JP2002303410A - Waste gasifying melting device - Google Patents

Waste gasifying melting device

Info

Publication number
JP2002303410A
JP2002303410A JP2001105105A JP2001105105A JP2002303410A JP 2002303410 A JP2002303410 A JP 2002303410A JP 2001105105 A JP2001105105 A JP 2001105105A JP 2001105105 A JP2001105105 A JP 2001105105A JP 2002303410 A JP2002303410 A JP 2002303410A
Authority
JP
Japan
Prior art keywords
gas
furnace
pressure
melting
gasification
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.)
Withdrawn
Application number
JP2001105105A
Other languages
Japanese (ja)
Inventor
Takahiro Marumoto
隆弘 丸本
Noriyuki Oyatsu
紀之 大谷津
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.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP2001105105A priority Critical patent/JP2002303410A/en
Publication of JP2002303410A publication Critical patent/JP2002303410A/en
Withdrawn legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a waste gasifying melting device capable of keeping a pressure in a gasifying furnace at a negative pressure regardless of an amount of gas generated in a gasifying furnace. SOLUTION: By providing a bypass line 35 through which gas 22 generated in the gasifying furnace 3 flows in a melting furnace outlet line 25 by causing the gas to bypass a melting furnace 5, a part of gas in the gasifying furnace is hardly reduced in a pressure and can flow in a melt furnace outlet line 25, where a pressure is comparatively low, not through the melting furnace 5, where a pressure is comparatively high. This constitution can reduce a pressure in the gasifying furnace 3 compared with conventional constitution wherein after the melting furnace 5 is decreased in a pressure, the gasifying furnace 3 is decreased in a pressure, and can keep the interior of the gasifying furnace 3 at a negative pressure regardless of an amount of the gas 22 generated in the gasifying furnace 3.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、廃棄物を熱分解し
て灰分を溶融する廃棄物ガス化溶融装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a waste gasification and melting apparatus for pyrolyzing waste and melting ash.

【0002】[0002]

【従来の技術】一般ごみ、産業廃棄物などをガス化炉内
でガス化、つまり熱分解すると有毒なガスが発生する場
合がある。このため、ガス化炉へ廃棄物を搬送する搬送
路には、ガス化炉内で発生したガスが、搬送路を通って
ガス化炉の外部へ放出されることをできるだけ防止する
ため、例えば、廃棄物が投入されると開き、それ以外の
ときは閉じている蓋やダンパーなどのシール装置が設け
られている。しかし、このシール装置には、廃棄物に含
まれた金属などの異物によるシール装置の故障、例え
ば、ダンパーと流路の壁面との間に異物が挟まることで
ダンパーが動かなくなるなどの故障の発生を防止するた
めに隙間が設けられている。したがって、シール装置に
よってガス化炉内のガスが外部に漏れないように完全な
気密状態を確保することは難しい。
2. Description of the Related Art When general refuse, industrial waste, and the like are gasified, that is, thermally decomposed in a gasification furnace, a toxic gas may be generated. For this reason, in the transport path for transporting waste to the gasifier, the gas generated in the gasifier, in order to prevent as much as possible to be released outside the gasifier through the transport path, for example, A sealing device such as a lid or a damper that is opened when waste is put in and is closed at other times is provided. However, in this sealing device, the failure of the sealing device due to foreign matter such as metal contained in waste, for example, the failure of the damper to be stuck due to the foreign material being caught between the damper and the wall surface of the flow path occurs. A gap is provided in order to prevent this. Therefore, it is difficult to secure a completely airtight state by the sealing device so that the gas inside the gasification furnace does not leak outside.

【0003】このため、従来の廃棄物ガス化溶融装置で
は、ガス化炉で発生したガスが通流するガス流路に、溶
融炉と誘引通風機とをガスの流れに対して上流側から順
次設け、誘引通風機がガス流路内のガスを吸引して下流
側に導く構成とすることで、ガス化炉内の圧力をガス化
炉の外部より低い圧力、つまり負圧に保ち、ガス化炉内
のガスがシール装置の隙間からガス化炉の外部へ放出さ
れることを防止している。
For this reason, in a conventional waste gasification and melting apparatus, a melting furnace and an induction ventilator are sequentially placed in a gas flow path through which gas generated in the gasification furnace flows from the upstream side with respect to the gas flow. By providing a structure in which the induction ventilator sucks the gas in the gas flow path and guides it to the downstream side, the pressure inside the gasification furnace is maintained at a lower pressure than the outside of the gasification furnace, that is, a negative pressure, and gasification is performed. Gas in the furnace is prevented from being released from the gap of the sealing device to the outside of the gasification furnace.

【0004】[0004]

【発明が解決しようとする課題】ところで、ガス化炉に
供給される廃棄物の種類や量は常に一定ではなく、ガス
化炉には、ガスを発生させやすい廃棄物が供給された
り、一時的に大量の廃棄物が供給されたりする場合があ
る。この場合、ガス化炉内で発生するガスの量は、通常
に比べて多くなり、ガス化炉からガス化炉の下流側に位
置する溶融炉へ供給されるガス及び未燃分の量も増加す
る。これに伴い溶融炉内での燃焼により生じる排ガスや
熱量がさらに増加するため、溶融炉の圧力が通常に比べ
て下がり難くなる。
By the way, the kind and amount of waste supplied to the gasifier are not always constant, and the gasifier is supplied with waste which is likely to generate gas or temporarily. A large amount of waste may be supplied. In this case, the amount of gas generated in the gasifier becomes larger than usual, and the amount of gas and unburned gas supplied from the gasifier to the melting furnace located downstream of the gasifier also increases. I do. Accordingly, the amount of exhaust gas and the amount of heat generated by combustion in the melting furnace further increase, so that the pressure of the melting furnace is less likely to decrease than usual.

