JPH10273680A - Equipment for coal gasification - Google Patents
Equipment for coal gasificationInfo
- Publication number
- JPH10273680A JPH10273680A JP7843497A JP7843497A JPH10273680A JP H10273680 A JPH10273680 A JP H10273680A JP 7843497 A JP7843497 A JP 7843497A JP 7843497 A JP7843497 A JP 7843497A JP H10273680 A JPH10273680 A JP H10273680A
- Authority
- JP
- Japan
- Prior art keywords
- cooling water
- slag
- cooling
- hopper
- water tank
- 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.)
- Pending
Links
Landscapes
- Gasification And Melting Of Waste (AREA)
Abstract
Description
【０００１】[0001]
【発明の属する技術分野】本発明は、石炭及び炭素質固
体を加熱して熱分解させる石炭ガス化設備に関するもの
である。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a coal gasification facility for heating coal and carbonaceous solids for pyrolysis.
【０００２】[0002]
【従来の技術】微粉炭やその他の炭素質固体を熱分解に
よってガス化してこれを回収し、エネルギ源として利用
するため、従来から石炭ガス化のための設備が利用され
ている。この設備は、微粉炭等の原料をガス化炉の中に
装入し、酸素含有ガス及び高温蒸気を供給することによ
って部分燃焼させて熱分解し、この熱分解によって発生
ガスを回収するものである。このような石炭ガス化炉で
は、ガス化反応が行われると、微粉炭等の原料に含まれ
る無機成分が溶融し、溶融したスラグが炉壁を伝って流
下する。2. Description of the Related Art In order to gasify pulverized coal and other carbonaceous solids by pyrolysis, collect the gas, and use it as an energy source, equipment for coal gasification has conventionally been used. In this facility, raw materials such as pulverized coal are charged into a gasification furnace, supplied with an oxygen-containing gas and high-temperature steam to partially burn and thermally decompose, and the generated gas is recovered by this pyrolysis. is there. In such a coal gasifier, when the gasification reaction is performed, the inorganic components contained in the raw material such as pulverized coal are melted, and the molten slag flows down the furnace wall.
【０００３】円滑に連続運転を行うためには、溶融した
スラグを連続的に系外に排出する必要がある。そこで、
ガス化炉下部にスラグタップを設けスラグタップより溶
融スラグを流下させ、スラグ冷却ホッパにて水砕し、系
外に水砕スラグを排出することが提案されている。冷却
水は、温度の上昇及び蒸発による発生ガスへの混入を避
けるため、循環されることが提案されている。In order to smoothly perform continuous operation, it is necessary to continuously discharge molten slag out of the system. Therefore,
It has been proposed to provide a slag tap at the lower part of the gasification furnace, allow molten slag to flow down from the slag tap, granulate with a slag cooling hopper, and discharge the granulated slag outside the system. It has been proposed that the cooling water be circulated in order to avoid mixing into the generated gas due to temperature rise and evaporation.
【０００４】ところが、このようなガス化炉では、ガス
化反応が行われると、熱分解によってガス化すべき微粉
炭やその他の炭素質個体の一部がガス化されずにガス化
炉下部に開口したスラグタップを通じてスラグ冷却ホッ
パに落下する。これらの一度高温の熱履歴を受けた微粉
炭や炭素質個体は、非常に嵩密度が低く疎水性であるた
め、冷却水水面に浮く。さらに、流下してくる溶融スラ
グの落下衝撃にて攪拌され、冷却水と混合され冷却水面
に浮遊する泡状の浮遊物（以下スカムと記載する。）と
なる。極端な場合においては、前記スカムが水面にて成
長し、スラグタップにまで届きスラグタップを閉塞さ
せ、かつスラグタップを冷却するため溶融したスラグが
スラグタップ付近で固化し、操業不能に陥るという問題
があった。これらのスカムの発生は、ガス化炉起動時で
ガス化炉炉内温度が低いときに多く発生し、ガス化炉起
動を中断させるという問題があった。However, in such a gasification furnace, when a gasification reaction is performed, part of the pulverized coal or other carbonaceous substances to be gasified by thermal decomposition is not gasified and is opened at the lower part of the gasification furnace. The slag tap falls into the slag cooling hopper. Pulverized coal or carbonaceous solids that have once undergone a high-temperature heat history have a very low bulk density and are hydrophobic, and therefore float on the surface of the cooling water. Further, the molten slag flowing down is stirred by the drop impact, mixed with the cooling water, and becomes a foamy floating substance (hereinafter referred to as scum) floating on the cooling water surface. In an extreme case, the scum grows on the surface of the water, reaches the slag tap, closes the slag tap, and the slag melts to cool the slag tap, solidifying near the slag tap, causing an operation failure. was there. These scums are frequently generated when the temperature in the gasification furnace is low at the time of starting the gasification furnace, and there is a problem that the start of the gasification furnace is interrupted.
