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JPS6158508B2 - - Google Patents
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JPS6158508B2 - - Google Patents

Info

Publication number
JPS6158508B2
JPS6158508B2 JP59053684A JP5368484A JPS6158508B2 JP S6158508 B2 JPS6158508 B2 JP S6158508B2 JP 59053684 A JP59053684 A JP 59053684A JP 5368484 A JP5368484 A JP 5368484A JP S6158508 B2 JPS6158508 B2 JP S6158508B2
Authority
JP
Japan
Prior art keywords
heating
gas
air
connecting wall
wall
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
Application number
JP59053684A
Other languages
Japanese (ja)
Other versions
JPS59179692A (en
Inventor
Urubai Kurausu
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.)
Fuiruma Kaaru Shuteiru Unto Co KG GmbH
Original Assignee
Fuiruma Kaaru Shuteiru Unto Co KG GmbH
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 Fuiruma Kaaru Shuteiru Unto Co KG GmbH filed Critical Fuiruma Kaaru Shuteiru Unto Co KG GmbH
Publication of JPS59179692A publication Critical patent/JPS59179692A/en
Publication of JPS6158508B2 publication Critical patent/JPS6158508B2/ja
Granted 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
    • C10B21/00Heating of coke ovens with combustible gases
    • C10B21/20Methods of heating ovens of the chamber oven type
    • C10B21/22Methods of heating ovens of the chamber oven type by introducing the heating gas and air at various levels
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Coke Industry (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)
  • Secondary Cells (AREA)

Description

【発明の詳細な説明】 本発明は空気または貧ガスの予熱および排熱の
回収のため炉の全長にわたつて走る蓄熱室、加熱
炎道高さにわたつて分布する加熱炎道への出口ス
リツトを備える、加熱炎道つなぎ壁内の通路を通
る空気または空気および貧ガスの供給装置ならび
に加熱炎道への富ガス供給装置を有する富ガスお
よび貧ガスで加熱しうる蓄熱式コークス炉バツテ
リの加熱装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The invention provides a heat storage chamber running over the entire length of the furnace for preheating air or lean gases and recovery of waste heat, an outlet slit to the heating flame duct distributed over the height of the heating flame duct. Heating of a regenerative coke oven battery heatable with rich gas and lean gas, comprising a supply of air or air and lean gas through passages in the heating flame duct connecting wall and a rich gas supply to the heating flame duct. Regarding equipment.

このような加熱装置は炎道交替のためコークス
押出方向の中央で分割した加熱壁を有する2分割
系および加熱壁が加熱炎道の多数の群に対して分
割されている系である。
Such heating devices are two-part systems having a heating wall divided in the center in the direction of coke extrusion for flame path alternation, and systems in which the heating wall is divided into multiple groups of heating flame paths.

この加熱系の場合つなぎ壁通路から出口スリツ
トを介して加熱炎道へ入る加熱ガスおよび燃焼空
気の最適の分配に関する問題がある。加熱炎道高
さにわたる熱の分配は加熱ガス供給を約一にして
空気量を変化することによつて行われる。しかし
この方法によれば加熱ガスが理論的に必要な空気
量によつて燃焼する場合にしか最適の加熱効果は
達成されない。
In this heating system, there are problems regarding the optimal distribution of the heating gas and combustion air which enters the heating flame duct from the connecting wall channel via the outlet slot. The distribution of heat over the heating flame path height is achieved by varying the air volume with the heating gas supply approximately equal. However, with this method an optimum heating effect can only be achieved if the heating gas is combusted with the theoretically required amount of air.

加熱炎道内の熱分布を制御するため、斜め上向
きのつなぎ壁スリツトを配置することによつて加
熱炎道内の空気流に優先方向を与え、かつつなぎ
壁スリツトを閉鎖可能に形成することも公知であ
る(西独特許第1211125号明細書)。
In order to control the heat distribution in the heating flame duct, it is also known to give a preferential direction to the airflow in the heating flame duct by arranging a slanted upward tie wall slit, and to form the tether wall slit in a closable manner. Yes (West German Patent No. 1211125).