【0005】したがって、誘引通風機によって溶融炉内
を減圧した上でガス化炉内を減圧する従来の構成では、
ガス化炉内の減圧が難しくなり、ガス化炉内の圧力が外
部と同じ、もしくは、外部より高い状態になり易いた
め、ガス化炉内が負圧に保てない場合がある。この場
合、従来の廃棄物ガス化溶融装置は、ガス化炉内のガス
が外部に放出されることを防ぐために、廃棄物の供給を
停止もしくは廃棄物ガス化溶融装置全体を停止させてい
る。このため、ガス化炉で発生するガスの量が比較的大
量であっても、発生したガス量に関係無くガス化炉内を
負圧に保つことができる廃棄物ガス化溶融装置が望まれ
ている。
Therefore, in a conventional configuration in which the inside of the gasification furnace is depressurized after depressurizing the inside of the melting furnace by the induction ventilator,
Since it is difficult to reduce the pressure inside the gasification furnace and the pressure inside the gasification furnace tends to be equal to or higher than the outside, the inside of the gasification furnace may not be maintained at a negative pressure. In this case, in the conventional waste gasification and melting apparatus, in order to prevent the gas in the gasification furnace from being released to the outside, the supply of the waste is stopped or the entire waste gasification and melting apparatus is stopped. Therefore, even if the amount of gas generated in the gasification furnace is relatively large, a waste gasification and melting apparatus capable of maintaining the inside of the gasification furnace at a negative pressure regardless of the amount of generated gas is desired. I have.

【0006】本発明の課題は、ガス化炉内で発生するガ
スの量に関係無く、ガス化炉内の圧力を負圧に保つこと
にある。
An object of the present invention is to keep the pressure in a gasification furnace negative regardless of the amount of gas generated in the gasification furnace.

【0007】[0007]

【課題を解決するための手段】本発明の廃棄物ガス化溶
融装置は、廃棄物を熱分解するガス化炉と、熱分解で生
じたガスが通流するガス流路と、このガス流路に設けら
れガス流路内にガスを誘引してを通流させる誘引通風機
と、ガス流路のガス化炉及び誘引通風機間の部分に設け
られガス及びガスに同伴されている未燃分を燃焼させる
と共に灰分を溶融する溶融炉とを備え、ガス化炉内で発
生したガスを、溶融炉をバイパスさせてガス流路の溶融
炉と誘引通風機との間の部分に流入させるバイパス流路
を設けたことにより上記課題を解決する。
SUMMARY OF THE INVENTION A waste gasification and melting apparatus according to the present invention comprises a gasification furnace for thermally decomposing waste, a gas flow path through which gas generated by the pyrolysis flows, and a gas flow path. An air ventilator that is provided in the gas flow path for inducing and flowing gas into the gas flow path, and a gas and an unburned component that is provided in a portion of the gas flow path between the gasification furnace and the induction ventilator. And a melting furnace for melting the ash, and a gas generated in the gasification furnace, bypassing the melting furnace and flowing into a portion of the gas flow path between the melting furnace and the induction ventilator. The above problem is solved by providing a road.

【0008】また、本発明の廃棄物ガス化溶融装置は、
廃棄物を熱分解するガス化炉と、このガス化炉に廃棄物
を搬送する搬送路と、熱分解で生じたガスが通流するガ
ス流路と、このガス流路に設けられガス流路内にガスを
誘引してを通流させる誘引通風機と、ガス流路のガス化
炉及び誘引通風機間の部分に設けられガス及びガスに同
伴されている未燃分を燃焼させると共に灰分を溶融する
溶融炉とを備え、ガス化炉から搬送路へ流入したガス
を、溶融炉をバイパスさせてガス流路の溶融炉と誘引通
風機との間の部分に流入させるバイパス流路を設けたこ
とにより上記課題を解決する。
[0008] The waste gasification and melting apparatus of the present invention comprises:
A gasification furnace for thermally decomposing waste, a conveyance path for conveying waste to the gasification furnace, a gas flow path through which gas generated by the pyrolysis flows, and a gas flow path provided in the gas flow path A draft fan that draws gas into the gas flower, and a gas flow furnace that is provided between the gasifier and the draft fan in the gas flow path, burns gas and unburned components entrained in the gas, and reduces ash content. A melting furnace was provided for melting, and a bypass flow path was provided in which the gas flowing from the gasification furnace to the transfer path was allowed to flow into the gas flow path between the melting furnace and the induction ventilator by bypassing the melting furnace. This solves the above problem.

【0009】このような構成により、ガス化炉内で発生
したガスの一部を、バイパス流路を介して溶融炉及び誘
引通風機間のガス流路へ流入させることができる。つま
り、ガス化炉内のガスの一部、または搬送路内のガスの
一部を、減圧し難く、かつ、比較的圧力が高い溶融炉内
を介さずに、比較的圧力の低い溶融炉及び誘引通風機間
のガス流路へ流入させることができる。これにより、溶
融炉が減圧されてからガス化炉が減圧される従来の構成
に比べて、ガス化炉内の減圧を行うことができる。した
がって、ガス化炉で発生するガスの量に関係無く、ガス
化炉内を負圧に保つことができる。
With such a configuration, a part of the gas generated in the gasification furnace can flow into the gas flow path between the melting furnace and the induction ventilator via the bypass flow path. That is, it is difficult to decompress a part of the gas in the gasification furnace or a part of the gas in the transfer path, and without passing through a relatively high-pressure melting furnace, a relatively low-pressure melting furnace and The gas can flow into the gas flow path between the induction ventilators. Thereby, the pressure in the gasification furnace can be reduced as compared with the conventional configuration in which the pressure in the melting furnace is reduced and then the pressure in the gasification furnace is reduced. Therefore, the inside of the gasification furnace can be maintained at a negative pressure regardless of the amount of gas generated in the gasification furnace.

