JPH0562159B2 - - Google Patents
Info
- Publication number
- JPH0562159B2 JPH0562159B2 JP59033920A JP3392084A JPH0562159B2 JP H0562159 B2 JPH0562159 B2 JP H0562159B2 JP 59033920 A JP59033920 A JP 59033920A JP 3392084 A JP3392084 A JP 3392084A JP H0562159 B2 JPH0562159 B2 JP H0562159B2
- Authority
- JP
- Japan
- Prior art keywords
- pipe
- riser pipe
- dry main
- waste gas
- riser
- 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
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Landscapes
- Coke Industry (AREA)
Description
【発明の詳細な説明】
本発明は、炭化室夫々の接続される鉛直配設の
上昇管と、上昇管の上部側端部に水平配設のドラ
イメイン接続管を介して接続されるドライメイン
とを備えるとともに、上昇管とドライメインとの
間に開閉操作自在な締切装置を備えたコークス炉
であつて、炭化室で発生したコークス炉ガスをド
ライメインに集めて回収できるように、かつ、コ
ークス炉ガスの可燃成分が減少すると、締切装置
を閉じて、ドライメインへのガス供給を停止でき
るように構成したコークス炉の改良に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention provides a vertically arranged riser pipe connected to each carbonization chamber, and a dry main connected to the upper end of the riser pipe via a horizontally arranged dry main connecting pipe. A coke oven is equipped with a shutoff device that can be opened and closed between the riser pipe and the dry main, and the coke oven gas generated in the carbonization chamber can be collected in the dry main and recovered. The present invention relates to an improvement in a coke oven configured to close a shutoff device and stop gas supply to a dry main when combustible components of coke oven gas decrease.
従来、締切装置を閉じた後、炭化室からのガス
を上昇管の上端から燃焼させながら大気放散させ
ており、これは、炎によつて炭化室での火落を判
定する等していたためであり、また、締切装置を
閉じてから石灰装入までの時間が比較的短くて、
熱損失がそれ程大きくは無いと認識されていたた
めである。 Conventionally, after the shut-off device was closed, the gas from the carbonization chamber was combusted from the top of the riser pipe and released into the atmosphere. In addition, the time from closing the cofferdam to charging lime is relatively short.
This is because it was recognized that the heat loss was not that large.
しかし、現在では、火落判定のために必ずしも
炎を必要としなくなつており、実際には、上昇管
からの燃焼排ガス放出に起因する熱エネルギーの
無駄がかなりあり、また、炭塵飛散等の作業環境
上に若干の問題もあつた。 However, nowadays, flames are no longer necessary to determine whether a fire has occurred, and in reality, there is a considerable amount of thermal energy wasted due to the release of combustion exhaust gas from the riser, and there is also a large amount of wasted thermal energy due to coal dust scattering, etc. There were also some problems with the working environment.
本発明の目的は、締切装置を閉じてからコーク
ス排出までの間の熱エネルギーの無駄を極めて少
くでき、また、集塵なども容易に行えるようにす
る点にある。 An object of the present invention is to extremely reduce waste of thermal energy from closing the shut-off device to discharging coke, and also to facilitate dust collection.
本発明によるコークス炉の特徴構成は、上昇管
の上部側炭部の上側に、開閉装置を介して鉛直配
設の上昇管延出部を夫々設け、上昇管延出管の上
部側炭部を水平配設の廃ガス接続管にて排ガス回
収管に接続し、排ガス回収管に熱回収装置と集塵
装置を記載順に設備してあることにあり、その作
用結果は次の通りである。 The characteristic structure of the coke oven according to the present invention is that vertically arranged riser pipe extension parts are provided above the upper coal part of the riser pipe through opening/closing devices, and the upper coal part of the riser pipe extension pipe is connected to the riser pipe extension part. It is connected to the exhaust gas recovery pipe through a horizontally arranged waste gas connection pipe, and the exhaust gas recovery pipe is equipped with a heat recovery device and a dust collector in the order listed, and the results are as follows.
