JPH07292370A - Coal gasification furnace device - Google Patents

Coal gasification furnace device

Info

Publication number
JPH07292370A
JPH07292370A JP11036294A JP11036294A JPH07292370A JP H07292370 A JPH07292370 A JP H07292370A JP 11036294 A JP11036294 A JP 11036294A JP 11036294 A JP11036294 A JP 11036294A JP H07292370 A JPH07292370 A JP H07292370A
Authority
JP
Japan
Prior art keywords
duct
pressure
char
reductor
combustor
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.)
Granted
Application number
JP11036294A
Other languages
Japanese (ja)
Other versions
JP2559339B2 (en
Inventor
Shunpei Nozoe
浚平 野添
Tatsuo Ino
辰夫 井野
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.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki Heavy Industries Ltd
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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP6110362A priority Critical patent/JP2559339B2/en
Publication of JPH07292370A publication Critical patent/JPH07292370A/en
Application granted granted Critical
Publication of JP2559339B2 publication Critical patent/JP2559339B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To provide a coal gasification device capable of avoiding variability of pressure in a pressure combustion device caused by periodic fall of char resulting from adhesion and growth of char on a reductor (reaction column) wall of the coal gasification device and being stably operated. CONSTITUTION:A pressure combustor 2 and an L duct 3 connected to the combustor 2 are put in pressure containers 1. A reductor 5 connected through a coupling duct 4 to the L duct 3 is put in the other pressure container 1'. Both the pressure containers are coupled with a piping and the reductor 5 is installed vertically downward. A gas route 7 is arranged at one side of the lower part of the reductor 5 and a dust hopper 8 is laid at the lower end of the reductor to provide the objective coal gasification device.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、石炭ガス化炉の本体で
ある加圧燃焼器を耐圧容器に入れた石炭ガス化炉の運転
を安定して行う為の石炭ガス化炉装置に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a coal gasification furnace device for stably operating a coal gasification furnace in which a pressurized combustor, which is the body of a coal gasification furnace, is placed in a pressure vessel. is there.

【0002】[0002]

【従来の技術】従来より石炭ガス化炉は、図2に示すよ
うに耐圧容器1に入れた加圧燃焼器2のLダクト3に上
向きに連なるディフューザ4の上部にリダクタ(反応
塔)5を設ける構造が一般的である(先行技術文献とし
て特願平5−237882号公報がある)。
2. Description of the Related Art Conventionally, as shown in FIG. 2, in a coal gasification furnace, a reducer (reaction tower) 5 is provided above a diffuser 4 which is upwardly connected to an L duct 3 of a pressurized combustor 2 contained in a pressure vessel 1. The structure is generally provided (as a prior art document, there is Japanese Patent Application No. 5-237882).

【0003】この石炭ガス化炉は、加圧燃焼器2内で理
論空気量より少ない空気で投入した微粉炭の一部を燃焼
し、その時の熱により残りの微粉炭をリダクタ5でガス
化するものである。
In this coal gasifier, a portion of the pulverized coal charged with less than the theoretical amount of air is burned in the pressurized combustor 2, and the remaining pulverized coal is gasified by the reducer 5 by the heat at that time. It is a thing.

【0004】ところで、加圧燃焼器2内に投入された微
粉炭の一部とLダクト3に投入された微粉炭の一部がチ
ャーとして生成ガスと一緒に排出される。その際、リダ
クタ壁にチャーが付着成長し、周期的に脱落を繰り返す
場合がある。
By the way, part of the pulverized coal charged in the pressurized combustor 2 and part of the pulverized coal charged in the L duct 3 are discharged together with the produced gas as char. At that time, char may adhere to and grow on the wall of the reducer, and the char may drop off periodically.

【0005】このような場合、脱落チャーがLダクト3
の入口でガス流れをチョークし、加圧燃焼器2内の圧力
が大きく変動し、生成ガス発熱量の変動、水封切れの問
題が生じ、ひいては運転の継続が困難となる恐れがあ
る。
In such a case, the dropped char is the L duct 3
There is a possibility that the gas flow is choked at the inlet of the valve, the pressure inside the pressurized combustor 2 fluctuates greatly, the fluctuation of the generated gas calorific value and the problem of water shutoff occur, and it becomes difficult to continue the operation.