【0010】さらに、ガス化炉内の圧力に応じて、バイ
パス流路の開閉を制御する開閉弁を備えた構成とするこ
とができる。このような構成とすることにより、バイパ
ス流路を介して溶融炉及び誘引通風機間のガス流路へ流
入させるガスの量をガス化炉内の圧力に応じて調整する
ことができる。これにより、ガス化炉内の圧力を所定の
範囲に保つことができるので好ましい。
[0010] Further, an on-off valve for controlling the opening and closing of the bypass flow passage according to the pressure in the gasification furnace can be provided. With such a configuration, the amount of gas flowing into the gas flow path between the melting furnace and the induction ventilator via the bypass flow path can be adjusted according to the pressure in the gasification furnace. This is preferable because the pressure in the gasification furnace can be kept in a predetermined range.

【0011】[0011]

【発明の実施の形態】(第1の実施形態)以下、本発明
を適用してなる廃棄物ガス化溶融装置の第1の実施形態
について図1を参照して説明する。図1は、本発明を適
用してなる廃棄物ガス化溶融装置の第1の実施形態の概
略構成と動さとを示した概略断面図である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS (First Embodiment) A first embodiment of a waste gasification and melting apparatus to which the present invention is applied will be described below with reference to FIG. FIG. 1 is a schematic sectional view showing a schematic configuration and operation of a first embodiment of a waste gasification and melting apparatus to which the present invention is applied.

【0012】本実施形態の廃棄物ガス化溶融装置1の構
成は、図1に示すように、ガス化炉3、溶融炉5、排ガ
ス7を完全に燃焼させる燃焼室9、排ガス7の熱を回収
する熱回収ボイラ11、排ガス7に含まれる煤塵13を
捕集する集塵装置15及び排ガス7を下流へ誘引する誘
引通風機17などで構成されている。
As shown in FIG. 1, the configuration of the waste gasification / melting apparatus 1 of the present embodiment includes a gasification furnace 3, a melting furnace 5, a combustion chamber 9 for completely burning the exhaust gas 7, and a heat of the exhaust gas 7. It comprises a heat recovery boiler 11 to be recovered, a dust collecting device 15 for collecting dust 13 contained in the exhaust gas 7, an induction ventilator 17 for inducing the exhaust gas 7 downstream, and the like.

【0013】ガス化炉3には、ガス化炉3内へ廃棄物2
0を導く搬送路19の一端が連結され、搬送路19の他
端は、例えば、廃棄物20の供給する量を調整するコン
ベアやスクリューフィーダなどの供給装置21に連結さ
れている。さらに、ガス化炉3には、ガス化炉3内で発
生したガス22及び未燃分であるチャー23などを下流
側へ導くガス化炉出口管路24の一端が連結され、ガス
化炉出口管路24の他端は、溶融炉5に連結されてい
る。溶融炉5には、溶融炉5内で発生した排ガス7を下
流側へ導く溶融炉出口管路25の一端が連結され、溶融
炉出口管路25の他端は、燃焼室9に連結されている。
また、ガス化炉3には、バイパス流路であるバイパス管
路35の一端が連結され、バイパス管路35の他端は、
溶融炉出口管路25に連結されている。さらに、ガス化
炉3には、ガス化炉3内の圧力を検出する圧力計37が
設けられている。
In the gasifier 3, waste 2 is introduced into the gasifier 3.
One end of the transport path 19 for guiding the waste 20 is connected, and the other end of the transport path 19 is connected to a supply device 21 such as a conveyor or a screw feeder for adjusting the amount of the waste 20 to be supplied. Further, the gasification furnace 3 is connected to one end of a gasification furnace outlet pipe 24 that guides the gas 22 generated in the gasification furnace 3 and the unburned char 23 to the downstream side. The other end of the pipe 24 is connected to the melting furnace 5. To the melting furnace 5, one end of a melting furnace outlet pipe 25 for guiding the exhaust gas 7 generated in the melting furnace 5 to the downstream side is connected, and the other end of the melting furnace outlet pipe 25 is connected to the combustion chamber 9. I have.
Further, one end of a bypass pipe 35 serving as a bypass flow path is connected to the gasification furnace 3, and the other end of the bypass pipe 35 is
It is connected to the melting furnace outlet line 25. Further, the gasification furnace 3 is provided with a pressure gauge 37 for detecting the pressure in the gasification furnace 3.

【0014】燃焼室9は、燃焼室出口管路26介して熱
回収ボイラ11に連結され、熱回収ボイラ11は、熱回
収ボイラ出口管路28を介して集塵装置15に連結され
ている。集塵装置15は誘引通風機入口管路30を介し
て誘引通風機17に連結され、誘引通風機17は、煙突
管路32を介して煙突27と連結されている。ガス化炉
3、ガス化炉出口管路24、溶融炉5、溶融炉出口管路
25、燃焼室9、燃焼室出口管路26、熱回収ボイラ1
1、熱回収ボイラ出口管路28、集塵装置15、誘引通
風機入口管路30、誘引通風機17、煙突管路32、煙
突27により、ガス化炉3内で発生したガス22を導く
ガス流路が形成されている。
The combustion chamber 9 is connected to the heat recovery boiler 11 via a combustion chamber outlet pipe 26, and the heat recovery boiler 11 is connected to the dust collector 15 via a heat recovery boiler outlet pipe 28. The dust collecting device 15 is connected to the induction ventilator 17 via an induction ventilator inlet conduit 30, and the induction ventilator 17 is connected to the chimney 27 via a chimney conduit 32. Gasification furnace 3, gasification furnace outlet line 24, melting furnace 5, melting furnace outlet line 25, combustion chamber 9, combustion chamber outlet line 26, heat recovery boiler 1
1. Gas that guides the gas 22 generated in the gasification furnace 3 by the heat recovery boiler outlet line 28, the dust collector 15, the induction ventilator inlet line 30, the induction ventilator 17, the chimney line 32, and the chimney 27. A channel is formed.