出口スリツトを垂直方向に1線にそろえずに、
横方向に互いにずらして配置し、加熱炎道への出
口スリツトの開口に種々の断面の交換可能のノズ
ルレンガを備えることも同様公知である(たとえ
ば西独特許公報第1903805号参照)。
Do not align the exit slits vertically in one line.
It is likewise known to provide exchangeable nozzle bricks of various cross-sections arranged laterally offset from each other and of different cross-sections at the opening of the outlet slot to the heating flame channel (see, for example, German Patent No. 1903805).

この加熱装置によればたとえば加熱を富ガスか
ら貧ガスへもしくはその反対に切替える際、また
加熱壁の熱需要が変化した際、空気供給比を外側
からすなわちバツテリの低温部からガス種類また
は石炭種類に、所望の有利な壁加熱に必要な加熱
炎道内の炎形成が達成されるように、適合させる
ことは大きい熱損失を伴わなければ可能でない。
With this heating device, for example, when switching the heating from gas-rich to gas-poor gas or vice versa, or when the heat demand of the heating wall changes, the air supply ratio can be changed from the outside, i.e. from the cold part of the battery to the type of gas or type of coal. It is only possible to adapt the flame formation in the heating flame duct so that the flame formation necessary for the desired advantageous wall heating is achieved without large heat losses.

燃焼空気または貧ガスのための横壁によつて分
割された蓄熱室区画を有し、各加熱炎道内の高い
および低い燃焼部ならびに加熱炎道底部の富ガス
供給孔を有する蓄熱式コークス炉バツテリも公知
であり、その際加熱炎道の下側燃焼部は蓄熱式の
各第1区画と結合し、上側燃焼部は蓄熱式の各第
2区画と結合し、各区画は加熱炎道の全高にわた
る均一な加熱を達成するため、種々の高さにある
燃焼部に供給すべき種々の空気または貧ガス量に
適合した断面を有する。このような加熱は外側の
低温部からその加熱媒体量が調節可能であるけれ
ども、この場合加熱炎道内の燃焼部は2つだけす
なわち上側に1つ、下側に1つであり、本発明の
場合のようにつなぎ壁通路から加熱炎道への貧ガ
スまたは空気出口スリツトは多数でない。
Regenerative coke oven batteries also have regenerator compartments divided by lateral walls for combustion air or lean gases, with high and low combustion sections in each heating flame duct and rich gas feed holes at the bottom of the heating duct. It is known that the lower combustion section of the heating flame duct is connected to a respective first section of the regenerative type, and the upper combustion section is connected to a respective second section of the regenerative type, each section extending over the entire height of the heating duct. In order to achieve uniform heating, it has a cross section adapted to the different amounts of air or lean gas to be supplied to the combustion section at different heights. Although the amount of heating medium in such heating can be adjusted from the outside low temperature part, in this case there are only two combustion parts in the heating flame path, one on the upper side and one on the lower side, and the present invention There are not as many gas or air outlet slits from the connecting wall passage to the heating flame duct as in the case.

