JPH08296973A - Furnace bottom residue discharging apparatus for organic matter gasifying furnace - Google Patents

Furnace bottom residue discharging apparatus for organic matter gasifying furnace

Info

Publication number
JPH08296973A
JPH08296973A JP7105179A JP10517995A JPH08296973A JP H08296973 A JPH08296973 A JP H08296973A JP 7105179 A JP7105179 A JP 7105179A JP 10517995 A JP10517995 A JP 10517995A JP H08296973 A JPH08296973 A JP H08296973A
Authority
JP
Japan
Prior art keywords
furnace
furnace bottom
jet
partition plate
gas supply
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
JP7105179A
Other languages
Japanese (ja)
Other versions
JP3746536B2 (en
Inventor
Shinji Kono
眞司 河野
Masaki Hirano
正樹 平野
Tadashi Sumino
匡 角野
Koichi Yonezawa
鴻一 米沢
Masanori Oraku
正則 大楽
Kenji Tokumasa
賢治 徳政
Yoshibumi Ito
義文 伊藤
Kenji Shinya
謙治 新屋
Masahito Kaneko
雅人 金子
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.)
Kansai Electric Power Co Inc
Chugoku Electric Power Co Inc
Mitsubishi Heavy Industries Ltd
Original Assignee
Kansai Electric Power Co Inc
Chugoku Electric Power Co Inc
Mitsubishi 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 Kansai Electric Power Co Inc, Chugoku Electric Power Co Inc, Mitsubishi Heavy Industries Ltd filed Critical Kansai Electric Power Co Inc
Priority to JP10517995A priority Critical patent/JP3746536B2/en
Publication of JPH08296973A publication Critical patent/JPH08296973A/en
Application granted granted Critical
Publication of JP3746536B2 publication Critical patent/JP3746536B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • 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
    • Y02P10/00Technologies related to metal processing
    • Y02P10/10Reduction of greenhouse gas [GHG] emissions
    • Y02P10/143Reduction of greenhouse gas [GHG] emissions of methane [CH4]

Landscapes

  • Crucibles And Fluidized-Bed Furnaces (AREA)

Abstract

PURPOSE: To prevent an injection hole from being clogged owing to residues by providing a water seal injecting gas supply tube on the lower portion of a furnace bottom opening part, and further providing a furnace bottom partition plate having the injection hole with a smaller cross section than that of the furnace bottom opening part for providing a predetermined injection speed to the injecting gas such that the partition plate is opened/closed in a furnace bottom chamber. CONSTITUTION: A furnace bottom opening part 51b is provided on the lowest part of a furnace bottom part 51a of a gasifying furnace 51 which has a cross section enough to fall down residues 64, and a furnace bottom chamber 1 is disposed on the lower part of the lowest part of the furnace bottom part. An injection outlet 2a is formed in a furnace bottom partition plate 2 which has an opening area capable of providing a predetermined injection speed to injecting gas 62. The furnace bottom partition plate is accommodated in the furnace bottom chamber 1 so as to open downward with the aid of a rotary shaft 3, an arm 5, and a hydraulic cylinder 4. An injecting gas supply tube 8 dipped in a water seal tank 51 in its lower end is disposed on the lower part of the furnace bottom chamber 1, and an injecting gas supply line 56 is mounted on the injecting gas supply pipe 8.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は有機物(重質油、残渣
油、プラスチックなど)の部分ガス化炉における炉底残
渣排出装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a bottom residue discharge device for a partial gasification furnace for organic substances (heavy oil, residual oil, plastic, etc.).

【0002】[0002]

【従来の技術】図6は従来の噴流床型有機物部分ガス化
炉の一例の概念を示す側面図である。図示するように、
装置の始動時にガス化炉51を予熱装置58によって約
700℃に予熱する。次に、噴流用ガス供給ライン56
から、このガス化炉51に水封タンク57によってシー
ルされた噴流用ガス供給管55を介して、例えば窒素ガ
ス、炭酸ガスなどのイナートガスである噴流用ガス62
を常温で供給して炉底部51aから吹き上げるととも
に、水蒸気・酸素(酸素は支燃ガス)供給ライン52及
び原料供給装置54から水蒸気・酸素混合ガス61及び
例えばプラスチック廃棄物を粉砕した有機物原料60を
供給し、噴流用ガス62のガス化炉51内での噴流及び
酸素によって有機物原料60と水蒸気とを反応させてガ
ス化し、メタノール合成の原料用ガス63を生成する。
ガス化炉51内は、この反応熱によって700℃前後の
温度が維持される。
2. Description of the Related Art FIG. 6 is a side view showing the concept of an example of a conventional spouted bed type organic partial gasification furnace. As shown
When starting the apparatus, the gasification furnace 51 is preheated to about 700 ° C. by the preheating device 58. Next, the jet gas supply line 56
From the gasification furnace 51 via a jet gas supply pipe 55 sealed by a water sealing tank 57, for example, a jet gas 62 which is an inert gas such as nitrogen gas or carbon dioxide gas.
Is supplied at room temperature and blown up from the furnace bottom portion 51a, and a steam / oxygen (oxygen is a combustion-supporting gas) supply line 52 and a raw material supply device 54 are mixed with a steam / oxygen mixed gas 61 and an organic raw material 60 obtained by crushing, for example, plastic waste. The organic material raw material 60 and the steam are reacted and gasified by the jet flow of the jet gas 62 in the gasification furnace 51 and oxygen, and the raw material gas 63 for methanol synthesis is generated.
The temperature of around 700 ° C. is maintained in the gasification furnace 51 by this reaction heat.