【0015】供給装置21には、廃棄物20を貯留する
供給ホッパ31が設けられ、供給装置21は、供給ホッ
パ31に貯留された廃棄物20の量を調整して搬送路1
9へ排出するように、搬送路19に連結されている。ま
た、廃棄物20を搬送路19へ排出する供給装置21の
排出部分には、例えば、廃棄物20が搬送路19へ投入
されるときに開き、それ以外のときは閉じている蓋やダ
ンパーなどのシール装置33が設けられている。シール
装置33は、ガス化炉3内で発生したガス22が、搬送
路19を通り供給装置21からガス化炉3の外部へ放出
されることをできるだけ抑制するために設けられている
が、廃棄物20に含まれた金属などの異物が蓋に挟まる
ことによる故障や停止などを防止するため、隙間や遊び
などが設けられている。
The supply device 21 is provided with a supply hopper 31 for storing the waste 20. The supply device 21 adjusts the amount of the waste 20 stored in the supply hopper 31 to
9 is connected to the transport path 19 so as to be discharged. In addition, for example, a lid or a damper that is opened when the waste 20 is put into the transport path 19 and is closed when the waste 20 is put into the transport path 19 may be provided at a discharge portion of the supply device 21 that discharges the waste 20 to the transport path 19. Is provided. The sealing device 33 is provided in order to suppress the gas 22 generated in the gasification furnace 3 from being released from the supply device 21 to the outside of the gasification furnace 3 through the transport path 19 as much as possible. Gaps, play, and the like are provided in order to prevent a failure or a stop caused by a foreign substance such as metal contained in the object 20 being caught in the lid.

【0016】誘引通風機入口管路30には、配線45を
通じて圧力計37に電気的に接続されたダンパー34が
設けられている。ダンパー34は、圧力計37からの信
号に応じて、ガス化炉3内の圧力が所定の負圧になるよ
うに、誘引通風機入口管路30内を流れる排ガス7の流
量を調整する。一方、バイパス管路35には、開閉弁で
あるダンパー39が設けられており、ダンパー39は、
配線41を通じて圧力計37に電気的に接続されてい
る。ダンパー39は、ダンパー34が全開になった場合
に作動し、圧力計37からの信号に応じて、ガス化炉3
内の圧力が所定の負圧になるように、バイパス管路35
内を流れるガス22の流量を調整する。
A damper 34 which is electrically connected to a pressure gauge 37 through a wiring 45 is provided in the induction ventilator inlet line 30. The damper 34 adjusts the flow rate of the exhaust gas 7 flowing in the induction ventilator inlet pipe 30 according to a signal from the pressure gauge 37 so that the pressure in the gasifier 3 becomes a predetermined negative pressure. On the other hand, a damper 39 which is an on-off valve is provided in the bypass pipe 35, and the damper 39
It is electrically connected to the pressure gauge 37 through the wiring 41. The damper 39 operates when the damper 34 is fully opened, and in response to a signal from the pressure gauge 37, the gasifier 3
The pressure in the bypass line 35 is adjusted so that the internal pressure becomes a predetermined negative pressure.
The flow rate of the gas 22 flowing inside is adjusted.

【0017】このような構成の廃棄物ガス化溶融装置1
の動作と本発明の特徴部について説明する。まず、運転
起動時に、誘引通風機17が作動して誘引通風機入口管
路30内の気体を吸引し煙突管路32へ排出する。これ
により、廃棄物ガス化溶融装置1内の圧力は、図2に示
すように下流側から順次減圧される。また、廃棄物ガス
化溶融装置1の運転中、ガス化炉3に設けられた圧力計
37は、ガス化炉3内の圧力を検出し、検出した圧力の
信号を、ダンパー34及び39にへ発信する。
The waste gasification and melting apparatus 1 having such a configuration
The operation of the present invention and the features of the present invention will be described. First, when the operation is started, the induction ventilator 17 operates to suck the gas in the induction ventilator inlet conduit 30 and discharge it to the chimney conduit 32. Thereby, the pressure in the waste gasification and melting apparatus 1 is sequentially reduced from the downstream side as shown in FIG. During the operation of the waste gasification and melting apparatus 1, the pressure gauge 37 provided in the gasification furnace 3 detects the pressure in the gasification furnace 3 and sends a signal of the detected pressure to the dampers 34 and 39. send.

【0018】ガス化炉3内が所定の負圧まで減圧された
後、運転が開始され、供給ホッパ31に貯留されている
廃棄物20は、供給装置21により、供給装置21の排
出部分へ送られる。シール装置33は、排出部に送られ
た廃棄物20を、例えば、重さや光センサーなどにより
検知することで作動し、供給装置21の排出部分と搬送
路19とを連通させる。これにより、廃棄物20は搬送
路19内を滑り落ち、ガス化炉3へ投入される。廃棄物
20を投入後、シール装置33は再び排出部分と搬送路
19とを遮断する。一方、ガス化炉3内に投入された廃
棄物20は、ガス化炉3の底部から供給される流動化空
気と反応し熱分解される。廃棄物20が熱分解されるこ
とにより、ガス化炉3内では可燃性のガス22、未燃カ
ーボンであるチャー23、及び灰分が生成され排出され
る。
After the pressure in the gasification furnace 3 is reduced to a predetermined negative pressure, the operation is started, and the waste 20 stored in the supply hopper 31 is sent to the discharge part of the supply device 21 by the supply device 21. Can be The seal device 33 operates by detecting the waste 20 sent to the discharge unit by, for example, a weight or an optical sensor, and makes the discharge portion of the supply device 21 communicate with the transport path 19. Thereby, the waste 20 slides down in the transport path 19 and is injected into the gasification furnace 3. After the waste 20 is charged, the sealing device 33 shuts off the discharge portion and the transport path 19 again. On the other hand, the waste 20 charged into the gasification furnace 3 reacts with fluidized air supplied from the bottom of the gasification furnace 3 and is thermally decomposed. As the waste 20 is thermally decomposed, combustible gas 22, char 23 which is unburned carbon, and ash are generated and discharged in the gasification furnace 3.