【０００５】冷却水を循環しているスラグ冷却ホッパに
おいては、前記スカムを冷却水水面近傍に開口した排水
口より冷却水と共に排出することが可能であるが、前記
スカムが水面に浮遊しているため、ガス化炉内の発生ガ
スと共に排出せざるを得ず、冷却水配水系の大気解放口
で、ガス化炉内の発生ガスが大量に漏れる問題があっ
た。In a slag cooling hopper that circulates cooling water, the scum can be discharged together with the cooling water from a drain port opened near the surface of the cooling water, but the scum is floating on the water surface. For this reason, the gas generated in the gasification furnace must be discharged together with the generated gas, and a large amount of the gas generated in the gasification furnace leaks from the air opening of the cooling water distribution system.
【０００６】[0006]
【発明が解決しようとする課題】そこで、本発明が解決
すべき課題は、前記スカムに操業を阻害されることのな
い石炭ガス化炉を提供する事にある。SUMMARY OF THE INVENTION An object of the present invention is to provide a coal gasifier which is not hindered by the scum.
【０００７】[0007]
【課題を解決するための手段】前記課題を解決するた
め、本発明は、石炭及び炭素質固体を酸化剤で部分燃焼
させガス化し、かつ、前記石炭及び炭素質固体の灰を溶
融スラグ化させるガス化炉と、該ガス化炉から流下する
溶融スラグを水砕化するスラグ冷却ホッパを具備した石
炭ガス化設備において、該スラグ冷却ホッパの冷却水水
面近傍に開口した冷却水排水口と連絡管にて該スラグ冷
却ホッパと連結され、かつ、冷却水排水口を備えた冷却
水タンクを設けたことを特徴とする石炭ガス化設備を要
旨とする。SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention is to partially burn coal and carbonaceous solids with an oxidizing agent to gasify them, and to melt the ash of the coals and carbonaceous solids into molten slag. In a coal gasification facility equipped with a gasification furnace and a slag cooling hopper for granulating molten slag flowing down from the gasification furnace, a cooling water discharge port and a communication pipe opened near a cooling water surface of the slag cooling hopper. And a cooling water tank provided with a cooling water discharge port connected to the slag cooling hopper.
【０００８】[0008]
【発明の実施の形態】以下、本発明を図面に示す実施例
を参照しながら具体的に説明する。図１は、本発明の石
炭ガス化設備の実施例を示すものである。ガス化炉１に
は石炭とＯ2 ガスを供給する石炭バーナ３が設けられて
いる。ガス化炉１下部にはスラグタップ４の加熱用スラ
グタップバーナー５とガス化炉１から流下する溶融スラ
グを水砕化するスラグ冷却ホッパ２が設けられている。
スラグ冷却ホッパ２には、冷却水補給管６と冷却水水面
近傍に開口した連絡管７と冷却水排水口９を設け連絡管
７にてスラグ冷却ホッパと連結された冷却水タンク８が
設けられている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be specifically described below with reference to embodiments shown in the drawings. FIG. 1 shows an embodiment of the coal gasification facility of the present invention. The gasifier 1 is provided with a coal burner 3 for supplying coal and O 2 gas. A slag tap burner 5 for heating the slag tap 4 and a slag cooling hopper 2 for granulating molten slag flowing down from the gasification furnace 1 are provided below the gasification furnace 1.