【0003】[0003]

【発明が解決しようとする課題】前述した従来の噴流床
型のガス化炉51では、噴流用ガス62を炉底部51a
から炉内に吹き上げるときのガス速度は炉内の噴流速度
以上に設定する必要がある。また、噴流用ガス62に
は、反応に関与しない常温のイナートガスを用いている
ので,この流量が多くなると反応場の温度が低下してガ
ス化反応が維持できなくなる。一方、前記噴流速度は一
定の値以上が必要であるから、噴流用ガス62の噴出流
速を低下させないためには、炉底部51aの噴流口の断
面積(噴流用ガス供給管55の管径)を小さく設定する
必要がある。従って、ガス化炉51内でガス化しなかっ
たプラスチック廃棄物片やこの廃棄物に付着したアッシ
ュ、金属などの異物が炉底部51aに落下して残渣64
となり、場合によってはこの残渣64が前記噴流口を閉
塞し、運転を阻害することがある。本発明は上記の技術
水準に鑑み、従来技術におけるような残渣による噴流口
の閉塞が防止できる有機物ガス化炉の炉底残渣排出装置
を提供しようとするものである。
In the above-mentioned conventional jet bed type gasification furnace 51, the jet gas 62 is supplied to the furnace bottom portion 51a.
It is necessary to set the gas velocity when the gas is blown up into the furnace from the jet speed in the furnace or higher. Further, since the inert gas at room temperature that does not participate in the reaction is used as the jet gas 62, if the flow rate increases, the temperature of the reaction field decreases and the gasification reaction cannot be maintained. On the other hand, since the jet velocity needs to be a certain value or more, in order not to reduce the jet flow velocity of the jet gas 62, the sectional area of the jet port of the furnace bottom part 51a (the diameter of the jet gas supply pipe 55) Needs to be set small. Therefore, foreign matter such as plastic waste pieces that have not been gasified in the gasification furnace 51, ash attached to the waste, and metals drop to the furnace bottom 51a and the residue 64
Therefore, in some cases, the residue 64 may block the jet port and hinder the operation. In view of the above-mentioned state of the art, the present invention aims to provide a bottom residue discharge device for an organic matter gasification furnace capable of preventing clogging of a jet port due to a residue as in the prior art.

【0004】[0004]

【課題を解決するための手段】前記課題を解決するため
の、本発明による有機物ガス化炉の炉底残渣排出装置の
構成は次のとおりである。
[Means for Solving the Problems] The structure of the apparatus for discharging the bottom residue of an organic matter gasification furnace according to the present invention for solving the above problems is as follows.

【0005】(1)水蒸気、支燃ガス及び有機物原料を
高温の炉内に供給し、炉内の噴流によって部分ガス化反
応させてメタノール合成用原料ガスを生成する有機物の
ガス化炉において、炉底残渣を落下させるに充分な水平
方向断面積を形成した炉底開口部を前記ガス化炉の炉底
最下部に設け、前記炉底残渣を落下させるに充分な水平
方向断面積を形成して下端部が水封タンクに浸漬する水
封式の噴流用ガス供給管を前記炉底開口部の下方に設
け,前記炉底開口部と前記噴流用ガス供給管との間に炉
底室を介装し、前記炉底開口部よりも小断面積で噴流用
ガスに所定の噴出速度を付与する噴出口を有する炉底仕
切板を前記炉底室内で開閉するように設けてなることを
特徴とする有機物ガス化炉の炉底残渣排出装置。
(1) In a gasification furnace for organic matter, in which steam, combustion-supporting gas and organic material raw material are supplied into a high temperature furnace and a partial gasification reaction is caused by a jet flow in the furnace to produce a raw material gas for methanol synthesis A bottom opening is provided at the bottom of the bottom of the gasification furnace, the bottom opening having a horizontal cross-sectional area sufficient to drop the bottom residue, and a horizontal cross-sectional area sufficient to drop the bottom residue is formed. A water-sealed jet gas supply pipe whose lower end is immersed in a water-sealed tank is provided below the furnace bottom opening, and a furnace bottom chamber is interposed between the furnace bottom opening and the jet gas supply pipe. And a furnace bottom partition plate having a cross-sectional area smaller than that of the furnace bottom opening and having a jet port for imparting a predetermined jetting speed to the jet gas, is provided so as to open and close in the furnace bottom chamber. Residue bottom discharge device for organic gasifier.