【0019】排出されたガス22、チャー23及び灰分
は、ガス化炉出口管路24内を通り溶融炉5へ送られ
る。溶融炉5に送られたガス22及びチャー23は、炉
内で燃焼用の空気と混合され燃焼させられる。溶融炉5
内では、燃焼によって発生した熱により灰分が溶融さ
れ、溶融された灰分は図示していないスラグとして溶融
炉5の外へ排出される。溶融炉5内の燃焼により発生し
た排ガス7は、溶融炉出口管路25内を通流して燃焼室
9に送られる。なお、溶融炉5内では、窒素酸化物の発
生を抑制するために、空気過剰率を比較的低くした運転
を行っているので、溶融炉5から排出される排ガス7内
に、完全に燃焼していない未燃焼ガスが含まれる場合が
ある。しかし、燃焼室9に流入した未燃焼ガスは、燃焼
室9内で完全に燃焼される。
The discharged gas 22, char 23 and ash are sent to the melting furnace 5 through the gasification furnace outlet line 24. The gas 22 and the char 23 sent to the melting furnace 5 are mixed with air for combustion in the furnace and burned. Melting furnace 5
Inside, the ash is melted by the heat generated by the combustion, and the melted ash is discharged out of the melting furnace 5 as slag (not shown). The exhaust gas 7 generated by the combustion in the melting furnace 5 flows through the melting furnace outlet pipe 25 and is sent to the combustion chamber 9. Since the operation in the melting furnace 5 is performed with a relatively low excess air ratio in order to suppress the generation of nitrogen oxides, the exhaust gas 7 discharged from the melting furnace 5 is completely burned. Unburned gas may be included. However, the unburned gas flowing into the combustion chamber 9 is completely burned in the combustion chamber 9.

【0020】完全に燃焼された排ガス7は、燃焼室出口
管路26内を通流して熱回収ボイラ11に送られる。熱
回収ボイラ11へ送られた排ガス7の熱は、熱回収ボイ
ラ11内で回収される。熱回収ボイラ11内で熱を回収
された排ガス7は、熱回収ボイラ出口管路28内を経て
集塵装置15内で排ガス7に含まれる煤塵13を取り除
かれた後、誘引通風機入口管路30内へ流入する。誘引
通風機入口管路30内へ送られた排ガスは、誘引通風機
17により誘引、つまり吸引されて、煙突管路32へ送
られ、煙突27から大気中へ放出される。
The completely burned exhaust gas 7 flows through the combustion chamber outlet pipe 26 and is sent to the heat recovery boiler 11. The heat of the exhaust gas 7 sent to the heat recovery boiler 11 is recovered in the heat recovery boiler 11. The exhaust gas 7 from which heat has been recovered in the heat recovery boiler 11 passes through a heat recovery boiler outlet pipe 28, and after the dust 13 contained in the exhaust gas 7 has been removed in the dust collector 15, the induction ventilator inlet pipe It flows into 30. The exhaust gas sent into the induction ventilator inlet duct 30 is attracted, that is, sucked by the induction ventilator 17, sent to the chimney duct 32, and discharged from the chimney 27 into the atmosphere.

【0021】廃棄物ガス化溶融装置1の運転中、ダンパ
ー34は、圧力計37からの信号に応じて誘引通風機入
口管路30の流量を調整する。例えば、ガス化炉3に投
入される廃棄物20の供給量が一時的に減少したり、比
較的ガスを発生させない組成の廃棄物20が供給される
ことで、ガス化炉3内の圧力が所定の負圧より低くなる
場合、圧力計37からの信号を受けたダンパー34は、
信号に応じてダンパー34の開度を調整し、誘引通風機
入口管路30内を流れる排ガス7の流量を減らす。これ
により、誘引通風機17に吸引される排ガス7の量が減
り、つまり、誘引通風機17がガス流路内を減圧し難く
なり、ガス化炉3内の圧力が上昇して所定の負圧にな
る。
During operation of the waste gasification and melting apparatus 1, the damper 34 adjusts the flow rate of the induction ventilator inlet line 30 according to a signal from the pressure gauge 37. For example, the supply amount of the waste 20 supplied to the gasification furnace 3 is temporarily reduced, or the waste 20 having a composition that does not relatively generate gas is supplied. When the pressure becomes lower than the predetermined negative pressure, the damper 34 receiving the signal from the pressure gauge 37
The opening degree of the damper 34 is adjusted according to the signal to reduce the flow rate of the exhaust gas 7 flowing in the induction ventilator inlet conduit 30. As a result, the amount of the exhaust gas 7 sucked into the induction ventilator 17 is reduced, that is, it becomes difficult for the induction ventilator 17 to reduce the pressure in the gas flow path, and the pressure in the gasification furnace 3 increases to a predetermined negative pressure. become.

