JP2880766B2 - Coal charging method for coke oven - Google Patents

Coal charging method for coke oven

Info

Publication number
JP2880766B2
JP2880766B2 JP2142872A JP14287290A JP2880766B2 JP 2880766 B2 JP2880766 B2 JP 2880766B2 JP 2142872 A JP2142872 A JP 2142872A JP 14287290 A JP14287290 A JP 14287290A JP 2880766 B2 JP2880766 B2 JP 2880766B2
Authority
JP
Japan
Prior art keywords
coal
pressure
charging
coke oven
furnace
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
Application number
JP2142872A
Other languages
Japanese (ja)
Other versions
JPH0436385A (en
Inventor
田中  均
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 JP2142872A priority Critical patent/JP2880766B2/en
Publication of JPH0436385A publication Critical patent/JPH0436385A/en
Application granted granted Critical
Publication of JP2880766B2 publication Critical patent/JP2880766B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B41/00Safety devices, e.g. signalling or controlling devices for use in the discharge of coke
    • C10B41/005Safety devices, e.g. signalling or controlling devices for use in the discharge of coke for charging coal

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Coke Industry (AREA)

Description

【発明の詳細な説明】 <産業上の利用分野> 本発明は、コークス炉への石炭装入方法に関する。The present invention relates to a method for charging coal into a coke oven.

<従来の技術> コークス炉10では、一般に第6図に示すように原料の
石炭を装入する方法として装入車1のホッパー2に積込
まれた石炭を、コークス炉10炉頂部に設けた4あるいは
5個の装入口11(第6図では4個)から重力落下により
炭化室12へ装入する方法がとられている。
<Conventional Technology> In a coke oven 10, as shown in FIG. 6, as a method for charging coal as a raw material, coal loaded in a hopper 2 of a charging vehicle 1 is generally provided at the top of the coke oven 10. In this method, four or five charging ports 11 (four in FIG. 6) are charged into the carbonization chamber 12 by gravity.

また、石炭装入時に発生する粉塵、ガスは、装入車集
塵機3により集塵される一方、上昇管ベンド部4での高
圧安水4aによるエゼクター効果により上昇管側へ吸引さ
れる。
Dust and gas generated at the time of charging coal are collected by the charged vehicle dust collector 3, while being sucked to the riser tube side by the ejector effect of the high-pressure water 4a in the riser tube bend unit 4.

しかし、石炭の装入初期は石炭の落下距離が長く、か
つ終速が速くなり、また装入末期はガスの発生量が増大
する。これらの影響で、第7図に示すように炭化室12内
圧力(以下、炉内圧という)は大きく変動し、上記集塵
方法のみでは炉外への粉塵、ガスの漏洩を防止すること
は困難であった。
However, in the early stage of charging coal, the falling distance of the coal is long and the final speed is fast, and the amount of generated gas increases in the last stage of charging. Due to these effects, as shown in FIG. 7, the pressure inside the carbonization chamber 12 (hereinafter referred to as furnace pressure) fluctuates greatly, and it is difficult to prevent dust and gas from leaking out of the furnace only by the above dust collection method. Met.

<発明が解決しようとする課題> 石炭装入時における粉塵、ガスの炉外への漏洩および
炉内圧の下がりすぎによる空気の炉内への侵入を防止す
る方法として、特公昭60−6387号が提案されている。こ
の方法は、上昇管ベンド部におけるエゼクター効果を調
節し常に適正な炉内圧に維持するものであり、この方法
により粉塵、ガス等の炉外への漏洩は、抑制可能であ
る。しかしながら、この方法では炉内圧上昇時に上昇管
の吸引力を高めるため、原料石炭の水分の低下時等では
石炭のキャリオーバーが増大し、タール中に石炭が混入
してタール品質を著しく悪化させることになるという問
題があった。
<Problems to be Solved by the Invention> Japanese Patent Publication No. 60-6387 discloses a method for preventing dust and gas from leaking out of the furnace at the time of coal charging and preventing air from entering the furnace due to an excessively low furnace pressure. Proposed. This method adjusts the ejector effect at the riser tube bend section to always maintain an appropriate furnace pressure. By this method, leakage of dust, gas, etc. to the outside of the furnace can be suppressed. However, in this method, the suction force of the riser tube is increased when the furnace pressure rises, so that when the water content of the raw coal decreases, the carryover of the coal increases, and the coal is mixed into the tar and significantly deteriorates the tar quality. There was a problem of becoming.