The slag cooling hopper 2 is provided with a cooling water supply pipe 6, a communication pipe 7 opened near the surface of the cooling water, and a cooling water tank 8 connected to the slag cooling hopper through the communication pipe 7. ing.
【０００９】次に、この実施例の操作方法について説明
する。ガス化設備の運転時に、冷却水水面近傍に開口し
た連絡口７−１より冷却水が前記スカムを同伴して連絡
管７−２を通じて冷却水タンク８に導かれる。冷却水タ
ンク８に導かれた冷却水は、冷却水タンク８に設けられ
た排水口９を通じて排水される。冷却水タンク８が空に
ならないように運転することにより、前記スカムは、冷
却水タンク８にのみ滞留し、スラグ冷却ホッパ２には滞
留せずガス化設備の運転支障をきたすことがなく、か
つ、ガス化炉１炉内の発生ガスを漏洩させることがな
い。冷却水タンク８に設けられた冷却水排水口９から
は、前記スカムを含まない冷却水のみを得ることが可能
となる。前記スカムの流動性が悪い、もしくは、発生量
が多い場合には、連絡管７−２に傾斜を設けることも有
用である。Next, the operation method of this embodiment will be described. During operation of the gasification facility, the cooling water is guided to the cooling water tank 8 through the communication pipe 7-2 along with the scum through the communication port 7-1 opened near the surface of the cooling water. The cooling water guided to the cooling water tank 8 is drained through a drain port 9 provided in the cooling water tank 8. By operating so that the cooling water tank 8 does not become empty, the scum stays only in the cooling water tank 8, does not stay in the slag cooling hopper 2 and does not hinder the operation of the gasification facility, and In addition, the gas generated in the gasifier 1 does not leak. From the cooling water discharge port 9 provided in the cooling water tank 8, only the cooling water not containing the scum can be obtained. When the fluidity of the scum is poor or the amount of generated scum is large, it is also useful to provide the connecting pipe 7-2 with an inclination.
【００１０】別の実施例を図２に示す。前記連絡管７−
２に遮断弁１０を設けている。通常運転時は、遮断弁１
０は開にしておく。定期的もしくは不定期に遮断弁１０
を閉にし、同時にスラグ冷却ホッパ２への冷却水補給を
停止する。次に、冷却水タンク８上部空間をＮ2 でパー
ジして冷却水タンク８内の冷却水全量を冷却水排水口９
より排出することにより、冷却水タンク８に滞留した前
記スカムを、ガス化炉１炉内の発生ガスを漏洩させるこ
となく、系外に排出することが可能となる。また、前記
スカムを系外に排出する際に、冷却水タンク８内へのス
カムの付着を防止し、円滑に排出するために、冷却水タ
ンク８上部にノズル８−１を設け、前記ノズル８−１よ
り水又は溶剤を噴霧することも有用である。Another embodiment is shown in FIG. The connecting pipe 7-
2 is provided with a shutoff valve 10. During normal operation, shut off valve 1
Leave 0 open. Shut-off valve 10 regularly or irregularly
Is closed, and at the same time, the supply of cooling water to the slag cooling hopper 2 is stopped. Next, the upper space of the cooling water tank 8 is purged with N 2 and the entire amount of cooling water in the cooling water tank 8 is discharged to the cooling water discharge port 9.
By discharging the gas, the scum accumulated in the cooling water tank 8 can be discharged out of the system without causing the generated gas in the gasification furnace 1 to leak. When discharging the scum out of the system, a nozzle 8-1 is provided above the cooling water tank 8 in order to prevent scum from adhering into the cooling water tank 8 and smoothly discharge the scum. It is also useful to spray water or a solvent from -1.