【0022】また、ガス化炉3に投入される廃棄物20
の供給量が一時的に増加したり、比較的大量にガスを発
生させる組成の廃棄物20が供給されることで、ガス化
炉3内の圧力が所定の負圧より高くなる場合、圧力計3
7からの信号を受けたダンパー34は、信号に応じてダ
ンパー34を調整し、誘引通風機入口管路30内を流れ
る排ガス7の流量を増やす。したがって、誘引通風機1
7に吸引される排ガス7の量が増え、つまり、誘引通風
機17がガス流路内を減圧し易くなり、ガス化炉3内の
圧力が低下して所定の負圧になる。
The waste 20 charged into the gasifier 3
When the pressure in the gasifier 3 becomes higher than a predetermined negative pressure due to a temporary increase in the supply amount of the gas or a supply of the waste 20 having a composition that generates a relatively large amount of gas, 3
The damper 34 that has received the signal from 7 adjusts the damper 34 according to the signal, and increases the flow rate of the exhaust gas 7 flowing in the induction ventilator inlet line 30. Therefore, the induced draft fan 1
The amount of the exhaust gas 7 sucked by the exhaust gas 7 increases, that is, the induction ventilator 17 easily reduces the pressure in the gas flow path, and the pressure in the gasification furnace 3 decreases to a predetermined negative pressure.

【0023】このように、ダンパー34によりガス化炉
3内の圧力が所定の負圧に保たれている場合、ダンパー
39は作動せず、ダンパー39は閉じられている。しか
しながら、ガス化炉3に投入される廃棄物20の供給量
がさらに増加すると、ダンパー34が全開であるにもか
かわらず、ガス化炉3内を負圧に保てない場合がある。
この場合、圧力計37からガス化炉3内が所定の負圧以
上の圧力である信号を受信することでダンパー39が開
き、ガス化炉3と溶融炉出口管路25とが連通される。
溶融炉出口管路25内の圧力は、ガス化炉出口管路24
や溶融炉5内の圧力より低いため、ガス化炉3内のガス
22は、バイパス管路35内を通流し、溶融炉出口管路
25内へ流れる。
As described above, when the pressure in the gasification furnace 3 is maintained at a predetermined negative pressure by the damper 34, the damper 39 does not operate and the damper 39 is closed. However, if the supply amount of the waste 20 charged into the gasification furnace 3 further increases, the inside of the gasification furnace 3 may not be maintained at a negative pressure even though the damper 34 is fully opened.
In this case, the damper 39 is opened by receiving a signal indicating that the pressure inside the gasification furnace 3 is equal to or higher than the predetermined negative pressure from the pressure gauge 37, and the gasification furnace 3 and the melting furnace outlet pipe 25 are connected.
The pressure in the melting furnace outlet line 25 is equal to the gasification furnace outlet line 24.
Since the pressure is lower than the pressure in the melting furnace 5, the gas 22 in the gasification furnace 3 flows through the bypass pipe 35 and flows into the melting furnace outlet pipe 25.

【0024】これにより、ガス化炉3内の圧力が低下し
ガス化炉3内が所定の負圧になると、圧力計37は、ガ
ス化炉3内の圧力が所定の負圧である信号をダンパー3
9へ発信する。信号を受信することでダンパー39は閉
じてバイパス管路35を塞ぐ。なお、バイパス管路35
内を通流して溶融炉出口管路25へ流入したガス22
は、燃焼室9に導かれ、燃焼室9内で完全に燃焼され
る。燃焼室9での燃焼により発生した排ガス7は、熱回
収ボイラ11で熱回収され、集塵装置15で排ガス7に
含まれる煤塵13を取り除かれた後、誘引通風機17、
煙突27を経て大気中に放出される。
As a result, when the pressure in the gasification furnace 3 decreases and the inside of the gasification furnace 3 becomes a predetermined negative pressure, the pressure gauge 37 outputs a signal indicating that the pressure in the gasification furnace 3 is the predetermined negative pressure. Damper 3
Call 9 Upon receiving the signal, the damper 39 closes and closes the bypass line 35. In addition, the bypass pipe 35
22 flowing into the furnace and flowing into the outlet line 25 of the melting furnace
Is guided to the combustion chamber 9 and is completely burned in the combustion chamber 9. The exhaust gas 7 generated by the combustion in the combustion chamber 9 is heat-recovered by the heat recovery boiler 11, and after the dust 13 included in the exhaust gas 7 is removed by the dust collecting device 15,
It is released to the atmosphere via a chimney 27.

【0025】このように、本実施形態の廃棄物ガス化溶
融装置1では、ガス化炉3内の圧力が所定の負圧より上
昇してしまった場合に、ガス化炉3と溶融炉出口管路2
5とをバイパス管路35により連通させることで、ガス
化炉3内で発生したガス22の一部を、溶融炉5を介さ
ずに溶融炉5より内部の圧力の低い溶融炉出口管路25
内へ流すことができる。これにより、溶融炉5が減圧さ
れてからガス化炉3が減圧される従来の構成に比べて、
溶融炉5内が減圧され難く、ガス化炉3から溶融炉5内
にガス22が流入し難い場合であっても、ガス化炉3内
のガス22を下流側に排出することができ、ガス化炉3
内を減圧して負圧に保つことができる。つまり、ガス化
炉3内で発生したガスの量に関係無く、ガス化炉3内を
減圧して負圧に保つことができる。
As described above, in the waste gasification and melting apparatus 1 of this embodiment, when the pressure in the gasification furnace 3 rises above a predetermined negative pressure, the gasification furnace 3 and the melting furnace outlet pipe Road 2
5 is communicated by the bypass line 35, so that a part of the gas 22 generated in the gasification furnace 3 can be transferred to the melting furnace outlet line 25 having a lower internal pressure than the melting furnace 5 without passing through the melting furnace 5.
Can be flushed into. Thereby, compared with the conventional configuration in which the pressure of the melting furnace 5 is reduced and then the pressure of the gasification furnace 3 is reduced,
Even when the pressure in the melting furnace 5 is hard to be reduced and the gas 22 is hard to flow from the gasification furnace 3 into the melting furnace 5, the gas 22 in the gasification furnace 3 can be discharged to the downstream side, Furnace 3
The interior can be depressurized and maintained at a negative pressure. That is, regardless of the amount of gas generated in the gasification furnace 3, the inside of the gasification furnace 3 can be depressurized and maintained at a negative pressure.