本発明は、前記問題点を解決し粉塵、ガス等の漏洩を
防止するとともにタール品質の悪化を抑制できるコーク
ス炉への石炭装入方法を提供することを目的としてい
る。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a method of charging coal into a coke oven, which solves the above problems, prevents dust and gas from leaking, and can suppress deterioration of tar quality.

<課題を解決するための手段> 本発明は、コークス炉への石炭装入時における炉内圧
の変動、石炭装入速度等を詳細に測定、解析することに
より完成された。石炭装入時に炉内圧を適正に維持する
方法として、上昇管部でのエゼクター効果を調整する方
法によらず石炭の装入速度を調整することにより炉内圧
を適正に維持し、石炭装入時の粉塵、ガスの炉外への漏
洩を防止するものである。
<Means for Solving the Problems> The present invention has been completed by measuring and analyzing the fluctuation of the furnace pressure, the charging speed of coal, and the like in detail when charging coal into a coke oven. As a method of maintaining the furnace pressure properly during coal charging, the furnace pressure is maintained properly by adjusting the coal charging speed regardless of the method of adjusting the ejector effect in the riser section. To prevent dust and gas from leaking out of the furnace.

すなわち、上記目的を達成するために本発明によれ
ば、コークス炉へ石炭を装入する際に、コークス炉の炭
化室内圧力を連続的に測定し、この測定値に基づき石炭
を装入する速度を予め定めた基準圧力と測定値を比較し
て調節し、前記炭化室内圧力を基準圧力範囲内になるよ
うに制御することを特徴とするコークス炉への石炭装入
方法が提供される。
That is, according to the present invention, in order to achieve the above object, when charging coal into a coke oven, the pressure in the carbonization chamber of the coke oven is continuously measured, and the rate at which coal is charged based on the measured value is measured. Is adjusted by comparing a measured value with a predetermined reference pressure, and the pressure in the coking chamber is controlled so as to be within a reference pressure range.

以下に本発明をさらに詳細に説明する。 Hereinafter, the present invention will be described in more detail.

第1図は、本発明を実施するための制御装置の構成の
1例を示す系統図である。
FIG. 1 is a system diagram showing an example of a configuration of a control device for implementing the present invention.

ホッパー2内の石炭は、テーブルフィーダー5の回転
により切出されて装入口11から炭化室12内へ装入され
る。
The coal in the hopper 2 is cut out by the rotation of the table feeder 5 and charged into the coking chamber 12 from the charging port 11.

6はテーブルフィーダー駆動用のモーターであり、モ
ーター6の回転数制御により、石炭の装入速度は制御さ
れる。また、7は炉内圧計測用の圧力計であり、各炭化
室12での圧力変化が連続測定され、基準圧力設定器9に
予め設定された基準圧力値との偏差に応じ石炭の装入速
度を変更するよう演算、制御用のシーケンサ8で演算さ
れ、モーター6の回転数を制御するようになっている。
Reference numeral 6 denotes a motor for driving the table feeder, and the charging speed of the coal is controlled by controlling the rotation speed of the motor 6. Reference numeral 7 denotes a pressure gauge for measuring furnace internal pressure, in which pressure changes in each of the coking chambers 12 are continuously measured, and the charging speed of coal is determined according to a deviation from a reference pressure value preset in a reference pressure setting device 9. Is changed by a calculation and control sequencer 8 to change the rotation speed of the motor 6.

前記設定器9に設定する基準圧力値は、コークス炉の
構造、集塵機能力、エゼクター効果、原料石炭の性状等
を考慮して適宜の値を設定すればよい。
The reference pressure value set in the setting unit 9 may be set to an appropriate value in consideration of the structure of the coke oven, the function of collecting dust, the ejector effect, the properties of the raw coal, and the like.

