JPS6034001B2 - Energy recovery device from red-hot coke extinguishing equipment - Google Patents
Energy recovery device from red-hot coke extinguishing equipmentInfo
- Publication number
- JPS6034001B2 JPS6034001B2 JP3897380A JP3897380A JPS6034001B2 JP S6034001 B2 JPS6034001 B2 JP S6034001B2 JP 3897380 A JP3897380 A JP 3897380A JP 3897380 A JP3897380 A JP 3897380A JP S6034001 B2 JPS6034001 B2 JP S6034001B2
- Authority
- JP
- Japan
- Prior art keywords
- steam
- red
- hot coke
- water gas
- container
- 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
Links
- 239000000571 coke Substances 0.000 title claims description 27
- 238000011084 recovery Methods 0.000 title claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 25
- 238000010248 power generation Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 description 20
- 238000000034 method Methods 0.000 description 6
- 238000009835 boiling Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000003763 carbonization Methods 0.000 description 1
- 238000010000 carbonizing Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
Landscapes
- Engine Equipment That Uses Special Cycles (AREA)
Description
【発明の詳細な説明】
本発明は赤熱コークスを消火する際発生する高温の蒸気
を利用してェネルギを回収する装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for recovering energy by utilizing high temperature steam generated when extinguishing red-hot coke.
従来、コークス炉から赤熱した状態のコークスはコーク
ス消火車によって消火塔内に運搬され、そこで散水し冷
却される。Conventionally, red-hot coke from a coke oven is transported by a coke fire extinguishing truck to a fire extinguishing tower, where it is cooled by water spraying.
その際高温の蒸気が一度に多量に発生し、消火塔の頂部
から無駄に放散される。この高温の蒸気のもつ多量の熱
は、大気中に放散されているために有効利用ができない
。At this time, a large amount of high-temperature steam is generated at once and is wasted away from the top of the fire tower. The large amount of heat contained in this high-temperature steam cannot be used effectively because it is dissipated into the atmosphere.
このため赤熱コークスの消火に際して不活性ガスを密閉
循環させてこれで該赤熱コークスを冷却し、この2次熱
源を熱交換器で回収してタービンを駆動し、電力回収を
行う乾式消火というものがあるが、その多大な設備投資
と、運転経費には省エネ設備として適切でなく、その上
その広大な占有面積が必要であるといった欠点があった
。又、従来の消火設備ではコークス炉機械の一押出し作
業工程で赤熱コークスの全量を1つの函体内にうけて消
火することから次の工程迄の蒸気の発生が断続的となり
、発生する蒸気の量や温度が著しく変化することから押
出された蒸気中の熱ェネルギを連続的に回収して再利用
することには大きな問題があった。For this reason, when extinguishing red-hot coke, there is a dry extinguishing method in which inert gas is circulated in a sealed manner to cool the red-hot coke, and this secondary heat source is recovered using a heat exchanger to drive a turbine and recover electricity. However, due to the large capital investment and operating costs, it is not suitable as an energy-saving facility, and it also requires a large area. In addition, in conventional fire extinguishing equipment, the entire amount of red-hot coke is extinguished by receiving it in one box during one extrusion process of the coke oven machine, so the generation of steam until the next process is intermittent, resulting in an increase in the amount of steam generated. There was a big problem in continuously recovering and reusing the heat energy in the extruded steam because the steam and temperature varied significantly.
本発明は上記従釆の欠点を解消すべく発明されたもので
、赤熱コークスを密閉圧力形コンテナで消火する際、そ
こで発生する蒸気の全量を回収して電気ェネルギとして
再利用しようとしたものである。The present invention was invented in order to solve the above-mentioned drawbacks of the conventional method, and aims to recover the entire amount of steam generated when red-hot coke is extinguished in a sealed pressure container and reuse it as electrical energy. be.