つまり、締切装置を閉じて、ドライメイによる
コークス炉ガス回収を終えた上昇管において、石
炭装入までの短時間に、開閉装置を開いて、可燃
成分が少くなつた高温のコークス炉ガス、装炭口
などからの空気供給により生成する燃焼ガスを、
廃ガス回収管により熱回収装置に供給し、例え
ば、コークス炉に供給する燃焼用空気の予熱やス
チーム製造等、適当な形態で熱エネルギーを回収
するのである。 In other words, after the shut-off device is closed and the coke oven gas has been recovered by dry may, the switch is opened in the riser pipe for a short period of time before the coal is charged, and the high-temperature coke oven gas with reduced combustible components is removed. Combustion gas generated by supplying air from the mouth, etc.
The waste gas recovery pipe supplies the heat energy to a heat recovery device, where the thermal energy is recovered in a suitable form, for example for preheating combustion air to be fed to a coke oven or for producing steam.
その結果、数十あるいは百数十というように多
数の炭化室夫々に対して、締切装置を閉じてから
コークスを排出するまでの間において、従来無駄
にしていた熱エネルギーを有効に回収でき、ある
工場で試算したところ一炭室当り6000kcal/h程
度の熱エネルギーを有効利用でき、全体として、
経済面及び省エネルギー面で極めて有利に操業で
きることが判つた。 As a result, thermal energy that was previously wasted can be effectively recovered from the time the shut-off device closes to the time the coke is discharged from each of the dozens or even hundreds of coking chambers. According to calculations made at the factory, approximately 6000kcal/h of heat energy can be effectively used per coal chamber, and overall,
It has been found that operation is extremely advantageous in terms of economy and energy conservation.
また、廃ガス回収管に除塵設備等を接続して、
粉塵飛散等による環境悪化の防止を図ることも容
易にできることが判つた。 In addition, by connecting dust removal equipment to the waste gas recovery pipe,
It has been found that it is possible to easily prevent environmental deterioration due to dust scattering, etc.
さらにこの構成においては、上昇管と上昇管延
出部は、鉛直方向に直結される。さらに、上昇管
と上昇管延出部との夫々の上端部位より、夫々独
立に、ほぼ水平配設のドライメイン接続管、廃ガ
ス接続を設けて所定部位へのガスの導入を図つて
いる。従つて、この構成においては、廃ガスを廃
ガス回収管に導く場合に、このガス中に比較的多
量に含有されている炭塵が、ドライメイン側へは
侵入しにくい。 Furthermore, in this configuration, the riser pipe and the riser pipe extension are directly connected in the vertical direction. Further, from the upper end portions of the riser pipe and the riser pipe extension, a dry main connection pipe and a waste gas connection are provided, which are disposed substantially horizontally, independently of each other, to introduce gas into predetermined portions. Therefore, in this configuration, when the waste gas is led to the waste gas recovery pipe, coal dust contained in a relatively large amount in the gas is difficult to enter the dry main side.
さらに、上昇管および上昇管延出部が鉛直方向
において、ほぼ直結した構造となつているため、
この部位を上昇管延出部の頂部から清掃作業等を
容易におこなうこができる。 Furthermore, since the riser pipe and the riser pipe extension are almost directly connected in the vertical direction,
This area can be easily cleaned from the top of the rising pipe extension.
次に、実施例を示す。 Next, examples will be shown.
第1図に示すように、炉体1内に多数の炭化室
2と燃焼室3を交互に配置して形成し、炭化室2
夫々の上部に複数の装炭口4を形成し、装炭口4
に石炭を供給する装炭車5を、炉体1の上部に移
動自在に設け、炭化室2の全てに対して選択的に
装炭車5からコークス原料としての石炭を投入で
きるように構成してある。 As shown in FIG. 1, a large number of carbonization chambers 2 and combustion chambers 3 are arranged and formed alternately in a furnace body 1.