具体的に、基準圧力値の設定は、前記したようにコー
クス炉への石炭装入時における炉内圧の変動、石炭装入
速度等を詳細に測定、解析することにより、石炭装入時
の粉塵、ガスの炉外への漏洩を防止しうる値として設定
することができる。
Specifically, as described above, the setting of the reference pressure value is carried out by measuring and analyzing the fluctuation of the furnace internal pressure at the time of charging coal into the coke oven, the charging speed of coal, etc. , Can be set as a value that can prevent gas from leaking out of the furnace.

より具体的には、コークス炉の構造、集塵能力、エゼ
クター効果などが運転時と同様である条件下に、予めコ
ークス炉内へ石炭を装入して、図1に示す圧力計7によ
り炉内圧の変動を測定し、また石炭装入速度等を詳細に
測定、解析することにより、基準圧力値を設定すること
ができる。またこの際には一般的な手法を利用して原料
石炭の性状が考慮され、たとえば装入石炭の水分量と炉
内圧との関係、あるいは石炭の装入過程での炉内圧の変
化量などが測定される。
More specifically, coal is charged into the coke oven in advance under conditions where the structure, dust collection capacity, ejector effect, etc. of the coke oven are the same as during operation, and the furnace is operated by the pressure gauge 7 shown in FIG. The reference pressure value can be set by measuring the fluctuation of the internal pressure and measuring and analyzing the coal charging speed and the like in detail. At this time, the properties of the raw coal are taken into account using a general method, and for example, the relationship between the moisture content of the charged coal and the furnace pressure, or the amount of change in the furnace pressure during the coal charging process, etc. Measured.

そして、石炭装入時に炉内圧を連続的に測定し、予め
定めた基準圧力と比較し基準圧よりも高ければ石炭の装
入速度を低下させ、また低ければ石炭の装入速度を増加
させる方法を採り、炭化室内圧力(炉内圧)を基準圧力
範囲になるように制御するため、常に炉内圧を集塵機能
力範囲内に維持でき、粉塵、ガスの炉外への漏洩を防止
できるばかりか、石炭のタール中へのキャリオーバーを
抑制することができる。
Then, the furnace internal pressure is continuously measured at the time of charging coal, and the charging speed of the coal is reduced if the pressure is higher than the reference pressure compared with a predetermined reference pressure, and the charging speed of the coal is increased if the pressure is lower than the reference pressure. In order to control the pressure in the carbonization chamber (furnace pressure) within the reference pressure range, the pressure inside the furnace can always be maintained within the range of the dust collection function, preventing not only dust and gas from leaking out of the furnace, but also coal. Carryover into the tar can be suppressed.

第2図に、本発明による石炭装入速度の制御の1例を
示す。この結果、第3図に示すように石炭装入開始から
完了までの間の炉内圧は、基準圧力範囲内に保持するこ
とが可能となる。
FIG. 2 shows an example of the control of the coal charging speed according to the present invention. As a result, as shown in FIG. 3, the furnace pressure from the start to the completion of coal charging can be maintained within the reference pressure range.

<実施例> 以下に本発明を実施例に基づき具体的に説明する。<Example> Hereinafter, the present invention will be specifically described based on examples.

(実施例1) 第1図に示す制御装置を用い、1回の石炭装入量30t
(水分8.0%)、基準圧力範囲5〜15mmH2Oにてコークス
を製造した。連続11日間のガス洩れ率および石炭のター
ル中へのキャリオーバー量は、それぞれ第4図および第
5図のとおり(○印)で従来法による値(●印)に比
べ、どちらも大幅に低減された。
(Example 1) Using the control device shown in Fig. 1, the amount of coal charged at one time is 30t.
(8.0% moisture), it was produced coke in the reference pressure range 5~15mmH 2 O. The gas leakage rate and the carryover amount of coal into tar for 11 consecutive days were significantly reduced as compared with the values obtained by the conventional method (●), as shown in Fig. 4 and Fig. 5 (○). Was done.