【0006】(2)前記(1)項の装置において、前記
噴流用ガス供給管または炉底室に噴流用ガス圧力検出手
段を設け、この噴流用ガス圧力検出値によって前記仕切
板を自動的に開閉させる仕切板開閉手段を設けてなるこ
とを特徴とする有機物ガス化炉の炉底残渣排出装置。
(2) In the apparatus of the above item (1), a jet gas pressure detecting means is provided in the jet gas supply pipe or the furnace bottom chamber, and the partition plate is automatically operated by the jet gas pressure detection value. A furnace bottom residue discharging device for an organic matter gasification furnace, characterized in that a partition plate opening / closing means for opening / closing is provided.

【0007】(3)水蒸気、支燃ガス及び有機物原料を
高温の炉内に供給し、炉内の噴流によって部分ガス化反
応させてメタノール合成用原料ガスを生成する有機物の
ガス化炉において、炉底残渣を落下させるに充分な水平
方向断面積を形成した炉底開口部を前記ガス化炉の炉底
最下部に設け、前記炉底残渣を落下させるに充分な水平
方向断面積を形成して下端部が水封タンクに浸漬する水
封式の噴流用ガス供給管を前記炉底開口部の下方に設
け、前記炉底開口部よりも小断面積で噴流用ガスに所定
の噴出速度を付与する噴出口を有する炉底仕切板を前記
噴流用ガス供給管内で開閉するように設けてなることを
特徴とする有機物ガス化炉の炉底残渣排出装置。
(3) In a gasification furnace for organic matter, in which steam, combustion-supporting gas, and organic material raw material are supplied into a high-temperature furnace, and a partial gasification reaction is caused by a jet flow in the furnace to produce a raw material gas for methanol synthesis. A bottom opening is provided at the bottom of the bottom of the gasification furnace, the bottom opening having a horizontal cross-sectional area sufficient to drop the bottom residue, and a horizontal cross-sectional area sufficient to drop the bottom residue is formed. A water-sealed jet gas supply pipe whose lower end is immersed in a water-sealed tank is provided below the furnace bottom opening to give a predetermined jetting speed to the jet gas with a cross-sectional area smaller than that of the furnace bottom opening. A furnace bottom residue discharge device for an organic matter gasification furnace, characterized in that a furnace bottom partition plate having a jet outlet is provided so as to open and close in the jet gas supply pipe.

【0008】(4)前記(3)項の装置において、前記
噴流用ガス供給管に噴流用ガス圧力検出手段を設け,こ
の噴流ガス圧力検出値によって前記仕切板を自動的に開
閉させる仕切板開閉手段を設けてなる事を特徴とする有
機物ガス化炉の炉底残渣排出装置。
(4) In the apparatus of the above item (3), a jet plate gas pressure detecting means is provided in the jet gas supply pipe, and a partition plate opening / closing is provided for automatically opening / closing the partition plate according to the jet gas pressure detection value. An apparatus for discharging bottom residue of an organic matter gasification furnace, characterized in that it is provided with means.

【0009】[0009]

【作用】噴流用ガスを噴流用ガス供給管及び炉底仕切板
の噴出口からガス化炉の炉底最下部に所定の噴出速度で
噴出させて炉内に噴流を発生させるとともにに、水蒸
気、支燃ガス(酸素又は空気などの酸素含有ガス)及び
有機物原料を高温の炉内に供給し、有機物原料と水蒸気
とを支燃ガスによって反応させてガス化し、例えばメタ
ノール合成の原料用ガスを生成する。ガス化炉内は、こ
の反応熱によって反応に必要な温度が維持される。炉底
最下部すなわち炉底仕切板の上面には、炉内でガス化し
なかった有機物片やこの有機物に付着したアッシュ、金
属等の異物が落下して炉底残渣となって堆積し、炉底開
口部を閉塞しようとする。この炉底開口部の開口面積が
炉底仕切板の噴出口よりも小さくなると、炉底室内又は
噴流用ガス供給管内で炉底仕切板を開いて炉底残渣を炉
底室を経て噴流用ガス供給管から、又は直接噴流用ガス
供給管から水封タンクに落下させ、噴流用ガスの噴出速
度低下すなわち炉内噴流速度の低下を防止する。炉底残
渣が落下して除去されると炉底仕切板を炉底開口部の下
方に戻し、ガス化炉を正常運転に戻す。
The jet gas is spouted from the jet gas supply pipe and the jet port of the furnace bottom partition plate to the lowermost portion of the bottom of the gasification furnace at a predetermined jet speed to generate a jet flow in the furnace, and at the same time, steam, A combustion-supporting gas (oxygen-containing gas such as oxygen or air) and an organic material are supplied into a high-temperature furnace, and the organic-material raw material and steam are reacted by the combustion-supporting gas to be gasified, for example, a raw material gas for methanol synthesis is generated. To do. The temperature required for the reaction is maintained in the gasification furnace by this reaction heat. At the bottom of the bottom of the furnace, that is, on the top of the bottom partition plate, organic pieces that have not been gasified in the furnace, ash adhering to this organic matter, and foreign substances such as metals fall and accumulate as the bottom residue of the furnace. Trying to close the opening. When the opening area of this furnace bottom opening becomes smaller than the jet port of the furnace bottom partition plate, the furnace bottom partition plate is opened in the furnace bottom chamber or in the jet gas supply pipe, and the furnace bottom residue is passed through the furnace bottom chamber to the jet gas. The gas is dropped from the supply pipe or directly from the jet gas supply pipe to the water seal tank to prevent the jet gas from being jetted at a low velocity, that is, the in-furnace jet velocity to be reduced. When the bottom residue is removed by dropping, the bottom partition plate is returned below the bottom opening, and the gasification furnace is returned to normal operation.