A plurality of coal charging ports 4 are formed in the upper part of each coal charging port 4.
A coal loading car 5 for supplying coal is movably installed in the upper part of the furnace body 1, and is configured such that coal as a raw material for coke can be selectively fed into all of the coking chambers 2 from the coal loading car 5. .
炭化室2の夫々に上昇管6を接続すると共に、
上昇管6の全てにドライメイン7を接続し、燃焼
室3からの熱による石炭の乾留によつて生成する
コークス炉ガスを、上昇管6とドライメイン7に
より精製設備8へ送るように構成してある。 While connecting the riser pipe 6 to each of the carbonization chambers 2,
A dry main 7 is connected to all of the riser pipes 6, and coke oven gas generated by carbonization of coal using heat from the combustion chamber 3 is configured to be sent to the refining equipment 8 through the riser pipes 6 and the dry main 7. There is.
さらに詳細には、第2図に示すように、上昇管
6は鉛直配設されるとともに、この上昇管6の上
部側端部6aに水平配設のドライメイン接続管7
aを介して、前述のドライメイン7が接続され、
上昇管6とドライメイン7との間に開閉操作自在
な締切装置10が備えられている。さらに、上昇
管6の上部側端部6aの上側に、開閉装置11を
介して鉛直配設の上昇管延出部6bを夫々設け、
前記上昇管延出部6bの上部側端部6cを水平配
設の廃ガス接続管9aにて廃ガス回収管9に接続
してあり、さらに、熱回収装置12、集塵装置1
3、ブロワー14及びスタツク15を廃ガス回収
管9に接続し、もつて、締切装置10と開閉装置
11の人為操作によつて、ドライメイン7による
コークス炉ガスの回収が終ると、コークスを炭化
室2から排出し、新たに石炭を挿入するまでの間
において、可燃成分の少い高温のコークス炉ガ
ス、及び、カバー16を外して空気を装炭口4か
ら炭化室2に入れることによつて得られる燃焼ガ
スの有する熱エネルギーを、熱回収装置12によ
り有効利用できるように構成し、それらガスを集
塵装置13で除塵して大気放出できるように構成
してある。 More specifically, as shown in FIG. 2, the riser pipe 6 is arranged vertically, and the dry main connecting pipe 7 is arranged horizontally at the upper end 6a of the riser pipe 6.
The aforementioned dry main 7 is connected via a,
A shutoff device 10 that can be opened and closed is provided between the riser pipe 6 and the dry main 7. Further, vertically arranged riser pipe extension portions 6b are provided above the upper end portion 6a of the riser pipe 6 via the opening/closing device 11, respectively.
The upper end 6c of the riser pipe extension 6b is connected to the waste gas recovery pipe 9 via a horizontally arranged waste gas connection pipe 9a, and further includes a heat recovery device 12 and a dust collector 1.
3. Connect the blower 14 and stack 15 to the waste gas recovery pipe 9, and then, by manual operation of the shutoff device 10 and the opening/closing device 11, when the dry main 7 finishes recovering the coke oven gas, the coke is carbonized. During the period between the discharge from the chamber 2 and the insertion of new coal, high-temperature coke oven gas with low combustible components and air are introduced into the coking chamber 2 through the coal charging port 4 by removing the cover 16. The heat energy contained in the combustion gas thus obtained can be effectively utilized by a heat recovery device 12, and the gas can be removed by a dust collector 13 and released into the atmosphere.
尚、炉体1の横一側方に押出機17をかつ横地
側方に消火車18を、夫々炭化室2並設方向に移
動操作自在に設けて、炭化室2の全てに対して選
択的に、乾留が完了すれば炭化室2内のコークス
を押出機17により消火車18に回収できるよう
に構成してある。 An extruder 17 is installed on one horizontal side of the furnace body 1, and a fire extinguisher 18 is installed on the horizontal side of the furnace body 1, so that they can be moved and operated in the direction in which the carbonization chambers 2 are arranged side by side, so that all of the carbonization chambers 2 can be selectively operated. Furthermore, when the carbonization is completed, the coke in the carbonization chamber 2 can be collected by an extruder 17 into a fire extinguisher 18.
