JPH078984B2 - Edge flue temperature raising method in coke oven - Google Patents
Edge flue temperature raising method in coke ovenInfo
- Publication number
- JPH078984B2 JPH078984B2 JP4485588A JP4485588A JPH078984B2 JP H078984 B2 JPH078984 B2 JP H078984B2 JP 4485588 A JP4485588 A JP 4485588A JP 4485588 A JP4485588 A JP 4485588A JP H078984 B2 JPH078984 B2 JP H078984B2
- Authority
- JP
- Japan
- Prior art keywords
- flue
- coke oven
- nozzles
- temperature distribution
- combustion
- 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
Links
Landscapes
- Coke Industry (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は、単段燃焼方式のコークス炉における端フリュ
ーの昇温方法に関するものである。The present invention relates to a method for raising the temperature of end flue in a single-stage combustion type coke oven.
(従来の技術) 単段燃焼方式のコークス炉においては、炉高方向のフリ
ュー(燃焼室)内における壁温分布を制御する場合、フ
リュー底に設けたフリューポートのポートダンパーにて
フリューポートの開孔面積を変更し、燃焼状況に影響を
与える噴出速度を調整して目的に応じた炉高方向の壁温
分布を得るようにしている。(Prior art) In a single-stage combustion type coke oven, when controlling the wall temperature distribution in the flue (combustion chamber) in the furnace height direction, the flue port is opened by the flue port port damper installed at the flue bottom. By changing the hole area and adjusting the jet speed that affects the combustion condition, the wall temperature distribution in the furnace height direction according to the purpose is obtained.
また、端フリューを昇温するために、燃焼ガスのみか、
あるいは本出願人が先に特願昭62−2051号(特開昭63−
135485号公報)で提案した燃料ガスと燃焼用空気の両方
を投入する方法もある。Also, in order to raise the temperature of the end flue, only the combustion gas,
Alternatively, the present applicant previously filed Japanese Patent Application No. 62-2051 (Japanese Patent Laid-Open No. 63-
There is also a method proposed in JP-A-135485) in which both fuel gas and combustion air are introduced.
(発明が解決しようとする課題) しかしながら、負荷率(入熱量)の変更や空気比および
炉圧等の変化に応じて、各々のフリューポート開孔面積
を変更させることは非常に困難である。特に、端フリュ
ーに関しては、炉壁からの放散熱が多く、ポートダンパ
ーによる調整だけでは、任意の炉高方向壁温分布が得ら
れない為、炭化室に与える温度分布が悪くなってコーク
スの焼きムラによる品質のバラツキが起こる。またこの
バラツキを改善するために、中央部のフリューに対し
て、必要以上に乾留時間を要し、ひいては乾留熱量の増
加により、省エネルギー面に支障をきたす。(Problems to be Solved by the Invention) However, it is very difficult to change each flu port opening area in accordance with a change in load factor (heat input amount) or a change in air ratio, furnace pressure, or the like. Especially for the end flue, there is a large amount of heat radiated from the furnace wall, and an arbitrary wall temperature distribution in the furnace high direction cannot be obtained simply by adjusting the port damper. Variations in quality occur due to unevenness. Further, in order to improve this variation, the flue in the central portion requires an excessive amount of dry distillation time, which in turn causes an increase in the amount of dry distillation heat, which causes an obstacle to energy saving.
また、単に炉高方向において、燃料ガスのみや燃焼用空
気との両方を投入しても、ノズル挿入部分の昇温には効
果があるものの、操業条件に見合ったフリュー内の壁温
分布パターンは得られず、品質のバラツキや乾留熱量の
低減には効果は不充分である。Further, even if only the fuel gas and the combustion air are introduced in the furnace height direction, it is effective in raising the temperature of the nozzle insertion part, but the wall temperature distribution pattern in the flue that matches the operating conditions is It is not obtained, and the effect is insufficient for quality variation and reduction of dry distillation heat quantity.
本発明は、かかる問題点を解決できるコークス炉の端フ
リュー昇温方法を提供せんとするものである。The present invention aims to provide a method for raising the temperature of the end flue of a coke oven that can solve the above problems.
(課題を解決するための手段) 上記した目的を達成するために本発明は、押出機側及び
消化車側の各端フリュー内の適宜の位置に、夫々の噴出
孔を相対向させるよう燃料ガスノズルと燃焼要空気ノズ
ルを挿入配置し、予め求めておいた前記両ノズルからの
噴出角度とフリュー内での壁温分布に基づき、これら両
ノズルと両側の炭化室方向に0〜90゜の範囲で回転させ
るものである。(Means for Solving the Problems) In order to achieve the above-mentioned object, the present invention is directed to a fuel gas nozzle such that respective ejection holes face each other at appropriate positions in the respective end flues on the extruder side and the digestion wheel side. Based on the ejection angle from both nozzles and the wall temperature distribution in the flue that are obtained in advance, the nozzles for combustion need to be inserted and arranged in the range of 0 to 90 ° in the direction of these nozzles and both sides of the carbonization chamber. It is to rotate.