【0010】前記の作用に加え、噴流用ガス供給管内ま
たは炉底室内の圧力を噴流用ガス圧力検出手段によって
連続して検出する。この検出値が予め設定した圧力上限
値を超えると、炉底仕切板の上面に炉底残渣が堆積し、
炉底開口部の開口面積が炉底仕切板の噴出口よりも小さ
くなっているので、仕切板開閉手段によって炉底仕切板
を自動的に開放し、炉底残渣を噴流用ガス供給管から水
封タンクに落下させ、噴流用ガスの噴出速度低下すなわ
ち炉内噴流速度の低下を防止する。
In addition to the above operation, the pressure in the jet gas supply pipe or in the furnace bottom chamber is continuously detected by the jet gas pressure detection means. When this detected value exceeds the preset upper pressure limit, the bottom residue accumulates on the upper surface of the bottom partition plate,
Since the opening area of the furnace bottom opening is smaller than the jet outlet of the furnace bottom partition plate, the partition plate opening / closing means automatically opens the furnace bottom partition plate to remove the bottom residue from the jet gas supply pipe. It is dropped in a sealed tank to prevent the jetting speed of the jetting gas, that is, the jetting speed in the furnace from dropping.

【0011】[0011]

【実施例】図1は本発明の第1実施例である炉底残渣排
出装置を備えた噴流床型有機物部分ガス化炉の概念を示
す側面図、図2は図1の炉底残渣排出時の状態を示す側
面図、図3はその制御器の構成を示すブロック図、図4
はその手順を要約したフロー図である。なお、従来の装
置と同一の部材及び部位には同一の符号を付し、重複す
る説明を省略する。
FIG. 1 is a side view showing the concept of a spouted bed type organic matter partial gasification furnace equipped with a furnace bottom residue discharging apparatus according to the first embodiment of the present invention, and FIG. 4 is a side view showing the state of FIG. 3, FIG. 3 is a block diagram showing the configuration of the controller, FIG.
Is a flow chart summarizing the procedure. The same members and parts as those of the conventional device are denoted by the same reference numerals, and redundant description will be omitted.

【0012】図1及び図2において、ガス化炉51の炉
底部51a最下部には、残渣64を落下させるに充分な
断面積の炉底開口部51bが設けられ、さらにその下方
には炉底室1が配設されている。この炉底室1には予熱
装置58及び圧力検出器7が装着され、この圧力検出器
7は制御器10を介して油圧シリンダ4の切換弁6に検
出信号を送信するようになっている。2は炉底仕切板で
あり、噴流用ガス62に所定の噴出速度を付与すること
のできる開口面積を有する噴出口2aが穿設され、回転
軸3、アーム5及び油圧シリンダ4によって下方に開く
ように炉底室1に収納されている。炉底室1の下方には
下端部が水封タンク57に浸漬する噴流用ガス供給管8
が配設され、この噴流用ガス供給管8には噴流用ガス供
給ライン56が装着されている。
1 and 2, a furnace bottom 51a of the gasification furnace 51 is provided with a furnace bottom opening 51b having a cross-sectional area sufficient for dropping the residue 64 at the bottom, and further below the furnace bottom 51a. A chamber 1 is arranged. A preheating device 58 and a pressure detector 7 are attached to the furnace bottom chamber 1, and the pressure detector 7 transmits a detection signal to the switching valve 6 of the hydraulic cylinder 4 via the controller 10. Reference numeral 2 denotes a furnace bottom partition plate, which is provided with a jet port 2a having an opening area capable of imparting a predetermined jet velocity to the jet gas 62, and is opened downward by a rotary shaft 3, an arm 5 and a hydraulic cylinder 4. Is housed in the hearth chamber 1. Below the furnace bottom chamber 1, a jet gas supply pipe 8 whose lower end is immersed in a water seal tank 57
A jet gas supply line 56 is attached to the jet gas supply pipe 8.