【００１１】別の実施例を図３に示す。前記連絡口７−
１とは別にスラグ冷却ホッパ２に遮断弁１１を設けた排
水口１２を開口させている。冷却水タンク８に設けられ
た冷却水排水口９にも遮断弁１３が設けられている。通
常操業時は、連絡管７−２に設けられた遮断弁１０及び
冷却水タンク８の冷却水排水口９に設けられた遮断弁１
３は、開にしておく。また、スラグ冷却ホッパ２の排水
口１２に設けられた遮断弁１１は、閉にしておく。定期
的もしくは不定期に連絡管７−２に設けられた遮断弁１
０を閉にする。同時に冷却水排水口９に設けられた遮断
弁１３を閉にする。その後、別に設けられた排水口１２
に設けられた遮断弁１１を開にする。次に、冷却水タン
ク８上部空間をＮ2 でパージして、再び、冷却水タンク
８の冷却水排水口９に設けられた遮断弁１３を開にし
て、冷却水タンク８内の冷却水全量を冷却水排水口９よ
り排出することにより、冷却水タンク８に滞留した前記
スカムを、スラグ冷却ホッパ２への冷却水補給を止める
ことなく、ガス化炉１炉内の発生ガスの漏洩、冷却水の
温度上昇、蒸発による発生ガスへの混入をさせることな
く、系外に排出することが可能となる。Another embodiment is shown in FIG. The contact 7-
A drain port 12 provided with a shut-off valve 11 is opened in the slag cooling hopper 2 separately from 1. The cooling water drain port 9 provided in the cooling water tank 8 is also provided with a shutoff valve 13. During normal operation, the shut-off valve 10 provided on the connecting pipe 7-2 and the shut-off valve 1 provided on the cooling water discharge port 9 of the cooling water tank 8 are provided.
3 is left open. Further, the shutoff valve 11 provided at the drain port 12 of the slag cooling hopper 2 is closed. Shut-off valve 1 provided on communication pipe 7-2 regularly or irregularly
Close 0. At the same time, the shut-off valve 13 provided at the cooling water outlet 9 is closed. Thereafter, a drain port 12 provided separately is provided.
Is opened. Next, the upper space of the cooling water tank 8 is purged with N 2 , and the shut-off valve 13 provided at the cooling water discharge port 9 of the cooling water tank 8 is opened again, so that the total amount of the cooling water in the cooling water tank 8 is increased. The scum accumulated in the cooling water tank 8 is discharged from the cooling water discharge port 9 so that the gas generated in the gasification furnace 1 can be leaked and cooled without stopping the supply of the cooling water to the slag cooling hopper 2. The water can be discharged out of the system without mixing into the generated gas due to the temperature rise and evaporation of the water.
【００１２】別の実施例を図４に示す。冷却水タンク８
に設けられた冷却水排水口９を冷却水配管１４との２系
統に分け、おのおのに遮断弁１３、遮断弁１５を設けて
いる。通常操業時は、通常操業時は、連絡管７−２に設
けられた遮断弁１０及び冷却水タンク８の冷却水排水口
９に設けられた遮断弁１３は、開にしておき、系統を分
けた冷却排水口１４に設けられた遮断弁１５は、閉にし
ておく。また、冷却ホッパ２の排水口１２に設けられた
遮断弁１１は、閉にしておく。定期的もしくは不定期に
連絡管７に設けられた遮断弁１０を閉にする。同時に冷
却水排水口９に設けられた遮断弁１３を閉にする。その
後、排水口１２に設けられた遮断弁１１を開にする。次
に、冷却水タンク８上部空間をＮ2 でパージし、系統を
分けた冷却排水口１４に設けられた遮断弁１５を開に
し、冷却水タンク８内の冷却水全量を冷却水排水口１４
より排出することにより、冷却水タンク８に滞留した前
記スカムを、スラグ冷却ホッパ２へ冷却水補給を止める
ことなく、ガス化炉１炉内の発生ガスの漏洩、冷却水の
温度上昇、蒸発による発生ガスへの混入をさせることな
く、通常操業時の冷却水と混合させることなくほぼ前記
スカムのみを系外に排出することが可能となる。Another embodiment is shown in FIG. Cooling water tank 8
