
| JP7700764B2 (en) * | 2022-09-30 | 2025-07-01 | Jfeスチール株式会社 | Apparatus and method for producing raw materials for blast furnaces |
| JP7743827B2 (en) * | 2022-10-11 | 2025-09-25 | Jfeスチール株式会社 | Blast furnace raw material manufacturing device and blast furnace raw material manufacturing method |
-
1987
- 1987-03-11 JP JP5627287A patent/JPH078985B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63223088A (en) | 1988-09-16 |
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