さらに加熱壁の加熱炎道つなぎ壁内の通路およ
びつなぎ壁通路から加熱炎道への貧ガスまたは空
気出口スリツトならびに区画に分割した蓄熱室を
有する富ガスまたは貧ガスで加熱しうる蓄熱式コ
ークス炉バツテリの加熱装置が公知であり、蓄熱
室は一方で底部炎道を介して貧ガスもしくは空気
弁または排熱弁と結合し、他方でつなぎ壁通路と
結合し、貧ガスから富ガスへもしくはその反対の
切替またはコークス化する炭種を1つから他へ切
替える際、異なる蓄熱室区画に接続したつなぎ壁
通路の貧ガスまたは空気出口スリツトの断面の大
きさが高さにわたつて2つ以上の一定であるけれ
ど種々の法則により選択されていることによつ
て、最適の作業に適するように形成される。この
場合1つの加熱炎道の隣接または相対するつなぎ
壁通路のガスまたは空気出口スリツトの断面は高
さにわたつて直線的に増大もしくは減少し、また
他の法則により変化することができる。スリツト
断面のこの形成により加熱炎道の高さにわたつて
空気を多数の位置に分配することができ、空気分
配を外側からすなわちバツテリの低温部から底部
炎道の外側端部の空気−排熱弁によつて調節する
こともできる(西独特許第2013024号明細書参
照)。
Furthermore, a regenerative coke oven capable of heating with gas-rich or gas-poor gas has a passage in the heating flame duct connecting wall of the heating wall and a lean gas or air outlet slit from the connecting wall passage to the heating flame duct and a compartmentalized regenerator. Batteries heating devices are known, in which the regenerator is connected on the one hand via a bottom flame channel with a gas-poor or air valve or with a waste heat valve and on the other hand with a connecting wall passage, which converts gas-poor to gas-rich or vice versa. or when changing over from one type of coal to be coked to another, the cross-sectional size of the poor gas or air outlet slits of the connecting wall passages connected to different storage compartments is constant over the height of two or more. However, by being selected according to various rules, it is formed to be optimally suited for the task. In this case, the cross-section of the gas or air outlet slits of adjacent or opposing connecting wall passages of one heating flame channel increases or decreases linearly over the height and can also vary according to other laws. This formation of the slit cross-section makes it possible to distribute the air to a number of locations over the height of the heating flame duct, with the air distribution being carried out from the outside, i.e. from the cold part of the battery to the air-exhaust valve at the outer end of the bottom flame duct. (see German Patent No. 2013024).

つなぎ壁通路の出口スリツトは加熱炎道の上部
すなわち加熱炎道高さの半分より上へ配置するこ
ともできるので、空気調節したがつて熱の調節は
炉室のはるか上部まで達する。しかし、加熱炎道
上部たとえば中央で分割した加熱系の場合、炉室
のなお石炭が装入されている高さの上部水平通路
の範囲には調節可能性または空気供給可能性が公
知技術では存在しない。加熱系が半分に分割され
たコークス炉バツテリの場合の上部水平通路は、
4炎道加熱系を有するバツテリの場合のつなぎ壁
を超えて同じ加熱壁の隣接加熱炎道に通ずる上部
加熱ガス通路に相当する。これは同時に加熱ガス
の方向反転部である。このような反転部はヘアピ
ン形加熱炎道の場合にもある。
The outlet slits of the connecting wall passages can also be arranged above the heating flame duct, ie above half the height of the heating duct, so that the air conditioning and therefore the heat regulation reaches far into the top of the furnace chamber. However, in the case of a centrally divided heating system, for example in the case of a centrally divided heating system, the possibility of adjusting or supplying air in the area of the upper horizontal passage of the furnace chamber at the level where the coal is charged does not exist in the prior art. do not. The upper horizontal passage in the case of a coke oven battery with a heating system divided in half is
This corresponds to the upper heating gas passage leading beyond the connecting wall to the adjacent heating flame duct of the same heating wall in the case of a battery with a four-flame duct heating system. This is at the same time a direction reversal of the heating gas. Such inversions also exist in the case of hairpin-shaped heating flame channels.

しかし作業条件に応じてこの系に対して水平通
路の範囲または1つの加熱炎道もしくはその群か
ら隣接炎道もしくはその群への加熱ガスの反転部
の範囲にも空気供給の制御可能性を備えることが
望ましい。
However, depending on the working conditions, this system also has the possibility of controlling the air supply in the area of the horizontal passage or in the area of the reversal of the heating gas from one heating flame duct or groups thereof to an adjacent flame duct or groups thereof. This is desirable.