Is divided into two systems, that is, a cooling water pipe 14 and a shutoff valve 13 and a shutoff valve 15, respectively. During normal operation, during normal operation, the shutoff valve 10 provided on the connecting pipe 7-2 and the shutoff valve 13 provided on the cooling water discharge port 9 of the cooling water tank 8 are kept open to separate the system. The shut-off valve 15 provided in the cooling drain port 14 is kept closed. Further, the shutoff valve 11 provided at the drain port 12 of the cooling hopper 2 is closed. The shutoff valve 10 provided on the communication pipe 7 is closed periodically or irregularly. At the same time, the shut-off valve 13 provided at the cooling water outlet 9 is closed. Thereafter, the shutoff valve 11 provided at the drain port 12 is opened. Next, the upper space of the cooling water tank 8 is purged with N 2 , the shut-off valve 15 provided at the cooling drain port 14 divided into systems is opened, and the entire amount of the cooling water in the cooling water tank 8 is released
By discharging the scum remaining in the cooling water tank 8, the scum accumulated in the cooling water tank 8 can be removed without stopping the supply of the cooling water to the slag cooling hopper 2 due to leakage of generated gas in the gasification furnace 1, temperature rise of the cooling water, and evaporation. Almost only the scum can be discharged out of the system without mixing into the generated gas and without mixing with the cooling water during normal operation.
【００１３】別の実施例を図５に示す。スラグ冷却ホッ
パ２の冷却水水面近傍に冷却水排水用の堰１６を設け、
連絡口７−１を堰の排水側に開口させている。スラグ冷
却ホッパ２内部の冷却水は、堰１６を越えて連絡口７−
１より前記連絡管７−２に導かれることにより、スラグ
冷却ホッパ２内部の冷却水水面に浮遊している前記スカ
ムを選択的に、連絡管７−２を通じて冷却水タンク８に
導くことが可能となる。Another embodiment is shown in FIG. A weir 16 for draining cooling water is provided near the cooling water surface of the slag cooling hopper 2,
The communication port 7-1 is opened on the drain side of the weir. The cooling water inside the slag cooling hopper 2 passes over the weir 16 and reaches the communication port 7-.
1, the scum floating on the surface of the cooling water inside the slag cooling hopper 2 can be selectively guided to the cooling water tank 8 through the connecting pipe 7-2. Becomes
【００１４】[0014]
【発明の効果】上述したように、本発明によれば下記の
効果を奏する。 スラグ冷却ホッパ内部の冷却水水面近傍に開口した冷
却水排水用の連絡口より連絡管にてスラグ冷却ホッパと
連結され、かつ、冷却水排水口を設けた冷却水タンクを
設けることにより、スカムは、スラグ冷却ホッパには滞
留せず冷却水タンクのみに滞留し、円滑なガス化設備の
連続運転が可能となる。As described above, according to the present invention, the following effects can be obtained. By providing a cooling water tank provided with a cooling water drainage port and connected to the slag cooling hopper through a communication pipe from a cooling water drainage communication port opened near the cooling water level inside the slag cooling hopper, However, the slag cooling hopper does not stay in the cooling water tank but stays in the slag cooling hopper.
【００１５】スラグ冷却ホッパ内部の冷却水水面近傍
に開口した冷却水排水用の連絡口より連絡管にてスラグ
冷却ホッパと連結され、かつ、冷却水排水口を設けた冷
却水タンクを設けることにより、ガス化炉炉内の発生ガ
スを漏洩させることがなく、スカムを含まない冷却水排
水を得ることが可能となる。By providing a cooling water tank connected to the slag cooling hopper through a communication pipe through a communication port for cooling water drainage opened in the vicinity of the cooling water level inside the slag cooling hopper and provided with a cooling water drainage port. In addition, it is possible to obtain the scum-free cooling water drainage without causing the generated gas in the gasification furnace to leak.