【0006】[0006]

【発明が解決しようとする課題】そこで本発明は、リダ
クタ壁でのチャーの付着成長の結果生じる周期的なチャ
ーの脱落による加圧燃焼器内の圧力変動を回避すること
のできる石炭ガス化炉装置を提供しようとするものであ
る。
SUMMARY OF THE INVENTION Therefore, the present invention is directed to a coal gasification furnace capable of avoiding pressure fluctuations in a pressurized combustor due to periodic char drop-off resulting from char sticking growth on a reductor wall. It is intended to provide a device.

【0007】[0007]

【課題を解決するための手段】上記課題を解決するため
の本発明の石炭ガス化炉装置は、加圧燃焼器と同燃焼器
に連なるLダクトを耐圧容器に入れ、Lダクトに連絡ダ
クトを介して連なるリダクタを別の耐圧容器に入れると
共に両耐圧容器を配管で結び、前記リダクタを下方に向
けて垂直に設け、このリダクタの下部一側にガス通路を
設け、下端にダストホッパを設けてなるものである。上
記Lダクトに連なる連絡ダクトは、ガス流れ方向に対し
上向き又は下向きの傾斜をもって設けられている。
In a coal gasifier apparatus of the present invention for solving the above problems, a pressurized combustor and an L duct connected to the combustor are put in a pressure resistant container, and a communication duct is connected to the L duct. The reducer connected via another is placed in another pressure vessel, both pressure vessels are connected by piping, the reducer is provided vertically downward, a gas passage is provided at one lower side of the reducer, and a dust hopper is provided at the lower end. It is a thing. The communication duct connected to the L duct is provided so as to be inclined upward or downward with respect to the gas flow direction.

【0008】[0008]

【作用】上記のように構成された本発明の石炭ガス化炉
装置によると、加圧燃焼器内に投入された微粉炭の一部
とLダクトに投入された微粉炭の一部がチャーとして生
成ガスと一緒にLダクトを通って上部に抜け出た後、1
80度反転し、ガス流れがリダクタで下向流となり、下
部一側のガス通路を通ってガスクーラーへと流れ、冷却
される。リダクタ壁では生成ガス中のチャーが付着成長
し、周期的に脱落を繰り返すが、脱落したチャーはダス
トホッパに受けられ、ここから加圧燃焼器へリサイクル
され、未燃チャーの熱量の有効回収が行われる。
According to the coal gasifier apparatus of the present invention configured as described above, a part of the pulverized coal charged in the pressurized combustor and a part of the pulverized coal charged in the L duct serve as char. After exiting to the upper part through the L duct together with the produced gas, 1
After reversing by 80 degrees, the gas flow becomes a downward flow by the reducer, flows through the gas passage on the lower one side to the gas cooler, and is cooled. The char in the generated gas adheres and grows on the reductor wall and periodically drops off.The dropped char is received by the dust hopper and recycled to the pressure combustor, where the heat of unburned char is effectively recovered. Be seen.

【0009】このようにリダクタ壁でのチャーの付着成
長の結果生じる周期的な脱落があってもダストホッパに
受けられるので、従来のようにLダクトの入口でガス流
れをチョークすることが無く、加圧燃焼器内の圧力が大
きく変動することが無い。
As described above, even if there is a periodic drop-off resulting from the adhesion and growth of char on the reducer wall, it can be received by the dust hopper, so that there is no choking of the gas flow at the inlet of the L duct unlike the conventional case, The pressure inside the pressure combustor does not fluctuate significantly.