又、この発明の他の目的は蒸気の発生が中断した際、そ
の蒸気の温度変化を継続的に維持するようにするために
別途補集した水性ガスを有効に利用することにある。Another object of the present invention is to effectively utilize separately collected water gas in order to continuously maintain the temperature change of the steam when the generation of steam is interrupted.
さらに本発明の他の目的は回収したェネルギを電気ェネ
ルギとして利用することを目的とする。Still another object of the present invention is to utilize the recovered energy as electrical energy.
本発明は赤熱コークスを圧力消火する密閉圧力形コンテ
ナと、この圧力形コンテナから発生する高温の蒸気を熱
交換する熱交換器と、当該圧力形コンテナで消火する際
発生する水性ガスを橘集して貯留する水性ガスタンクと
を有するものにおいて該桶集した水性ガスを燃焼させて
、前記高圧蒸気の発生が中断した時に該水性ガスを燃焼
させて連続したタービン発電が得られるようにしたこと
を特徴とするものである。以下本発明の実施例を図面に
よって説明する。The present invention includes a sealed pressure container for extinguishing red-hot coke under pressure, a heat exchanger for exchanging heat with high-temperature steam generated from the pressure container, and a system for collecting water gas generated when extinguishing the fire in the pressure container. and a water gas tank for storing water gas, the water gas collected in the tank is combusted, and when the generation of high pressure steam is interrupted, the water gas is combusted so that continuous turbine power generation can be obtained. That is. Embodiments of the present invention will be described below with reference to the drawings.
第1図及び第2図において1は石炭を乾留してコークス
を製造するコークス炉、2は赤熱コークスを炉より取り
出す作業を手伝うコークガイド車、3は圧力消火を行う
ように計画された圧力形コンテナ、4は取外し可能な圧
力形コンテナ3の蓋、5は赤熱コークスを消火する際発
生する発塵を除去するためのサイクロン、6は水性ガス
タンク7より水性ガスを供給し、その内部に設備したガ
スバーナ8により蒸気を発生或は加熱再生する装置であ
る。9,9′は熱交換器で、赤熱コークスから発生した
低圧で高温の過熱蒸気で蒸気タービンサイクルに必要な
所定の蒸気を発生させる装置である。In Figures 1 and 2, 1 is a coke oven that produces coke by carbonizing coal, 2 is a coke guide car that helps remove red-hot coke from the oven, and 3 is a pressure type designed to perform pressure extinguishing. Container 4 is a removable lid of pressure type container 3, 5 is a cyclone for removing dust generated when extinguishing red-hot coke, and 6 is a water gas tank 7 that supplies water gas and is installed inside the container. This is a device that generates or heats and regenerates steam using a gas burner 8. Reference numerals 9 and 9' denote heat exchangers, which are devices that generate a predetermined amount of steam necessary for the steam turbine cycle using low-pressure, high-temperature superheated steam generated from red-hot coke.
10は蒸気タービンで、配管11を介して熱交換器9と
接続され、かつ発電機12とも連結されている。Reference numeral 10 denotes a steam turbine, which is connected to a heat exchanger 9 via piping 11 and also to a generator 12.
又、同様に10′は有機媒体タービンで、配管11′を
介して熱交換器9′と接続され、これも又発電機12′
と連結されている。Similarly, 10' is an organic medium turbine, which is connected to a heat exchanger 9' via a pipe 11', which is also connected to a generator 12'.
is connected to.
13,13′はそれぞれ熱交換器9,9′に連結した配
管11,11′およびポンプ14,14′を介して接続
した凝縮器である。Condensers 13 and 13' are connected to heat exchangers 9 and 9' via pipes 11 and 11' and pumps 14 and 14', respectively.
15は水性ガス回収装置で、低圧で高温の発生蒸気中に
混入している水性ガスを回収処理するものである。Reference numeral 15 denotes a water gas recovery device, which recovers and processes water gas mixed in the low-pressure, high-temperature generated steam.