【００１６】さらに、連絡管に遮断弁を設けることに
より、スカムを系外に排出することが可能となる。Further, by providing a shut-off valve in the communication pipe, it becomes possible to discharge the scum out of the system.
【００１７】さらに、前記連絡口とは別にスラグ冷却
ホッパに遮断弁を設けた排水口を開口させ、冷却水タン
クに設けられた冷却水排水口にも遮断弁を設けることに
より、スカムを、スラグ冷却ホッパへの冷却水補給を止
めることなく、冷却水の温度上昇、蒸発による発生ガス
への混入をさせることなく、系外に排出することが可能
となる。Further, a drain port provided with a shut-off valve is opened in the slag cooling hopper separately from the communication port, and a shut-off valve is also provided in the cooling water drain port provided in the cooling water tank, so that the scum can be removed from the slag. The cooling water can be discharged out of the system without stopping the supply of the cooling water to the cooling hopper, without increasing the temperature of the cooling water and mixing the generated gas by evaporation.
【００１８】さらに、冷却水タンクに設けられた冷却
水排水口を２系統に分け、おのおのに遮断弁を設けてる
ことにより、冷却水と混合させることなくほぼ前記スカ
ムのみを系外に排出することが可能となる。Further, the cooling water drain port provided in the cooling water tank is divided into two systems, and each system is provided with a shutoff valve, so that almost only the scum is discharged out of the system without being mixed with the cooling water. Becomes possible.
【００１９】さらに、スラグ冷却ホッパ内部の冷却水
水面近傍に冷却水排水用の堰を設けることにより、スラ
グ冷却ホッパ内部の冷却水水面に浮遊している前記スカ
ムを選択的に、連絡口より連絡管を通じて冷却水タンク
に導くことが可能となる。Further, by providing a weir for draining cooling water near the surface of the cooling water inside the slag cooling hopper, the scum floating on the surface of the cooling water inside the slag cooling hopper can be selectively communicated from the communication port. It is possible to guide the cooling water tank through the pipe.
【図１】本発明の石炭ガス化炉の実施例を示す概略図で
ある。FIG. 1 is a schematic view showing an embodiment of a coal gasifier according to the present invention.
【図２】本発明の別の石炭ガス化炉の実施例を示す概略
図である。FIG. 2 is a schematic view showing another embodiment of the coal gasifier according to the present invention.
【図３】本発明の別の石炭ガス化炉の実施例を示す概略
図である。FIG. 3 is a schematic view showing another embodiment of the coal gasifier according to the present invention.
【図４】本発明の別の石炭ガス化炉の実施例を示す概略
図である。FIG. 4 is a schematic view showing another embodiment of the coal gasifier according to the present invention.
【図５】本発明の別の石炭ガス化炉の実施例を示す概略
図である。FIG. 5 is a schematic view showing another embodiment of the coal gasifier according to the present invention.
【符号の説明】 １ ガス化炉 ２ スラグ冷却ホッパ ３ 石炭バーナ ４ スラグタップ ５ 加熱用スラグタップバーナ ６ 冷却水補給管 ７−１ 連絡口 ７−２ 連絡管 ８ 冷却水タンク ８−１ ノズル ９ 排水口 １０ 遮断弁 １１ 遮断弁 １２ 排水口 １３ 遮断弁 １４ 排水口 １５ 遮断弁 １６ 堰[Description of Signs] 1 Gasifier 2 Slag cooling hopper 3 Coal burner 4 Slag tap 5 Slag tap burner for heating 6 Cooling water supply pipe 7-1 Connection port 7-2 Communication pipe 8 Cooling water tank 8-1 Nozzle 9 Drainage Mouth 10 Shut-off valve 11 Shut-off valve 12 Drain port 13 Shut-off valve 14 Drain port 15 Shut-off valve 16 Weir
Claims (5)
させガス化し、かつ、前記石炭及び炭素質固体の灰を溶
融スラグ化させるガス化炉と、該ガス化炉から流下する
溶融スラグを水砕化するスラグ冷却ホッパを具備した石
炭ガス化設備において、該スラグ冷却ホッパの冷却水水
面近傍に開口した冷却水排水口と連絡管にて該スラグ冷
却ホッパと連結され、かつ、冷却水排水口を備えた冷却
水タンクを設けたことを特徴とする石炭ガス化設備。A gasification furnace for partially burning coal and carbonaceous solids with an oxidizing agent to gasify the ash of the coals and carbonaceous solids, and a molten slag flowing down from the gasification furnace. In a coal gasification facility equipped with a slag cooling hopper for granulation, the slag cooling hopper is connected to the slag cooling hopper through a cooling water discharge port and a communication pipe opened in the vicinity of a cooling water surface of the slag cooling hopper, and the cooling water drainage is performed. A coal gasification facility comprising a cooling water tank provided with a mouth.