次に、別の実施例を説明する。 Next, another example will be described.
締切装置10及び開閉装置11の具体構造や操
作構成は各種変更自在であり、例えば、それら両
装置10,11を背反的に開閉されるように連係
させたり、あるいは、それら両装置10,11を
炭化室2の状態変化検出に基いて自動的に背反的
に開閉するように構成してもよい。 The specific structure and operation configuration of the closing device 10 and the opening/closing device 11 can be changed in various ways. For example, the two devices 10 and 11 may be linked so that they are opened and closed in a contradictory manner, or the two devices 10 and 11 may be It may be configured to automatically open and close in a contradictory manner based on the detection of a change in the state of the carbonization chamber 2.
熱回収装置12は、燃焼室3に供給する燃焼用
空気の予熱装置、廃熱ボイラー、その他の適当な
ものを1種又は複数種設ければよい。 The heat recovery device 12 may include one or more of a preheating device for combustion air supplied to the combustion chamber 3, a waste heat boiler, and other suitable devices.
集塵装置13は、乾式や湿式、その他適当なも
のを選択利用できるが、場合によつては省略でき
る。 The dust collector 13 can be selected from a dry type, a wet type, or any other suitable type, but may be omitted in some cases.
炉体1に備えられた炭化室2の数、あるいは、
熱回収装置12を接続する炉体1の数は不問であ
る。 The number of carbonization chambers 2 provided in the furnace body 1, or
The number of furnace bodies 1 to which the heat recovery device 12 is connected is not limited.
図面は本発明の実施例を示し、第1図は、コー
クス炉の一部切欠概略平面図、第2図は要部説明
図である。
2……炭化室、6……上昇管、7……ドライメ
イン、9……廃ガス回収管、10……締切装置、
11……開閉装置、12……熱回収装置。
The drawings show an embodiment of the present invention, and FIG. 1 is a partially cutaway schematic plan view of a coke oven, and FIG. 2 is an explanatory view of the main parts. 2... Carbonization chamber, 6... Rising pipe, 7... Dry main, 9... Waste gas recovery pipe, 10... Shutoff device,
11...Switching device, 12...Heat recovery device.
Claims (1)
6と、前記上昇管6の上部側端部6aに水平配設
のドライメイン接続管7aを介して接続されるド
ライメイン7とを備えるとともに、前記上昇管6
と前記ドライメイン7との間に開閉操作自在な締
切装置10を備えたコークス炉であつて、 前記上昇管6の前記上部側端部6aの上側に、
開閉装置11を介して鉛直配設の上昇管延出部6
bを夫々設け、前記上昇管延出部6bの上部側端
部6cを水平配設の廃ガス接続管9aにて廃ガス
回収管9に接続し、前記廃ガス回収管9に熱回収
装置12と集塵装置13を記載順に設備してある
コークス炉。[Scope of Claims] 1. A vertically arranged riser pipe 6 connected to each of the carbonization chambers 2, and a horizontally arranged dry main connecting pipe 7a connected to the upper end 6a of the riser pipe 6. a dry main 7, and the riser pipe 6.