本発明において、両ノズルの回転範囲を0゜〜90゜にし
たのは、90゜を超えた場合には、燃焼性が著しく不安定
(排ガスO2濃度のバラツキ大)になり、端フリューの目
的に応じた壁温分布が得られないためである。In the present invention, the reason why the rotation range of both nozzles is set to 0 ° to 90 ° is that if it exceeds 90 °, the combustibility becomes remarkably unstable (the exhaust gas O 2 concentration varies greatly) and the end flue is This is because the wall temperature distribution according to the purpose cannot be obtained.
(作用) 本発明は、単段燃焼方式コークス炉の端フリュー昇温方
法において、押出機側及び消化車側の各端フリュー内の
適宜の位置に、夫々の噴出孔を相対向させるように燃料
ガスノズルと燃焼要空気ノズルを挿入配置し、予め求め
ておいた前記両ノズルからの噴出角度とフリューでの壁
温分布に基づき、これら両ノズルを両側の炭化室方向に
0〜90゜の範囲で回転させるものであり、これによって
燃焼形態を急速燃焼から緩慢燃焼まで任意に変えられ、
炉高方向にフリュー内の壁温分布パターンを、目的に応
じて選択できる。(Operation) In the method for raising the temperature of the end flue of the single-stage combustion type coke oven, the present invention is arranged so that the respective ejection holes are opposed to each other at appropriate positions in the end flues on the extruder side and the digester side. A gas nozzle and a combustion air nozzle are inserted and arranged, and based on the ejection angle from both nozzles and the wall temperature distribution at the flue that have been obtained in advance, these nozzles are placed in the range of 0 to 90 ° in the direction of the carbonization chamber on both sides. It is to rotate, by which the combustion form can be arbitrarily changed from rapid combustion to slow combustion,
The wall temperature distribution pattern in the flue in the furnace height direction can be selected according to the purpose.
また、入熱量を調整することにより、さらに壁温分布パ
ターンの変化が容易になる。Further, by adjusting the heat input amount, it becomes easier to change the wall temperature distribution pattern.
(実 施 例) 以下本発明を第1図に示す一実施例に基づいて説明す
る。(Example) The present invention will be described below based on an example shown in FIG.
図面は本発明方法を適用する端フリュー部の概略断面図
であり、図中1はフリュー底より所定高さの位置に挿入
配置されて端フリュー2に燃焼用空気を吹込む燃焼用空
気ノズル、3は同じく燃焼ガスを吹込む燃料ガスノズル
を示しており、これら空気ノズル1と燃料ガスノズル3
の夫々の噴出孔4、5は端フリュー2内において相対向
すべく配置されている。The drawing is a schematic cross-sectional view of an end flue portion to which the method of the present invention is applied. In the drawing, reference numeral 1 denotes a combustion air nozzle which is inserted at a predetermined height from the flu bottom and blows combustion air into the end flue 2. Reference numeral 3 also designates a fuel gas nozzle for blowing combustion gas. These air nozzle 1 and fuel gas nozzle 3 are also provided.
The ejection holes 4 and 5 are arranged in the end flue 2 so as to face each other.
そして、これら両ノズル1、3は夫々例えば正逆回転可
能なモータ6、7及びギア8、9等の適宜の機構によっ
て例えば0〜90゜の範囲で回転位置決めできるように成
されている。The two nozzles 1 and 3 can be rotationally positioned within a range of, for example, 0 ° to 90 ° by an appropriate mechanism such as, for example, motors 6 and 7 and gears 8 and 9 capable of rotating in the forward and reverse directions.
なお、図中10はフリューポートを構成する燃料ポート、
11は同じく燃焼用空気ポート、12はポートダンパーを示
す。In the figure, 10 is the fuel port that constitutes the flue port,
11 is a combustion air port, and 12 is a port damper.
例えば炉高が3m、炉幅が370mm、炉長さが190mmの端フリ
ュー燃焼空モデル(相似比K=0.7)内のフリュー底よ
り420mmの位置に210mmの間隔を存して空気ノズル1と燃
焼ガスノズル3を挿入配置し、これらノズル1、3の噴
出角度を0゜(真横)(第2図中の点線)、30゜(同一
点鎖線)、60゜(同二点鎖線)、90゜(真上)(同破
線)と変化させた場合の端フリュー昇温による壁温分布
を従来のフリューポートのみによる場合(第2図中の実
線)と共に示すと第2図の如くになる。なお、この場合
のベース入熱量は27600kcal/h(COG=6.0Nm3/h)、増熱
量は29.5%(8140kcal/h)であった。For example, in an end-flue combustion air model (similarity ratio K = 0.7) with a furnace height of 3 m, a furnace width of 370 mm, and a furnace length of 190 mm, burn with the air nozzle 1 at a distance of 210 mm at a position 420 mm from the flu bottom. The gas nozzle 3 is inserted and arranged, and the ejection angles of these nozzles 1 and 3 are 0 ° (right side) (dotted line in FIG. 2), 30 ° (same dashed line), 60 ° (same two-dot chain line), 90 ° ( FIG. 2 shows the wall temperature distribution due to the temperature rise of the end flue when it is changed to (directly above) (the same broken line) together with the case where only the conventional flue port is used (solid line in FIG. 2). In this case, the base heat input was 27600 kcal / h (COG = 6.0 Nm 3 / h) and the heat gain was 29.5% (8140 kcal / h).