【0010】[0010]

【実施例】本発明の石炭ガス化炉装置の一実施例を図に
よって説明すると、図1に示すように加圧燃焼器2を耐
圧容器1に入れた石炭ガス化炉6を建屋上部に設置し、
前記加圧燃焼器2のLダクト3に連なる連絡ダクト4を
ガス流れ方向に対し上向き(又は下向き)の傾斜を持た
せて設け、この連絡ダクト4に連なるリダクタ(反応
塔)5を下方に向けて垂直に設け、このリダクタ5の下
部外周の一側にガス通路7を設け、下端にダストホッパ
8を設けている。前記リダクタ5は、前記耐圧容器1に
配管1aで連結された耐圧容器1′に入れられている。
前記ガス通路7は、途中に高温の生成ガスを冷却するガ
スクーラー9、生成ガスに含まれる不純物を取り除くガ
ス精製装置10としてサイクロン10a、セラミックフ
ィルタ10bが設けられて、生成ガスを燃料とするガス
タービン発電装置(必ずしも発電でなくとも良い)11
に接続されている。12はガスタービン発電装置11の
圧縮機からの圧縮空気の一部を更に圧力を高めて加圧燃
焼器2に空気を供給する圧縮機であり、13はガスター
ビン発電装置11の排ガスの熱を回収する排ガスボイラ
である。14は排ガスボイラ13からの蒸気で駆動され
る蒸気タービン発電装置であり、15は排ガスボイラ1
3からの排ガスを放出する排気装置である。前記ダスト
ホッパ8の下端の切り出し装置16のチャー排出口17
と、前記ガスクーラー9、サイクロン10a、セラミッ
クフィルタ10bからチャーを受け入れたダストタンク
18の下端の切り出し装置19のチャー排出口20は、
加圧燃焼器2へ連なるチャー搬送管22に接続され、こ
のチャー搬送管22は、圧縮機12から加圧空気を加圧
燃焼器2へ供給する燃焼用空気供給管21から分岐した
ものである。
EXAMPLE An example of a coal gasification furnace apparatus of the present invention will be described with reference to the drawing. As shown in FIG. 1, a coal gasification furnace 6 in which a pressurized combustor 2 is placed in a pressure vessel 1 is installed at the top of a building. Then
A connecting duct 4 connected to the L duct 3 of the pressurized combustor 2 is provided with an upward (or downward) inclination with respect to the gas flow direction, and a reducer (reaction tower) 5 connected to the connecting duct 4 is directed downward. The gas passage 7 is provided on one side of the lower outer periphery of the reductor 5, and the dust hopper 8 is provided at the lower end. The reducer 5 is placed in a pressure resistant container 1 ′ connected to the pressure resistant container 1 by a pipe 1 a.
The gas passage 7 is provided with a gas cooler 9 for cooling the high-temperature generated gas, a cyclone 10a as a gas refining device 10 for removing impurities contained in the generated gas, and a ceramic filter 10b, and uses the generated gas as a fuel. Turbine power generator (not necessarily power generation) 11
It is connected to the. Reference numeral 12 is a compressor for further increasing the pressure of a part of the compressed air from the compressor of the gas turbine power generator 11 to supply air to the pressurized combustor 2, and 13 is heat of the exhaust gas of the gas turbine power generator 11. It is an exhaust gas boiler to be recovered. Reference numeral 14 is a steam turbine power generator driven by steam from the exhaust gas boiler 13, and 15 is the exhaust gas boiler 1.
It is an exhaust device that discharges the exhaust gas from No. 3. Char discharge port 17 of the cutting device 16 at the lower end of the dust hopper 8
And the char discharge port 20 of the cutting device 19 at the lower end of the dust tank 18 that has received the char from the gas cooler 9, the cyclone 10a, and the ceramic filter 10b,
It is connected to a char carrying pipe 22 connected to the pressurized combustor 2, and this char carrying pipe 22 is branched from a combustion air supply pipe 21 for supplying pressurized air from the compressor 12 to the pressurized combustor 2. .