この回収装置15で回収された水性ガスはガスタンク7
内に貯留される。以上のような構成において、所定の乾
留時間を経過したコークス炉1の排出口に、まずガイド
車2ならびに圧力形コンテナ3を搭載した消火車1.6
がセットされ、図示されていない反対側の押出機によっ
て圧力形コンテナ3の中に赤熱コークスが没入される。The water gas recovered by this recovery device 15 is stored in a gas tank 7.
stored within. In the above configuration, the fire extinguishing vehicle 1.6 equipped with the guide wheel 2 and the pressure type container 3 is first placed at the outlet of the coke oven 1 after a predetermined carbonization time has elapsed.
is set, and red-hot coke is immersed into the pressure type container 3 by an extruder on the opposite side (not shown).
次にコンテナの上蓋4が気密に閉じられ上蓋4内に取付
けられたスプレーノズルにより温水が散水された圧力形
コンテナ4内の赤熱コークスが冷却されると圧力形コン
テナ4の下部より瞬時に蒸発或いは加熱された高温の過
熱蒸気が多量に発生することになる。この発生蒸気はコ
ンテナ3の下部にある火格子(図示せず)を通して、外
部のダクトに排出されるように、過熱したコークスの間
を抜けて下方へと導かれる。Next, the top lid 4 of the container is hermetically closed, and when the red hot coke inside the pressure type container 4, which is sprayed with hot water by a spray nozzle installed inside the top lid 4, is cooled, it instantly evaporates or evaporates from the bottom of the pressure type container 4. A large amount of heated, high-temperature superheated steam will be generated. This generated steam is directed downwardly through the superheated coke through a grate (not shown) in the lower part of the container 3 to be discharged to an external duct.
さらにこの発生蒸気は、多量のダストを含有しているの
でこれを分離するためにサイクロン5へと導かれる。サ
イクロン5で除摩された蒸気は蒸気再生器6内を通過し
て熱交換器9内に入る。この熱交換器9内で蒸気タービ
ンサイクル用の蒸気を発生させ、この高圧蒸気が管路1
1を介して蒸気タービン10を駆動し発電機12で発電
して電気ェネルギを得る。蒸気タービン10を通過した
蒸気は凝縮器13で凝縮され、ポンプ14によって熱交
換器9へ再循環される。Furthermore, since this generated steam contains a large amount of dust, it is led to the cyclone 5 to separate it. The steam removed by the cyclone 5 passes through the steam regenerator 6 and enters the heat exchanger 9. Steam for the steam turbine cycle is generated in this heat exchanger 9, and this high pressure steam is transferred to the pipe line 1.
1, a steam turbine 10 is driven, and a generator 12 generates electricity to obtain electric energy. The steam that has passed through the steam turbine 10 is condensed in a condenser 13 and recirculated to the heat exchanger 9 by a pump 14.
一方熱交換器9を経た低温蒸気は第2の熱交換器9′内
へ導入される。ここでは有機媒体タービンサイクル用の
低沸点媒体と熱交換され、この低沸点媒体が蒸発する。On the other hand, the low temperature steam that has passed through the heat exchanger 9 is introduced into the second heat exchanger 9'. Here, heat is exchanged with a low-boiling medium for the organic medium turbine cycle, and this low-boiling medium is evaporated.
以下、上記の蒸気タービンサイクルと同様の作動で有機
媒体タービン10′が駆動され、発電機12′により電
気ェネルギが得られる。熱交換器9′を出た低圧蒸気は
、水性ガス回収装置15により水性ガスが分離される。Thereafter, the organic medium turbine 10' is driven in the same manner as the steam turbine cycle described above, and electric energy is obtained by the generator 12'. Water gas is separated from the low-pressure steam leaving the heat exchanger 9' by a water gas recovery device 15.
ここで分離された水性ガスはガスタンク7内に貯留され
る。一方残された温水は消火コンテナ3内の赤熱コーク
スの消火に再利用することもできる。The water gas separated here is stored in the gas tank 7. On the other hand, the remaining hot water can also be reused to extinguish red-hot coke in the fire extinguishing container 3.