に遮断弁を設けたことを特徴とする請求項１記載の石炭
ガス化設備。2. The coal gasification facility according to claim 1, wherein a shut-off valve is provided between the communication pipe and the cooling water tank drain port.
に遮断弁を設け、かつ、前記連絡管とは別にスラグ冷却
ホッパに遮断弁を設けた排水口を設けたことを特徴とす
る請求項１記載の石炭ガス化設備。3. A slag cooling hopper further comprising a drain valve provided with a shut-off valve separately from said communication pipe, said shut-off valve being provided between said communication pipe and said cooling water tank drain port. Item 4. The coal gasification facility according to Item 1.
に遮断弁を設け、かつ、少なくとも２系統以上の排水配
管を設けた冷却水タンクを有することを特徴とする請求
項１記載の石炭ガス化設備。4. The coal according to claim 1, further comprising a cooling water tank provided with a shut-off valve between the communication pipe and the cooling water tank drain port, and provided with at least two or more drainage pipes. Gasification equipment.
近傍に堰を設けたことを特徴とする請求項１記載の石炭
ガス化設備。5. The coal gasification facility according to claim 1, wherein a weir is provided in the slag cooling hopper near a cooling water surface.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7843497A JPH10273680A (en) | 1997-03-28 | 1997-03-28 | Equipment for coal gasification |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7843497A JPH10273680A (en) | 1997-03-28 | 1997-03-28 | Equipment for coal gasification |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH10273680A true JPH10273680A (en) | 1998-10-13 |
Family
ID=13661949
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7843497A Pending JPH10273680A (en) | 1997-03-28 | 1997-03-28 | Equipment for coal gasification |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH10273680A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9505995B2 (en) | 2011-09-07 | 2016-11-29 | Mitsubishi Hitachi Power Systems, Ltd. | Slag discharge system, gasifier, and gasification power generation apparatus |
| CN111322631A (en) * | 2020-03-13 | 2020-06-23 | 浙江鑫盛永磁科技有限公司 | Combustion chamber ash treatment device based on magnetofluid power generation |
| CN111607433A (en) * | 2019-02-25 | 2020-09-01 | 新能能源有限公司 | Cooling and deslagging method for coal ash |
-
1997
- 1997-03-28 JP JP7843497A patent/JPH10273680A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9505995B2 (en) | 2011-09-07 | 2016-11-29 | Mitsubishi Hitachi Power Systems, Ltd. | Slag discharge system, gasifier, and gasification power generation apparatus |
| CN111607433A (en) * | 2019-02-25 | 2020-09-01 | 新能能源有限公司 | Cooling and deslagging method for coal ash |
| CN111607433B (en) * | 2019-02-25 | 2021-04-30 | 新能能源有限公司 | Cooling and deslagging method for coal ash |
| CN111322631A (en) * | 2020-03-13 | 2020-06-23 | 浙江鑫盛永磁科技有限公司 | Combustion chamber ash treatment device based on magnetofluid power generation |
| CN111322631B (en) * | 2020-03-13 | 2021-12-03 | 浙江鑫盛永磁科技有限公司 | Combustion chamber ash treatment device based on magnetofluid power generation |
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