<発明の効果> 本発明は、以上説明したように構成されているので、
石炭の装入時に炉内圧を測定し、その結果に基づき石炭
の装入速度調整を行なう方法であるため、窯による炉内
圧レベルの差異等に関係なく、常に適正な炉内圧に制御
でき、粉塵、ガス等の炉外への漏洩を防止できるでけで
なく、他の方法に比べ、石炭のキャリオーバーによるタ
ールの品質悪化も抑制できる。
<Effects of the Invention> Since the present invention is configured as described above,
Since the furnace pressure is measured at the time of charging coal and the charging speed is adjusted based on the results, the furnace pressure can always be controlled to an appropriate level regardless of the difference in furnace pressure level between kilns. In addition, it is possible not only to prevent gas and the like from leaking out of the furnace, but also to suppress deterioration of tar quality due to coal carryover as compared with other methods.

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

第1図は、本発明を実施するための制御装置の構成の1
例を示す系統図である。 第2図は、本発明による石炭装入速度の制御の1例を示
すグラフである。 第3図は、第2図に示す制御時の炉内圧の変動を示すグ
ラフである。 第4図および第5図は、それぞれ本発明におけるガス洩
れ率および石炭のタール中へのキャリオーバー量の推移
を示すグラフである。 第6図は、コークス炉への石炭装入状況を示す説明図で
ある。 第7図は、従来の炉内圧の変動を示すグラフである。 符号の説明 1…装入車、2…ホッパー、3…装入車集塵機、4…上
昇管ベンド部、4a…高圧安水、5…テーブルフィーダ
ー、6…駆動用モーター、7…圧力計、8…演算、制御
用シーケンサー、9…基準圧力設定器、10…コークス
炉、11…装入口、12…炭化室
FIG. 1 shows a configuration of a control device for implementing the present invention.
It is a system diagram showing an example. FIG. 2 is a graph showing an example of the control of the coal charging speed according to the present invention. FIG. 3 is a graph showing a change in furnace pressure during the control shown in FIG. FIGS. 4 and 5 are graphs showing changes in the gas leakage rate and the amount of carryover of coal into tar in the present invention, respectively. FIG. 6 is an explanatory diagram showing a state of charging coal into a coke oven. FIG. 7 is a graph showing a conventional furnace pressure fluctuation. DESCRIPTION OF SYMBOLS 1 ... loaded car, 2 ... hopper, 3 ... loaded car dust collector, 4 ... riser bend part, 4a ... high pressure water, 5 ... table feeder, 6 ... drive motor, 7 ... pressure gauge, 8 ... Sequencer for calculation and control, 9 ... Reference pressure setting device, 10 ... Coke oven, 11 ... Inlet, 12 ... Coking room

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】コークス炉へ石炭を装入する際に、コーク
ス炉の炭化室内圧力を連続的に測定し、この測定値に基
づき石炭を装入する速度を予め定めた基準圧力と測定値
を比較して調節し、前記炭化室内圧力を基準圧力範囲内
になるように制御することを特徴とするコークス炉への
石炭装入方法。
When charging coal into a coke oven, the pressure in the carbonization chamber of the coke oven is continuously measured, and based on the measured value, the reference pressure and the measured value are set to a predetermined rate for charging the coal. A method for charging coal into a coke oven, wherein the method controls the pressure in the coking oven so that the pressure in the coking chamber falls within a reference pressure range.
JP2142872A 1990-05-31 1990-05-31 Coal charging method for coke oven Expired - Lifetime JP2880766B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2142872A JP2880766B2 (en) 1990-05-31 1990-05-31 Coal charging method for coke oven

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2142872A JP2880766B2 (en) 1990-05-31 1990-05-31 Coal charging method for coke oven

Publications (2)

Publication Number Publication Date
JPH0436385A JPH0436385A (en) 1992-02-06
JP2880766B2 true JP2880766B2 (en) 1999-04-12

Family

ID=15325563

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2142872A Expired - Lifetime JP2880766B2 (en) 1990-05-31 1990-05-31 Coal charging method for coke oven

Country Status (1)

Country Link
JP (1) JP2880766B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2291352T3 (en) * 2000-08-23 2008-03-01 Dmt Gmbh PROCEDURE FOR CHARGING COCKTAIL OVEN CAMERAS OF AN OVEN BATTERY.
JP5942488B2 (en) * 2012-03-06 2016-06-29 Jfeスチール株式会社 Coal charging method for coke oven charging vehicle

Also Published As

Publication number Publication date
JPH0436385A (en) 1992-02-06

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