本発明はの目的は空気供給が上部水平通路の範
囲またはつなぎ壁の上の範囲においても可能であ
り、それによつてこの範囲でも作業条件に応じて
温度または空気対ガスの比を補足的に調節しうる
ように前記加熱系を改善することである。
The object of the invention is that the air supply is also possible in the area of the upper horizontal passage or in the area above the connecting wall, so that even in this area the temperature or the air-to-gas ratio can be adjusted in a complementary manner depending on the working conditions. The purpose is to improve the heating system so as to make it possible.

本発明によりこの目的は空気供給のためのみに
役立つつなぎ壁通路がつなぎ壁内をつなぎ壁の上
端まで通じ、かつ上部水平通路または加熱ガスが
その流れ方向を上向きから下向きへまたはその反
対に変化するつなぎ壁上の加熱ガス反転部の範囲
への出口開口を有し、その断面を制御可能に形成
することによつて解決される。
According to the invention, this purpose is achieved by providing that a connecting wall channel serving only for the air supply runs in the connecting wall up to the upper end of the connecting wall, and that the upper horizontal channel or heating gas changes its flow direction from upwards to downwards or vice versa. This is solved by having an outlet opening in the region of the heated gas inversion on the connecting wall and by controllably shaping its cross section.

この場合この出口開口の断面をたとえばかぶせ
たスライドレンガによつて制御可能に形成するの
が有利であり、このレンガによつて出口スリツト
を完全に閉鎖することもできる。
In this case, it is advantageous to controllably form the cross-section of this outlet opening, for example by means of a covered slide brick, with which it is also possible to completely close off the outlet slot.

西独特願P3119923、9号の提案による加熱系
の本発明による形成はとくに有利である。
The inventive design of the heating system as proposed in German patent application P 3119923, no. 9 is particularly advantageous.

本発明によればさらに付加的に上部水平通路ま
たは加熱炎道の上部に、この範囲の炭化室に空気
または付加的熱を必要とする場合、任意に空気を
導入することができる。上部水平通路に供給する
空気量は加熱炎道の下部から取出した残りの部分
なので、全体として空気量は変化しないけれど、
ガス燃焼は一部上部水平通路または相当する位置
へずれる。
According to the invention, air can optionally also be introduced into the upper horizontal channel or the upper part of the heating flame channel, if air or additional heat is required in this area of the carbonization chamber. The amount of air supplied to the upper horizontal passage is the remaining portion taken out from the bottom of the heating flame path, so the overall amount of air does not change, but
Gas combustion is partially shifted to the upper horizontal passage or equivalent position.

さらに燃焼排ガスのNOx減少の点でも本発明
の手段は有利である。それは加熱炎道の下部範囲
で空気不足下に燃焼させ、水平通路の範囲で後燃
焼することができるからである。このような燃焼
の制御は公知構造の炉では不可能であつた。
Furthermore, the means of the present invention is advantageous in terms of reducing NOx in combustion exhaust gas. This is because combustion can occur under air deficiency in the lower region of the heating flame duct and after-combustion can occur in the region of the horizontal passage. Such control of combustion has not been possible in furnaces of known construction.

次に本発明を図面により説明する。 Next, the present invention will be explained with reference to the drawings.

第1〜3図は富ガスによるいわゆる4炎道加熱
系、第4図は富ガスおよび貧ガスによる4炎道複
合加熱系、第5図は富ガスおよび貧ガスのため半
分に分割した加熱系を示す。
Figures 1 to 3 show a so-called 4-flame-path heating system using rich gas, Figure 4 shows a 4-flame combined heating system using rich gas and poor gas, and Figure 5 shows a heating system divided in half for rich gas and poor gas. shows.