【0011】上記のように構成された実施例の石炭ガス
化炉装置によると、加圧燃焼器2内に投入された微粉炭
は圧縮機12からの加圧空気により燃焼され、またLダ
クト3に投入された微粉炭も同様に燃焼されるが、これ
ら微粉炭の一部はチャーとして生成ガスと一緒にLダク
ト3、連絡ダクト4を通って上部へ抜け出た後、180
度屈曲してリダクタ5内を下向きに流れる。そして下部
外周の一側に設けられたガス通路7を通ってガスクーラ
ー9へ流れて冷却される。冷却された生成ガスはサイク
ロン10a、セラミックフィルタ10bで、チャーを始
めとする不純物が取り除かれる。不純物の取り除かれた
生成ガスはガスタービン発電装置11へ送られて発電に
寄与し、排ガスは排ガスボイラ13に送られて熱回収さ
れた後、排気装置15より大気中に排気される。排ガス
ボイラ13で熱回収によって生じた蒸気は蒸気タービン
発電装置14に送られて該装置を駆動する。前記ガスタ
ービン発電装置11の圧縮機で圧縮した空気の一部を圧
縮機12に送って更に圧力を高めた後、加圧燃焼器2に
燃焼用空気として供給する。
According to the coal gasification furnace apparatus of the embodiment constructed as described above, the pulverized coal charged in the pressurized combustor 2 is combusted by the compressed air from the compressor 12, and the L duct 3 is used. Similarly, the pulverized coal charged in the same is combusted, but a part of the pulverized coal is discharged as char together with the produced gas through the L duct 3 and the communication duct 4 to the upper portion, and then 180
It bends once and flows downward in the reductor 5. Then, the gas flows to the gas cooler 9 through the gas passage 7 provided on one side of the lower outer periphery and is cooled. Impurities such as char are removed from the cooled product gas by the cyclone 10a and the ceramic filter 10b. The produced gas from which impurities have been removed is sent to the gas turbine power generator 11 to contribute to power generation, and the exhaust gas is sent to the exhaust gas boiler 13 to recover heat, and then exhausted to the atmosphere from the exhaust device 15. The steam generated by the heat recovery in the exhaust gas boiler 13 is sent to the steam turbine power generation device 14 to drive the device. A part of the air compressed by the compressor of the gas turbine power generator 11 is sent to the compressor 12 to further increase the pressure and then supplied to the pressurized combustor 2 as combustion air.

【0012】前記リダクタ5の内壁面では生成ガス中の
チャーが付着成長し、周期的に脱落を繰り返すが、脱落
したチャーはダストホッパ8に受けられ、ここから切り
出し装置16により切り出され、チャー排出口17から
チャー搬送管22を通して圧縮機12からの加圧空気に
より加圧燃焼器2へリサイクルされ、未燃チャーの燃焼
が行われ、熱量の有効回収が行われる。この脱落チャー
の加圧燃焼器2へのリサイクルの際、ガスクーラー9、
サイクロン10a、セラミックフィルタ10bからダス
トタンク18に受け入れたチャーも切り出し装置19に
より切り出し、チャー排出口20からチャー搬送管22
を通して加圧燃焼器2へリサイクルされる。
The char in the produced gas adheres and grows on the inner wall surface of the reductor 5 and periodically drops off. The dropped char is received by the dust hopper 8 and cut out by the cutting device 16 from the char discharge port. The compressed air from the compressor 12 is recycled to the pressurized combustor 2 through the char transport pipe 22 from the char 17, and the unburned char is burned and the amount of heat is effectively recovered. When recycling the dropped char to the pressure combustor 2, the gas cooler 9,
The char received in the dust tank 18 from the cyclone 10a and the ceramic filter 10b is also cut out by the cut-out device 19, and the char discharge port 20 through the char transport pipe 22.
Is recycled to the pressurized combustor 2.

【0013】上記のようにリダクタ5の内壁面でのチャ
ーの付着成長の結果生じる周期的な脱落があってもダス
トホッパ8に受けられるので、従来のようにLダクト3
の入口でガス流れをチョークすることが無く、加圧燃焼
器2内の圧力が大きく変動することが無い。
As described above, since the dust hopper 8 can receive the periodic dropout caused by the adhesion and growth of the char on the inner wall surface of the reductor 5, the L duct 3 can be received as in the conventional case.
There is no choking of the gas flow at the inlet, and the pressure in the pressurized combustor 2 does not fluctuate significantly.