The coke oven is equipped with a shutoff device 10 that can be opened and closed between the dry main 7 and the dry main 7, and above the upper end 6a of the riser pipe 6,
Vertically arranged riser pipe extension part 6 via opening/closing device 11
b, and the upper end 6c of the riser pipe extension 6b is connected to the waste gas recovery pipe 9 through a horizontally arranged waste gas connection pipe 9a, and the heat recovery device 12 is connected to the waste gas recovery pipe 9. A coke oven equipped with a dust collector 13 and a dust collector 13 in the order listed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59033920A JPS60177093A (en) | 1984-02-23 | 1984-02-23 | Coke oven |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59033920A JPS60177093A (en) | 1984-02-23 | 1984-02-23 | Coke oven |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60177093A JPS60177093A (en) | 1985-09-11 |
| JPH0562159B2 true JPH0562159B2 (en) | 1993-09-07 |
Family
ID=12399951
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59033920A Granted JPS60177093A (en) | 1984-02-23 | 1984-02-23 | Coke oven |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60177093A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108504370B (en) * | 2018-05-31 | 2020-04-07 | 武汉钢铁有限公司 | Coke oven carbonization chamber smoke and dust treatment system based on coal gas quality-divided recovery |
| CN113830489A (en) * | 2021-09-07 | 2021-12-24 | 曹昌海 | Slay pipeline is with preventing connecting device that splits |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE795031A (en) * | 1972-02-07 | 1973-05-29 | Waagner Biro Ag | FEEDING PROCESS AND DEVICE FOR COKE OVENS |
| JPS5030902A (en) * | 1973-07-18 | 1975-03-27 | ||
| DE2804934C2 (en) * | 1978-02-06 | 1984-05-10 | Carl Still Gmbh & Co Kg, 4350 Recklinghausen | Device for the separation of gases and solids in the coking of coal |
| JPS6047518B2 (en) * | 1980-08-13 | 1985-10-22 | 三菱重工業株式会社 | Method for recovering heat from crude gas generated in a coke oven |
| JPS58164991A (en) * | 1981-12-01 | 1983-09-29 | Mitsubishi Heavy Ind Ltd | Recovering method for heat of crude gas in cokefurnace |
-
1984
- 1984-02-23 JP JP59033920A patent/JPS60177093A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60177093A (en) | 1985-09-11 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| GB1587050A (en) | Incinerator with means for transferring burning waste through the combustion chamber | |
| JPH0562159B2 (en) | ||
| WO2007014489A1 (en) | A pyrolysis method for treating waste rubber and plastics and materials containing resins | |
| CN101875993B (en) | System for removing dust from converter gas by dry method and using method thereof | |
| CN110746993A (en) | Coupling system and process of tamping coke oven charging soot treatment and coke oven flue gas purification | |
| JP4078771B2 (en) | Waste pyrolysis treatment equipment | |
| US3645854A (en) | Method in byproduct coke oven operation and apparatus for same | |
| CN209636163U (en) | Combined collecting system for coal-charging coke-discharging dust gas and graphite-burning waste gas | |
| CN104673335B (en) | Ladder regenerative mixed combustion chamber smoke elimination and energy-saving vehicle | |
| CN212408639U (en) | Ash discharge device of circulating fluidized bed boiler settling chamber | |
| WO2014023211A1 (en) | Dry quenching device for a coal pyrolysis furnace | |
| US4265709A (en) | Method and apparatus for separating gases and solids during the carbonization of coal | |
| JP2995395B2 (en) | Waste tire chip dry distillation gas collection method | |
| GB1460735A (en) | Coking ovens | |
| CN1908120B (en) | Waste rubber and plastic goods and processing method of cracking goods containing resin component | |
| JPS6314033B2 (en) | ||
| JP3819615B2 (en) | Waste carbonization pyrolysis melting combustion equipment | |
| CN109517608A (en) | Combined collecting system for coal-charging coke-discharging dust gas and graphite-burning waste gas | |
| CN204454989U (en) | Ladder regenerative mixed combustion chamber smoke elimination and energy-saving vehicle | |
| CN206320752U (en) | Large Copacity high temperature garbage gasification jet burning system | |
| CN205099623U (en) | Coke oven carbomorphism room graphite sweeper | |
| CN111649321A (en) | Ash discharge device and ash discharge method for settling chamber of circulating fluidized bed boiler | |
| CN116412662B (en) | Method for drying kiln refractory material by using double-hearth kiln flue gas | |
| CN203123958U (en) | Chemical reaction furnace utilizing solid fuel | |
| CN2516553Y (en) | Vertical coke oven without recovery and using tamping coal |