図において1は天じよう、2は個々の加熱炎道
群の間の隔壁、3,3aはスライドレンガを表わ
す。4は2つの空気供給通路を有する中空つなぎ
壁、5は1つのみの空気供給通路を有する中空つ
なぎ壁である。6はこれに反し中央に配置した中
実つなぎ壁すなわち通路なしのつなぎ壁である。
7,7aはつなぎ壁通路、8は4炎道上部水平通
路への開口である。9はつなぎ壁スリツトであ
り、6aは上部つなぎレンガを表わす。10は2
つの空気供給通路7を有するつなぎ壁4と1つの
通路7aを有するつなぎ壁5によつて仕切られた
加熱炎道を表わす。これに対し10aは1つの空
気供給通路7aを有するつなぎ壁5と中実すなわ
ち空気供給通路を有しないつなぎ壁6によつて仕
切られた加熱炎道である。11はスライドレンガ
支持板、12は4炎道上部水平通路である。13
(第2図)は加熱炎道への富ガス供給通路を表わ
す。14はケイ酸塩材料からなるバツテリ中心構
造、15は蓄熱室を表わす。16は炉床ライニン
グ、17は加熱壁を表わす。18(第3図)は炉
室、19は4炎道ガス供給通路の側壁レンガ積で
ある。20は富ガスノズル、21は加熱ガスの反
転部である(第1図)。
In the figure, 1 represents a ceiling, 2 represents a partition wall between individual heating flame path groups, and 3 and 3a represent slide bricks. 4 is a hollow connecting wall having two air supply passages, and 5 is a hollow connecting wall having only one air supply passage. 6, on the other hand, is a centrally located solid connecting wall, that is, a connecting wall without passages.
7 and 7a are connecting wall passages, and 8 is an opening to the upper horizontal passage of the four flame ducts. 9 is a connecting wall slit, and 6a represents an upper connecting brick. 10 is 2
The heating flame path is partitioned by a connecting wall 4 with two air supply channels 7 and a connecting wall 5 with one channel 7a. On the other hand, 10a is a heating flame channel partitioned by a connecting wall 5 having one air supply passage 7a and a solid connecting wall 6, that is, having no air supply passage. 11 is a slide brick support plate, and 12 is a horizontal passage above the four flame ducts. 13
(Figure 2) represents the rich gas supply passage to the heating flame duct. 14 represents a battery center structure made of silicate material, and 15 represents a heat storage chamber. 16 represents a hearth lining, and 17 represents a heating wall. 18 (Fig. 3) is the furnace chamber, and 19 is the side wall brickwork of the four flame gas supply passages. 20 is a rich gas nozzle, and 21 is a heating gas reversal section (FIG. 1).

第4図において22は通路天じよう、23は加
熱炎道群の隔壁である。30はスライドレンガで
あり、これによつてつなぎ壁40を貫通する空気通
路70の4炎道水平通路120への開口80を閉
鎖し、またはその断面を変化することができる。
90はつなぎ壁通路70から加熱炎道100への
空気出口スリツトである。30aはスライドレン
ガ支持板110上のスライドレンガであり、この
レンガによつて加熱炎道100から4炎道水平通
路への加熱ガス通過断面を変化することができ
る。つなぎ壁60のスライドレンガ支持板110
は上部つなぎレンガ60a上にある。つなぎ壁6
0は貧ガス通路70aおよびガス出口スリツト9
0aを有する。加熱炎道100はすべて2つのつ
なぎ壁によつて仕切られ、その1つは上端まで貫
通する2つの空気供給通路70を有し、他のつな
ぎ壁60は1つの貧ガス供給通路70aを備える
だけである。ガス反転部は210で示される。
In FIG. 4, 22 is a passage top, and 23 is a partition wall of a group of heating flame channels. 30 is a sliding brick, by means of which the opening 80 of the air passage 70 penetrating the connecting wall 40 to the four-flame horizontal passage 120 can be closed or its cross section can be changed.
90 is an air outlet slit from the connecting wall passage 70 to the heating flame duct 100. 30a is a slide brick on the slide brick support plate 110, and this brick can change the heating gas passage cross section from the heating flame path 100 to the four flame path horizontal passages. Slide brick support plate 110 of connecting wall 60
is on the upper connecting brick 60a. Tie wall 6
0 is the poor gas passage 70a and the gas outlet slit 9
It has 0a. All heating flame ducts 100 are partitioned by two connecting walls, one of which has two air supply passages 70 penetrating to the upper end, and the other connecting wall 60 only has one poor gas supply passage 70a. It is. The gas inversion section is indicated at 210.