【0013】制御器10は図3に示すように、圧力検出
器7から検出信号を受信して圧力上限値と比較演算する
検出値比較部11と、圧力上限値を記憶する圧力上限記
憶部12と、切換弁6を作動させる切換弁作動指示部1
3とによって構成されている。
As shown in FIG. 3, the controller 10 receives a detection signal from the pressure detector 7 and compares it with a pressure upper limit value to perform a calculation operation, and a pressure upper limit storage unit 12 that stores the pressure upper limit value. And a switching valve operation instructing section 1 for operating the switching valve 6.
3.

【0014】装置の始動時には、予熱装置58から熱風
を炉底室1及び噴出口2aを介してガス化炉51内に供
給し、ガス化炉51を約700℃に予熱する。次に、噴
流用ガス供給ライン56から例えば窒素ガス、炭酸ガス
などのイナートガスである噴流用ガス62を噴流用ガス
供給管8及び炉底室1を介して噴出口2aからガス化炉
51内に噴出させ、炉51内に噴流を発生させると共
に、水蒸気酸素供給ライン52及び原料供給装置54か
ら水蒸気・酸素混合ガス61及び例えばプラスチック廃
棄物を粉砕した有機物原料60を供給し、炉内の熱及び
酸素によって有機物原料60と水蒸気とを反応させてガ
ス化し、メタノール合成の原料用ガス63を生成する。
定常運転中のガス化炉51内は、この反応熱によって7
00℃前後の温度に維持される。
At the time of starting the apparatus, hot air is supplied from the preheating device 58 into the gasification furnace 51 through the furnace bottom chamber 1 and the jet port 2a to preheat the gasification furnace 51 to about 700.degree. Next, a jet gas 62, which is an inert gas such as nitrogen gas or carbon dioxide gas, is introduced from the jet gas supply line 56 into the gasification furnace 51 through the jet gas supply pipe 8 and the furnace bottom chamber 1 from the jet outlet 2a. A jet flow is generated in the furnace 51, and a steam / oxygen mixed gas 61 and an organic material raw material 60 obtained by crushing, for example, plastic waste are supplied from the steam oxygen supply line 52 and the raw material supply device 54 to heat and heat the furnace. Oxygen reacts the organic material raw material 60 with water vapor to gasify it and generate a raw material gas 63 for methanol synthesis.
The inside of the gasification furnace 51 during steady operation is heated by this reaction heat to 7
The temperature is maintained around 00 ° C.

【0015】炉底部51aの炉底仕切板2の上面には、
ガス化炉51内でガス化しなかったプラスチック廃棄物
片やこの廃棄物に付着したアッシュ、金属などの異物が
落下して残渣64となって図1に示すように堆積し、炉
底開口部51bを閉塞しようとする。この炉底開口部5
1bの開口面積が炉底仕切板2の噴出口2aよりも小さ
くなると炉底室1内の圧力が上昇する。
On the upper surface of the furnace bottom partition plate 2 of the furnace bottom 51a,
Plastic waste pieces that have not been gasified in the gasification furnace 51 and foreign substances such as ash and metals attached to this waste fall to form a residue 64 and deposit as shown in FIG. Try to block. This furnace bottom opening 5
When the opening area of 1b becomes smaller than the ejection port 2a of the furnace bottom partition plate 2, the pressure in the furnace bottom chamber 1 rises.

【0016】圧力検出器7はこの圧力を連続して検出
し、制御器10に送信する。検出値比較部11はこの検
出値を受信して圧力上限値記憶部12に予め入力されて
いる圧力上限値と比較演算し、検出値がこの圧力上限値
を超えると、切換弁作動指示部13によって図2に示す
ように切換弁6が作動し、炉底仕切板2を下方に開いて
残渣64を噴流用ガス供給管8から水封タンク57に落
下させる。所定の時間が経過して残渣64が落下する
と、切換弁作動指示部13は図1に示すように切換弁6
を作動させ炉底仕切板2を元に戻す。この有機物部分ガ
ス化及び炉底残渣搬出の手順を要約すると図4のように
なる。
The pressure detector 7 continuously detects this pressure and sends it to the controller 10. The detection value comparison unit 11 receives the detection value and performs a comparison calculation with the pressure upper limit value that is input in advance in the pressure upper limit storage unit 12. When the detection value exceeds the pressure upper limit value, the switching valve operation instructing unit 13 As shown in FIG. 2, the switching valve 6 is actuated, the furnace bottom partition plate 2 is opened downward, and the residue 64 is dropped from the jet gas supply pipe 8 to the water sealing tank 57. When the residue 64 drops after a lapse of a predetermined time, the switching valve operation instructing section 13 causes the switching valve 6 to move as shown in FIG.
Is operated to return the bottom plate 2 to the original state. The procedure for partial gasification of organic substances and removal of residue from the bottom of the furnace is summarized in FIG.