本発明はこうして得られた水性ガスを、断続的に行われ
るコークスの消火作業の中断時に蒸気を連続的に且つ安
定して発生させるように蒸気再生器6内で燃焼させ、蒸
気タービンサイクルで安定した電力が得られるようにし
たものである。The present invention combusts the water gas thus obtained in the steam regenerator 6 so as to continuously and stably generate steam during interruptions in the intermittent coke extinguishing operation, and stabilizes it in the steam turbine cycle. It is designed so that the electric power can be obtained by
この消火方法は圧力形の密閉緑式消火方法であるため、
消火時の熱量が外部へ放出されることなく、有効な回収
利用できる。又温水を再利用するために熱量を外部への
がすことがなく、赤熱コークスの冷却水として循環使用
されるため汚染された水が系外へ殆んど排出されること
がなく利用される。上記の水性ガスバーナ8は熱交換器
9の内部に直かに取付けることもできる。This fire extinguishing method is a pressure-type closed green fire extinguishing method, so
The amount of heat generated during extinguishing a fire is not released to the outside and can be effectively recovered and used. In addition, since hot water is reused, no heat is lost to the outside, and as it is recycled as cooling water for red-hot coke, contaminated water is hardly discharged outside the system. . The water gas burner 8 described above can also be installed directly inside the heat exchanger 9.
第1図はコークス炉まわりの作業機械の配置を示す図、
第2図は本発明の回収ヱネルギ利用装置の概略図である
。
6・・・・・・蒸気再生器、9,9′・・・・・・熱交
換器、10・・・・・・蒸気タービン、10′・・・…
有機媒体夕一ビン、12,12′・・・・・・発電機、
15・・・・・・水性ガス回収装置。
第1図
第2図Figure 1 is a diagram showing the arrangement of working machines around the coke oven.
FIG. 2 is a schematic diagram of the recovered energy utilization device of the present invention. 6...Steam regenerator, 9,9'...Heat exchanger, 10...Steam turbine, 10'...
Organic medium bottle, 12, 12'... Generator,
15...Water gas recovery device. Figure 1 Figure 2
Claims (1)
、該コンテナから発生する高温の蒸気を熱交換する熱交
換器と、該コンテナで圧力消火する際一時的に発生する
水性ガスを捕集し、貯留する水性ガスタンクを有するも
のにおいて、該捕集した水性ガスを前記高温蒸気の発生
が中断している間に、連続的な蒸気の発生が得られるよ
う燃焼させて、連続したタービン発電を得られるように
したことを特徴とする赤熱コークスのエネルギ回収装置
。1. A sealed pressure container for extinguishing red-hot coke under pressure, a heat exchanger for exchanging heat with high-temperature steam generated from the container, and a system for collecting and storing water gas temporarily generated during pressure extinguishing in the container. In a device having a water gas tank, the collected water gas is combusted so as to continuously generate steam while the generation of high temperature steam is interrupted, so that continuous turbine power generation can be obtained. A red-hot coke energy recovery device characterized by:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3897380A JPS6034001B2 (en) | 1980-03-28 | 1980-03-28 | Energy recovery device from red-hot coke extinguishing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3897380A JPS6034001B2 (en) | 1980-03-28 | 1980-03-28 | Energy recovery device from red-hot coke extinguishing equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56137001A JPS56137001A (en) | 1981-10-26 |
| JPS6034001B2 true JPS6034001B2 (en) | 1985-08-06 |
Family
ID=12540092
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3897380A Expired JPS6034001B2 (en) | 1980-03-28 | 1980-03-28 | Energy recovery device from red-hot coke extinguishing equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6034001B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0738354U (en) * | 1993-12-24 | 1995-07-14 | 三龍機工株式会社 | Ridge roof tile |
-
1980
- 1980-03-28 JP JP3897380A patent/JPS6034001B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56137001A (en) | 1981-10-26 |
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