第5図には中央で分割される加熱壁の本発明に
よる実施例が示される。この場合上部水平通路は
220、ガス反転部は230で示される。240
は上部水平通路の天じようである。この加熱系の
場合中央に中央つなぎ壁250が配置され、この
壁は加熱炎道280への出口スリツト270を有
する2つの空気供給通路260を備える。つなぎ
壁250内の空気供給通路260は上端に上部つ
なぎレンガ250aおよび閉鎖板290を支持す
るつなぎ壁の上端まで貫通しない。その他の加熱
炎道300は上端まで貫通する空気供給通路32
0および上部水平通路220への開口を有するつ
なぎ壁310によつて仕切られる。この上部開口
は330で示され、その断面はスライドレンガ支
持板350に支持されるスライドレンガ340に
よつて変化することができる。加熱炎道310か
ら上部水平通路220への加熱ガスの出口はその
断面がスライドレンガ支持板360上のスライド
レンガ370によつて可変である。つなぎ壁通路
320は加熱炎道への空気出口スリツト380を
備え、つなぎ壁390は貧ガス供給通路400お
よび出口スリツト410を備える。
FIG. 5 shows an embodiment according to the invention of a centrally divided heating wall. In this case the upper horizontal passage is indicated at 220 and the gas inversion section at 230. 240
is like the sky of the upper horizontal passage. In this heating system, a central connecting wall 250 is arranged in the middle, which wall comprises two air supply channels 260 with outlet slots 270 to the heating flame channel 280 . The air supply passage 260 in the tie wall 250 does not penetrate to the upper end of the tie wall, which supports the upper tie brick 250a and the closing plate 290 at the upper end. The other heating flame path 300 is an air supply passage 32 that penetrates to the upper end.
0 and a tie wall 310 having an opening to the upper horizontal passage 220. This upper opening is indicated at 330 and its cross section can be varied by a sliding brick 340 supported on a sliding brick support plate 350. The outlet of the heated gas from the heating flame channel 310 to the upper horizontal passage 220 has a variable cross section by the sliding brick 370 on the sliding brick support plate 360. The tie wall passage 320 includes an air outlet slit 380 to the heating flame path, and the tie wall 390 includes a lean gas supply passage 400 and an outlet slit 410.

ガス流の方向は図面にはそれぞれ矢印500,
600および700で示される。加熱方向切替の
際ガスは反対方向に流れる。
The direction of gas flow is indicated by arrows 500 and 500 in the drawing, respectively.
600 and 700. When switching the heating direction, the gas flows in the opposite direction.

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

第1図は4炎道加熱系の縦断面図、第2図は第
1図つなぎ壁通路の第1図に対し直角の縦断面
図、第3図は第1図炎道の平面図、第4図は富ガ
スおよび貧ガスによる4炎道加熱系の縦断面図、
第5図は富ガスおよび貧ガスによる半分に分割し
た加熱系の縦断面図である。 2,23……隔壁、3,3a,30,30a,
340,370……スライドレンガ、7,70,
320……つなぎ壁通路、4,5,6,40,6
0,250,310……つなぎ壁、8,80,3
30……出口開口、10,10a,100,28
0,300……炎道、18……炉室、19……側
壁、20……富ガスノズル。
Figure 1 is a vertical sectional view of the four-flame duct heating system, Figure 2 is a vertical sectional view of the connecting wall passage in Figure 1, perpendicular to Figure 1, and Figure 3 is a plan view of the flame duct in Figure 1. Figure 4 is a longitudinal cross-sectional view of a four-flame heating system using rich gas and poor gas.
FIG. 5 is a longitudinal sectional view of a heating system divided into halves with rich gas and poor gas. 2, 23... partition wall, 3, 3a, 30, 30a,
340,370...slide brick, 7,70,
320... Connecting wall passage, 4, 5, 6, 40, 6
0,250,310...Connecting wall, 8,80,3
30...Exit opening, 10, 10a, 100, 28
0,300...flame path, 18...furnace chamber, 19...side wall, 20...rich gas nozzle.