【0014】[0014]

【発明の効果】以上の通り本発明の石炭ガス化炉装置
は、リダクタを下方に向けて垂直に設け、下端にダスト
ホッパを設けているので、リダクタ壁でのチャーの付着
成長の結果生じる周期的なチャーの脱落があってもダス
トホッパに受けられる。従って、従来のようにLダクト
の入口でガス流をチョークすることが無く、加圧燃焼器
内の圧力が大きく変動することが無いので、安定した運
転ができる。また、ダストホッパに受けた脱落チャー
は、加圧燃焼器へリサイクルすることにより、未燃チャ
ーの燃焼が行われ、熱量の有効回収が行われる。
As described above, in the coal gasification furnace apparatus of the present invention, the reductor is provided vertically downward, and the dust hopper is provided at the lower end. Even if a char falls out, it can be received by the dust hopper. Therefore, unlike the conventional case, the gas flow is not choked at the inlet of the L duct, and the pressure in the pressurized combustor does not fluctuate significantly, so that stable operation can be performed. Further, the fallen char received by the dust hopper is recycled to the pressure combustor, whereby the unburned char is burned and the amount of heat is effectively recovered.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の石炭ガス化炉装置の一実施例を示す概
略図である。
FIG. 1 is a schematic view showing an embodiment of a coal gasification furnace device of the present invention.

【図2】従来の石炭ガス化炉を示す概略図である。FIG. 2 is a schematic view showing a conventional coal gasification furnace.

【符号の説明】[Explanation of symbols]

1,1′ 耐圧容器 1a 配管 2 加圧燃焼器 3 Lダクト 4 連絡ダクト 5 リダクタ 6 石炭ガス化炉 7 ガス通路 8 ダストホッパ 1, 1'Pressure resistant container 1a Piping 2 Pressurized combustor 3 L duct 4 Communication duct 5 Reductor 6 Coal gasifier 7 Gas passage 8 Dust hopper

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 加圧燃焼器と同燃焼器に連なるLダクト
を耐圧容器に入れ、Lダクトに連絡ダクトを介して連な
るリダクタを別の耐圧容器に入れると共に両耐圧容器を
配管で結び、前記リダクタを下方に向けて垂直に設け、
このリダクタの下部一側にガス通路を設け、下端にダス
トホッパを設けてなる石炭ガス化炉装置。
1. A pressure combustor and an L duct connected to the combustor are placed in a pressure resistant container, a reducer connected to the L duct via a communication duct is placed in another pressure resistant container, and both pressure resistant containers are connected by piping. Install the reducer vertically downwards,
A coal gasifier apparatus having a gas passage provided at one side of the lower portion of the reducer and a dust hopper provided at the lower end.
【請求項2】 Lダクトに連なる連絡ダクトがガス流れ
方向に対し上向き又は下向きの傾斜を持って設けられて
いることを特徴とする請求項1記載の石炭ガス化炉装
置。
2. The coal gasification furnace device according to claim 1, wherein the connecting duct connected to the L duct is provided with an inclination upward or downward with respect to the gas flow direction.
JP6110362A 1994-04-26 1994-04-26 Coal gasifier equipment Expired - Lifetime JP2559339B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6110362A JP2559339B2 (en) 1994-04-26 1994-04-26 Coal gasifier equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6110362A JP2559339B2 (en) 1994-04-26 1994-04-26 Coal gasifier equipment

Publications (2)

Publication Number Publication Date
JPH07292370A true JPH07292370A (en) 1995-11-07
JP2559339B2 JP2559339B2 (en) 1996-12-04

Family

ID=14533869

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6110362A Expired - Lifetime JP2559339B2 (en) 1994-04-26 1994-04-26 Coal gasifier equipment

Country Status (1)

Country Link
JP (1) JP2559339B2 (en)

Also Published As

Publication number Publication date
JP2559339B2 (en) 1996-12-04

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