本発明では、上記したような端フリュー昇温による壁温
分布を予め求めておき、この壁温分布に基づいて最適な
壁温パターンとなるように両ノズル1、3の回動角度を
設定しつつ昇温するのである。In the present invention, the wall temperature distribution due to the above-described edge flue temperature rise is obtained in advance, and the rotation angles of both nozzles 1 and 3 are set based on this wall temperature distribution so as to obtain an optimum wall temperature pattern. While raising the temperature.
ちなみに、上記第2図に示す壁温分布に基づいて端フリ
ューの昇温を行ったところ、1)乾留熱量は、端フリュ
ー炉高方向温度分布の改善による平均炉温低減で、15kc
al/kg coal低減でき、2)品質のバラツキも窯口火落不
良改善により、大きく低減した。By the way, when the temperature of the end flue was raised based on the wall temperature distribution shown in Fig. 2, 1) the dry distillation heat quantity was 15 kc due to the average furnace temperature reduction due to the improvement of the end flue furnace high temperature distribution.
Al / kg coal can be reduced. 2) Variations in quality have also been greatly reduced by improving the kiln burnout failure.
(発明の効果) 以上説明したように本発明によれば、両ノズルを回転さ
せることにより、目的に応じた燃焼形態にし、中央部の
フリューに見合った乾留時間になるように、端フリュー
の入熱量を調整し、コークスの焼ムラをなくすことがで
きる。(Effects of the Invention) As described above, according to the present invention, by rotating both nozzles, a combustion mode suitable for the purpose is obtained, and the end flue is introduced so that the dry distillation time is commensurate with the flue in the central portion. The amount of heat can be adjusted to eliminate the uneven burning of coke.
第1図は本発明方法を適用する端フリュー部の概略断面
図で、(イ)は平面図、(ロ)は正面図、第2図は端フ
リュー昇温による壁温分布の一例を示す図面である。 1は空気ノズル、2は端フリュー、3は燃料ガスノズ
ル、4、5は噴出孔。FIG. 1 is a schematic cross-sectional view of an end flue part to which the method of the present invention is applied. (A) is a plan view, (b) is a front view, and FIG. 2 is a drawing showing an example of wall temperature distribution due to end flue temperature rise. Is. 1 is an air nozzle, 2 is an end flue, 3 is a fuel gas nozzle, and 4 and 5 are ejection holes.
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭62−62888(JP,A) 実開 昭62−21048(JP,U) 実開 昭62−21049(JP,U) ─────────────────────────────────────────────────── ─── Continuation of the front page (56) Reference JP-A-62-62888 (JP, A) Actually opened 62-21048 (JP, U) Actually opened 62-21049 (JP, U)
Claims (1)
方法において、押出機側及び消化車側の各端フリュー内
の適宜の位置に、夫々の噴出孔を相対向させるように燃
料ガスノズルと燃焼用空気ノズルを挿入配置し、予め求
めておいた前記両ノズルからの噴出角度とフリュー内で
の壁温分布に基づき、これら両ノズルを両側の炭化室方
向に0〜90゜の範囲で回転させることを特徴とするコー
クス炉における端フリュー昇温方法。1. In a method for raising the temperature of an end flue of a single-stage combustion type coke oven, a fuel gas nozzle is provided at an appropriate position in each end flue on the extruder side and the digestion car side so that respective ejection holes face each other. Combustion air nozzles are inserted and arranged, and both nozzles are rotated in the carbonization chamber direction on both sides in the range of 0 to 90 ° based on the ejection angles from both nozzles and the wall temperature distribution in the flue that have been obtained in advance. An edge flue temperature raising method in a coke oven, which comprises:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4485588A JPH078984B2 (en) | 1988-02-26 | 1988-02-26 | Edge flue temperature raising method in coke oven |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4485588A JPH078984B2 (en) | 1988-02-26 | 1988-02-26 | Edge flue temperature raising method in coke oven |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01217097A JPH01217097A (en) | 1989-08-30 |
| JPH078984B2 true JPH078984B2 (en) | 1995-02-01 |
Family
ID=12703097
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4485588A Expired - Lifetime JPH078984B2 (en) | 1988-02-26 | 1988-02-26 | Edge flue temperature raising method in coke oven |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH078984B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102008050599B3 (en) * | 2008-10-09 | 2010-07-29 | Uhde Gmbh | Apparatus and method for distributing primary air in coke ovens |
-
1988
- 1988-02-26 JP JP4485588A patent/JPH078984B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01217097A (en) | 1989-08-30 |
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