Claims (1)

【特許請求の範囲】 1 空気または貧ガスの予熱および排熱の回収の
ため炉の全長にわたつて走る蓄熱室、加熱炎道高
さにわたつて分布する加熱炎道への出口スリツト
を備える、加熱炎道つなぎ壁内の通路を通る空気
または空気および貧ガスの供給装置ならびに加熱
炎道への富ガス供給装置を有する富ガスおよび貧
ガスで加熱可能の蓄熱式コークス炉バツテリの加
熱装置において、つなぎ壁4,5,40,310
内を空気供給のためのみのつなぎ壁通路7,7
a,70,320がつなぎ壁の上端まで通じ、か
つ上部水平通路220へのまたは加熱ガスがその
流れの方向500,600,700を上向き流れ
から下向流れもしくはその反対に変化するつなぎ
壁上の加熱ガス反転部21,210への出口開口
8,80,330を有し、出口開口8,80,3
30の断面が制御可能に形成されていることを特
徴とする蓄熱式コークス炉バツテリの加熱装置。 2 出口開口8,80,330がスライドレンガ
3,30,340を備えている特許請求の範囲第
1項記載の装置。
[Scope of Claims] 1. A regenerator running over the entire length of the furnace for preheating the air or lean gas and recovering waste heat, with outlet slits to the heating flame duct distributed over the height of the heating flame duct. In a heating device for a regenerative coke oven battery capable of being heated with rich gas and lean gas, the heating device has a device for supplying air or air and a lean gas through a passage in a connecting wall of the heating flame path, and a device for supplying rich gas to the heating flame path, Connecting wall 4, 5, 40, 310
Connecting wall passages 7, 7 for internal air supply only
a, 70, 320 to the upper end of the tie wall and to the upper horizontal passage 220 or on the tie wall where the heated gas changes its direction of flow 500, 600, 700 from upward flow to downward flow or vice versa. It has an outlet opening 8, 80, 330 to the heated gas reversal section 21, 210;
A heating device for a regenerative coke oven battery, characterized in that a cross section of 30 is formed in a controllable manner. 2. Device according to claim 1, in which the outlet opening 8, 80, 330 is provided with a sliding brick 3, 30, 340.
JP59053684A 1983-03-22 1984-03-22 Device for heating regeneration type coke oven battery Granted JPS59179692A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3310243A DE3310243C2 (en) 1983-03-22 1983-03-22 Heating device for regenerative coking furnace batteries
DE3310243.0 1983-03-22

Publications (2)

Publication Number Publication Date
JPS59179692A JPS59179692A (en) 1984-10-12
JPS6158508B2 true JPS6158508B2 (en) 1986-12-11

Family

ID=6194215

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59053684A Granted JPS59179692A (en) 1983-03-22 1984-03-22 Device for heating regeneration type coke oven battery

Country Status (2)

Country Link
JP (1) JPS59179692A (en)
DE (1) DE3310243C2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3446295C1 (en) * 1984-12-19 1986-07-24 Carl Still Gmbh & Co Kg, 4350 Recklinghausen Device for adjusting the distribution of the heating media in coking ovens

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1671356A1 (en) * 1967-08-03 1972-03-09 Pkm Kohleverarbeitung Veb Process and device for the uniform heating of coke ovens

Also Published As

Publication number Publication date
DE3310243C2 (en) 1985-05-30
JPS59179692A (en) 1984-10-12
DE3310243A1 (en) 1984-10-04

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