【0026】さらに、ガス化炉3内を減圧して負圧に保
つことができることにより、ガス化炉3内のガス22が
搬送路19を介してガス化炉3の外部に放出されること
を防止することができ、廃棄物ガス化溶融装置の運転を
より安全に行うことができる。また、本発明は、溶融炉
5内が減圧され難く、ガス化炉3から溶融炉5内にガス
22が流入し難いガス化炉3の圧力を低下させることが
できることから、例えば、溶融炉を備えていないゴミ焼
却装置に設けられていた誘引通風機など、ガスを誘引す
る能力が比較的小さい誘引通風機を用いることができ
る。
Further, since the inside of the gasification furnace 3 can be maintained at a negative pressure by reducing the pressure, the gas 22 in the gasification furnace 3 is released to the outside of the gasification furnace 3 through the transfer path 19. Thus, the waste gasification and melting apparatus can be operated more safely. In addition, the present invention can reduce the pressure of the gasification furnace 3 in which the pressure in the melting furnace 5 is hard to be reduced and the gas 22 hardly flows into the melting furnace 5 from the gasification furnace 3. It is possible to use an induction ventilator having a relatively small ability to attract gas, such as an induction ventilator provided in a garbage incinerator not provided.

【0027】(第2の実施形態)本発明を適用してなる
廃棄物ガス化溶融装置の第2の実施形態について図3を
参照して説明する。図3は、本発明を適用してなる廃棄
物ガス化溶融装置50の概略構成と動作を示す断面図で
ある。なお、本実施形態では、第1の実施形態と同一の
ものには同じ符号を付して説明を省略し、第1の実施形
態と相違する構成及び特徴部などについて説明する。
(Second Embodiment) A second embodiment of the waste gasification and melting apparatus to which the present invention is applied will be described with reference to FIG. FIG. 3 is a cross-sectional view showing a schematic configuration and operation of a waste gasification and melting apparatus 50 to which the present invention is applied. Note that, in the present embodiment, the same components as those in the first embodiment are denoted by the same reference numerals, and the description thereof will be omitted, and the configuration and features different from those in the first embodiment will be described.

【0028】本実施形態と第1の実施形態との相違する
点は、図3に示すように、ガス化炉3と溶融炉出口管路
25とを連絡するバイパス管路35の代わりに、搬送路
19と溶融炉出口管路25とを連絡するバイパス管路5
2を設けた点である。バイパス管路52には、配線41
を通じて圧力計37と電気的に接続されたダンパー39
が設けられている。ダンパー39は、ダンパー34が全
開になった場合に作動し、ガス化炉3内の圧力が所定の
負圧になるように、バイパス管路52内を流れるガス2
2の流量を調整する。
The difference between the present embodiment and the first embodiment is that, as shown in FIG. 3, instead of a bypass pipe 35 connecting the gasification furnace 3 and the melting furnace outlet pipe 25, a conveying pipe is provided. Bypass line 5 connecting line 19 and melting furnace outlet line 25
2 is provided. In the bypass conduit 52, the wiring 41
Damper 39 electrically connected to the pressure gauge 37 through the
Is provided. The damper 39 is activated when the damper 34 is fully opened, and the gas 2 flowing through the bypass pipe 52 is controlled so that the pressure in the gasification furnace 3 becomes a predetermined negative pressure.
Adjust the flow rate of 2.

【0029】このような構成の本実施形態の廃棄物ガス
化溶融装置50の動さと特徴部について説明する。な
お、運転の開始、及びガス化炉3内の圧力が所定の負圧
より低い圧力である場合の動作の説明は、第1の実施形
態と同様なので省略する。
The operation and features of the waste gasification and melting apparatus 50 of this embodiment having the above-described configuration will be described. The description of the operation when the operation is started and the operation when the pressure in the gasification furnace 3 is lower than the predetermined negative pressure are the same as those in the first embodiment, and a description thereof will be omitted.

【0030】廃棄物ガス化溶融装置50の運転中に、ガ
ス化炉3に投入される廃棄物20の供給量が増加した
り、比較的大量にガスを発生させる組成の廃棄物20が
供給されると、ダンパー34は全開であるにもかかわら
ず、ガス化炉3内を負圧に保てない場合がある。この場
合、圧力計37は、ガス化炉3内の圧力が所定の負圧よ
り高いことを伝える信号をダンパー39へ発信しする。
圧力計37からの信号を受信することでダンパー39は
開き、搬送路19と溶融炉出口管路25が連通される。
溶融炉出口管路25内の圧力は、溶融炉5、ガス化炉出
口管路24及びガス化炉3内の圧力より低いため、搬送
路19内のガス22はバイパス管路52内を通流して溶
融炉5と燃焼室9との間の溶融炉出口管路25へ流入す
る。これにより、搬送路19内の圧力が低下し、それに
伴いガス化炉3内の圧力も低下する。
During operation of the waste gasification / melting apparatus 50, the supply amount of the waste 20 supplied to the gasification furnace 3 increases, or the waste 20 having a composition that generates gas in a relatively large amount is supplied. Then, even though the damper 34 is fully open, the inside of the gasification furnace 3 cannot be maintained at a negative pressure in some cases. In this case, the pressure gauge 37 transmits to the damper 39 a signal indicating that the pressure in the gasification furnace 3 is higher than a predetermined negative pressure.
Upon receiving the signal from the pressure gauge 37, the damper 39 is opened, and the transfer path 19 and the melting furnace outlet pipe 25 are connected.
Since the pressure in the melting furnace outlet pipe 25 is lower than the pressure in the melting furnace 5, the gasification furnace outlet pipe 24, and the gasification furnace 3, the gas 22 in the transfer path 19 flows through the bypass pipe 52. Then, it flows into a melting furnace outlet line 25 between the melting furnace 5 and the combustion chamber 9. As a result, the pressure in the transport path 19 decreases, and accordingly, the pressure in the gasification furnace 3 also decreases.