【0017】図5は本発明の第2実施例である炉底残渣
排出装置を備えた噴流床型有機物部分ガス化炉の概略を
示す側面図である。このガス化炉は第1実施例の炉底室
1を省略し、圧力検出器7を噴流用ガス供給管28に装
設してその圧力を検出し、炉底仕切板22を噴流用ガス
供給管28の上部で水平方向にスライドして開き、残渣
64を落下させるものである。なお、図5中図1と同一
部位には同一符号を付してあるので、説明は省略する。
FIG. 5 is a side view showing the outline of a spouted bed type organic matter partial gasification furnace equipped with a furnace bottom residue discharging apparatus according to a second embodiment of the present invention. In this gasification furnace, the furnace bottom chamber 1 of the first embodiment is omitted, the pressure detector 7 is attached to the jet gas supply pipe 28 to detect the pressure, and the furnace bottom partition plate 22 is supplied to the jet gas. The residue 64 is dropped by sliding horizontally on the upper portion of the pipe 28 to open it. Note that, in FIG. 5, the same parts as those in FIG.

【0018】[0018]

【発明の効果】本発明では次に示す効果がある。 (1)炉底残渣を落下させるに充分な断面積の炉底開口
部を前記ガス化炉の炉底最下部に設け、炉底残渣を落下
させるに充分な断面積で下端部が水封タンクに浸漬する
噴流用ガス供給管を炉底開口部の下方に設け、必要によ
り炉底開口部と噴流用ガス供給管との間に炉底室を介装
し、炉底開口部よりも小断面積で噴流用ガスに所定の噴
出速度を付与する噴出口を有する炉底仕切板を炉底室内
又は噴流用ガス供給管内で開閉するように設けたことに
より、炉底仕切板の上面に炉底残渣が堆積すると、炉底
仕切板を開いて炉底残渣を炉底室、噴流用ガス供給管か
ら水封タンクに落下させることが可能になり、炉底開口
部の開口面積の減少による噴流用ガスの噴出量減少を防
止し、ガス化炉を正常に運転することができる。
The present invention has the following effects. (1) A furnace bottom opening having a cross-sectional area sufficient to drop the bottom residue is provided at the bottom of the bottom of the gasification furnace, and the bottom end is a water sealing tank with a cross-sectional area sufficient to drop the bottom residue. A jet gas supply pipe to be immersed in the furnace is installed below the furnace bottom opening, and if necessary, a furnace bottom chamber is interposed between the furnace bottom opening and the jet gas supply pipe. The bottom of the furnace bottom partition plate is provided so as to open and close within the furnace bottom chamber or the gas supply pipe for the jet flow, and the bottom of the furnace bottom is provided on the upper surface of the furnace bottom partition plate. When residue accumulates, it is possible to open the furnace bottom partition plate and drop the furnace bottom residue from the furnace bottom chamber and jet gas supply pipe into the water seal tank. The gasification amount can be prevented from decreasing and the gasifier can be operated normally.

【0019】(2)前記(1)項の効果に加え、噴流用
ガス供給管または炉底室に噴流用ガス圧力検出手段を設
け、この噴流用ガス圧力検出値によって前記仕切板を自
動的に開閉させる仕切板開閉手段を設けたことにより、
噴流用ガス圧力検出手段によって連続して検出した噴流
用ガス供給管内、または炉底室内の圧力検出値が予め設
定した圧力上限値を超えると、仕切板開閉手段によって
炉底仕切板を自動的に開いて炉底残渣を噴流用ガス供給
管から水封タンクに落下させることが可能になり、炉底
開口部の開口面積の減少による噴流用ガスの噴出量減少
を防止し、ガス化炉運転の自動化に貢献することができ
る。
(2) In addition to the effect of item (1), a jet gas pressure detecting means is provided in the jet gas supply pipe or the furnace bottom chamber, and the partition plate is automatically operated by the jet gas pressure detection value. By providing the partition plate opening and closing means to open and close,
When the pressure detection value in the jet gas supply pipe continuously detected by the jet gas pressure detection means or the pressure detection value in the furnace bottom chamber exceeds a preset upper limit pressure, the furnace bottom partition plate is automatically opened by the partition plate opening / closing means. It becomes possible to open and drop the bottom residue from the jet gas supply pipe into the water seal tank, prevent the jet gas ejection amount from decreasing due to the reduction of the opening area of the furnace bottom opening, and prevent gasification furnace operation. Can contribute to automation.

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

【図1】本発明の第1実施例である炉底残渣排出装置を
備えた噴流床型有機物ガス化炉の概念を示す側面図。
FIG. 1 is a side view showing the concept of a spouted bed type organic matter gasification furnace equipped with a furnace bottom residue discharging apparatus according to a first embodiment of the present invention.

【図2】図1の装置の炉底残渣排出時の状態を示す側面
図。
FIG. 2 is a side view showing the state of the apparatus of FIG. 1 when discharging the bottom residue.

【図3】図1及び図2の制御器の構成を示すブロック
図。
FIG. 3 is a block diagram showing a configuration of a controller of FIGS. 1 and 2.

【図4】有機物部分ガス化及び炉底残渣排出の手順を要
約したフロー図。
FIG. 4 is a flow chart summarizing the procedure of partial gasification of organic matter and discharge of bottom residue.

【図5】本発明の第2実施例である炉底残渣排出装置を
備えた噴流床型有機物ガス化炉の概念を示す側面図。
FIG. 5 is a side view showing the concept of a spouted bed type organic matter gasification furnace equipped with a furnace bottom residue discharging apparatus according to a second embodiment of the present invention.

【図6】従来の噴流床型有機物ガス化炉の一例の概念を
示す側面図。
FIG. 6 is a side view showing the concept of an example of a conventional spouted bed type organic matter gasification furnace.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 平野 正樹 大阪府大阪市北区中之島3丁目3番22号 関西電力株式会社内 (72)発明者 角野 匡 大阪府大阪市北区中之島3丁目3番22号 関西電力株式会社内 (72)発明者 米沢 鴻一 広島県広島市中区小町4番33号 中国電力 株式会社内 (72)発明者 大楽 正則 広島県広島市中区小町4番33号 中国電力 株式会社内 (72)発明者 徳政 賢治 広島県広島市中区小町4番33号 中国電力 株式会社内 (72)発明者 伊藤 義文 広島県広島市西区観音新町四丁目6番22号 三菱重工業株式会社広島製作所内 (72)発明者 新屋 謙治 広島県広島市西区観音新町四丁目6番22号 三菱重工業株式会社広島研究所内 (72)発明者 金子 雅人 広島県広島市西区観音新町四丁目6番22号 三菱重工業株式会社広島研究所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Masaki Hirano 3-3-22 Nakanoshima, Kita-ku, Osaka City, Osaka Prefecture Kansai Electric Power Co., Inc. (72) Tadashi Tsunono 3-chome Nakanoshima, Kita-ku, Osaka City, Osaka Prefecture No. 22 in Kansai Electric Power Co., Inc. (72) Koichi Yonezawa 4-3 33, Komachi, Naka-ku, Hiroshima City, Hiroshima Prefecture China Electric Power Co., Ltd. (72) Masanori Ogaku 4-33, Komachi, Naka-ku, Hiroshima City, Hiroshima Prefecture Chugoku Electric Power Co., Inc. (72) Inventor Kenji Tokumasa 4-33 Komachi, Naka-ku, Hiroshima City, Hiroshima Prefecture Chugoku Electric Power Co., Inc. (72) Yoshifumi Ito 4-4-2, Kannon Shinmachi, Nishi-ku, Hiroshima City, Hiroshima Prefecture Mitsubishi Heavy Industries Inside the Hiroshima Works (72) Kenji Ariya, Kenji Shinya 4-6-22 Kannon Shinmachi, Nishi-ku, Hiroshima City, Hiroshima Prefecture Mitsubishi Heavy Industries Ltd. Hiroshima Research Institute (72) Inventor Masato Kaneko Hiro Prefecture of Hiroshima Nishi-ku Kan'onshin-cho, chome No. 6 No. 22 Mitsubishi Heavy Industries, Ltd. Hiroshima within the Institute

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 水蒸気、支燃ガス及び有機物原料を高温
の炉内に供給し、炉内の噴流によって部分ガス化反応さ
せてメタノール合成用原料ガスを生成する有機物のガス
化炉において、炉底残渣を落下させるに充分な水平方向
断面積を形成した炉底開口部を前記ガス化炉の炉底最下
部に設け、前記炉底残渣を落下させるに充分な水平方向
断面積を形成して下端部が水封タンクに浸漬する水封式
の噴流用ガス供給管を前記炉底開口部の下方に設け、前
記炉底開口部と前記噴流用ガス供給管との間に炉底室を
介装し、前記炉底開口部よりも小断面積で噴流用ガスに
所定の噴出速度を付与する噴出口を有する炉底仕切板を
前記炉底室内で開閉するように設けてなることを特徴と
する有機物ガス化炉の炉底残渣排出装置。
1. A gasification furnace for an organic substance, in which steam, combustion-supporting gas, and an organic material raw material are supplied into a high-temperature furnace, and a partial gasification reaction is caused by a jet flow in the furnace to produce a raw material gas for methanol synthesis. A bottom bottom opening having a horizontal cross-sectional area sufficient to drop the residue is provided at the bottom of the bottom of the gasification furnace, and a horizontal cross-sectional area sufficient to drop the bottom residue is formed to form a lower end. A water-sealed jet gas supply pipe whose part is immersed in a water-sealed tank is provided below the furnace bottom opening, and a furnace bottom chamber is interposed between the furnace bottom opening and the jet gas supply pipe. A furnace bottom partition plate having a cross-sectional area smaller than that of the furnace bottom opening and having a jet port for imparting a predetermined jetting speed to the jet gas is provided so as to open and close in the furnace bottom chamber. Residue bottom discharge device for organic gasifier.
【請求項2】 請求項1の装置において、前記噴流用ガ
ス供給管または炉底室に噴流用ガス圧力検出手段を設
け、この噴流用ガス圧力検出値によって前記仕切板を自
動的に開閉させる仕切板開閉手段を設けてなることを特
徴とする有機物ガス化炉の炉底残渣排出装置。
2. The partition according to claim 1, wherein the jet gas supply pipe or the furnace bottom chamber is provided with jet gas pressure detection means, and the partition plate is automatically opened and closed according to the jet gas pressure detection value. A bottom discharge device for an organic matter gasification furnace, characterized in that it is provided with a plate opening / closing means.
【請求項3】 水蒸気、支燃ガス及び有機物原料を高温
の炉内に供給し、炉内の噴流によって部分ガス化反応さ
せてメタノール合成用原料ガスを生成する有機物のガス
化炉において、炉底残渣を落下させるに充分な水平方向
断面積を形成した炉底開口部を前記ガス化炉の炉底最下
部に設け、前記炉底残渣を落下させるに充分な水平方向
断面積を形成して下端部が水封タンクに浸漬する水封式
の噴流用ガス供給管を前記炉底開口部の下方に設け、前
記炉底開口部よりも小断面積で噴流用ガスに所定の噴出
速度を付与する噴出口を有する炉底仕切板を前記噴流用
ガス供給管内で開閉するように設けてなることを特徴と
する有機物ガス化炉の炉底残渣排出装置。
3. A gasification furnace for an organic substance, in which steam, combustion-supporting gas, and organic material raw material are supplied into a high-temperature furnace, and a partial gasification reaction is caused by a jet flow in the furnace to produce a raw material gas for methanol synthesis. A bottom bottom opening having a horizontal cross-sectional area sufficient to drop the residue is provided at the bottom of the bottom of the gasification furnace, and a horizontal cross-sectional area sufficient to drop the bottom residue is formed to form a lower end. A water-sealed jet gas supply pipe whose portion is immersed in a water-sealed tank is provided below the furnace bottom opening, and a predetermined jetting speed is given to the jet gas with a cross-sectional area smaller than that of the furnace bottom opening. A furnace bottom residue discharging device for an organic matter gasification furnace, characterized in that a furnace bottom partition plate having a jet port is provided so as to be opened and closed in the jet gas supply pipe.
【請求項4】 請求項3の装置において、前記噴流用ガ
ス供給管に噴流用ガス圧力検出手段を設け,この噴流ガ
ス圧力検出値によって前記仕切板を自動的に開閉させる
仕切板開閉手段を設けてなる事を特徴とする有機物ガス
化炉の炉底残渣排出装置。
4. The apparatus according to claim 3, wherein the jet gas supply pipe is provided with jet gas pressure detection means, and partition plate opening / closing means is provided for automatically opening / closing the partition plate according to the jet gas pressure detection value. A bottom discharge device for organic gasification furnaces.
JP10517995A 1995-04-28 1995-04-28 Waste bottom discharge device for organic gasification furnace Expired - Fee Related JP3746536B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10517995A JP3746536B2 (en) 1995-04-28 1995-04-28 Waste bottom discharge device for organic gasification furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10517995A JP3746536B2 (en) 1995-04-28 1995-04-28 Waste bottom discharge device for organic gasification furnace

Publications (2)

Publication Number Publication Date
JPH08296973A true JPH08296973A (en) 1996-11-12
JP3746536B2 JP3746536B2 (en) 2006-02-15

Family

ID=14400460

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10517995A Expired - Fee Related JP3746536B2 (en) 1995-04-28 1995-04-28 Waste bottom discharge device for organic gasification furnace

Country Status (1)

Country Link
JP (1) JP3746536B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101417950B1 (en) * 2012-05-23 2014-07-10 한국생산기술연구원 Impurities extractor for scrap refining system using a non - contact crucible
WO2014175208A1 (en) * 2013-04-24 2014-10-30 株式会社Ihi Fluidized bed system and method for operating fluidized bed furnace

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101417950B1 (en) * 2012-05-23 2014-07-10 한국생산기술연구원 Impurities extractor for scrap refining system using a non - contact crucible
WO2014175208A1 (en) * 2013-04-24 2014-10-30 株式会社Ihi Fluidized bed system and method for operating fluidized bed furnace
JP5880783B2 (en) * 2013-04-24 2016-03-09 株式会社Ihi Fluidized bed system and fluidized bed furnace operating method
AU2014258500B2 (en) * 2013-04-24 2016-07-21 Ihi Corporation Fluidized bed system and method for operating fluidized bed furnace
US10011794B2 (en) 2013-04-24 2018-07-03 Ihi Corporation Fluidized bed system and method for operating fluidized bed furnace

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