【0031】その後、ガス化炉3内の圧力が所定の負圧
になると、圧力計37は、ダンパー39へ信号を発信す
る。信号を受けたダンパー39は、閉じてバイパス管路
52の流路を遮断する。なお、バイパス管路52内を通
流して溶融炉出口管路25へ流入したガス22は、燃焼
室9に導かれ、燃焼室9内で完全に燃焼される。燃焼室
9での燃焼により発生した排ガス7は、熱回収ボイラ1
1で熱回収され、集塵装置15で排ガス7に含まれる煤
塵13を取り除かれた後、誘引通風機17、煙突27を
経てガス化炉3の外部に放出される。
Thereafter, when the pressure in the gasification furnace 3 reaches a predetermined negative pressure, the pressure gauge 37 transmits a signal to the damper 39. Upon receiving the signal, the damper 39 closes and shuts off the flow path of the bypass conduit 52. The gas 22 flowing through the bypass pipe 52 and flowing into the melting furnace outlet pipe 25 is guided to the combustion chamber 9 and is completely burned in the combustion chamber 9. The exhaust gas 7 generated by the combustion in the combustion chamber 9 is supplied to the heat recovery boiler 1.
After the heat is recovered in 1 and the dust 13 contained in the exhaust gas 7 is removed by the dust collecting device 15, the dust is discharged to the outside of the gasification furnace 3 through the induction draft fan 17 and the chimney 27.

【0032】このように、本実施形態の廃棄物ガス化溶
融装置50では、ガス化炉3内の圧力が所定の負圧より
も高くなった場合に、搬送路19と溶融炉出口管路25
とをバイパス管路52により連通させることで、ガス化
炉3内で発生し、搬送路19へ流入したガス22の一部
を、減圧し難い溶融炉5を介さずに溶融炉5内より圧力
の低い溶融炉出口管路25へ流すことができる。これに
より、溶融炉5が減圧されてからガス化炉3が減圧され
る従来の構成に比べて、溶融炉5内が減圧され難く、ガ
ス化炉3から溶融炉5内にガス22が流入し難い場合で
あっても、ガス化炉3から搬送路19へ流れたガス22
を溶融炉5より下流側へ排出することができ、ガス化炉
3内を減圧して負圧に保つことができる。つまり、ガス
化炉3内で発生したガスの量に関係無く、ガス化炉3内
を減圧して負圧に保つことができる。
As described above, in the waste gasification and melting apparatus 50 of the present embodiment, when the pressure in the gasification furnace 3 becomes higher than the predetermined negative pressure, the conveyance path 19 and the melting furnace outlet pipe 25
Is communicated by the bypass pipe 52, so that a part of the gas 22 generated in the gasification furnace 3 and flowing into the transfer path 19 is supplied from the inside of the melting furnace 5 without passing through the melting furnace 5 which is difficult to decompress. To the lower melting furnace outlet line 25. As a result, as compared with the conventional configuration in which the pressure in the melting furnace 5 is reduced and then the pressure in the gasification furnace 3 is reduced, the pressure in the melting furnace 5 is less likely to be reduced, and the gas 22 flows into the melting furnace 5 from the gasification furnace 3. Even if difficult, the gas 22 flowing from the gasification furnace 3 to the transfer path 19
Can be discharged downstream of the melting furnace 5, and the pressure in the gasification furnace 3 can be reduced to maintain a negative pressure. That is, regardless of the amount of gas generated in the gasification furnace 3, the pressure inside the gasification furnace 3 can be reduced to maintain a negative pressure.

【0033】さらに、ガス化炉3から搬送路19を介し
て供給装置21へ流れ出すガス22を優先的にバイパス
管路52内へ流すことができ、ガス化炉3内のガス22
が搬送路19を介してガス化炉3の外部へより放出され
難くすることができる。また、供給装置21に近い位置
からガス22を抜き出すことができるので、第1の実施
の形態よりも応答性がよい。したがって、廃棄物ガス化
溶融装置の運転をさらに安全に行うことができる。
Further, the gas 22 flowing from the gasification furnace 3 to the supply device 21 via the transfer path 19 can be preferentially flown into the bypass pipe 52, and the gas 22 in the gasification furnace 3
From the gasification furnace 3 via the transfer path 19 can be made less likely to be released. Further, since the gas 22 can be extracted from a position close to the supply device 21, the responsiveness is better than in the first embodiment. Therefore, the operation of the waste gasification and melting apparatus can be performed more safely.

【0034】本発明の廃棄物ガス化溶融装置は、バイパ
ス管路35、52を設け、溶融炉5より上流側のガス2
2を、溶融炉5を介さずに誘引通風機17へ送ること
で、ガス化炉3の圧力を低下させることができればよい
ので、第1及び第2の実施形態に限らず、様々な構成と
することができる。例えば、第1の実施の形態では、バ
イパス管路35がガス化炉3に連結された構成となって
いるが、バイパス管路35はガス化炉出口管路24と溶
融炉出口管路25とを連通させる構成とすることができ
る。さらに、第1及び第2の実施の形態では、ダンパー
34が全開になり、かつ、ガス化炉3内の圧力が所定の
負圧より高くなった場合に、ダンパー39が開く制御を
行っているが、ダンパー34に関係無く、ガス化炉3内
の圧力が所定の負圧より高くなった場合に、ダンパー3
9が作動するという制御を行うこともできる。また、第
1及び第2の実施の形態では、ダンパー39は開閉を行
うことでバイパス管路35、52内にガス22を通流さ
せ、ガス化炉3内の圧力の調整を行っているが、例え
ば、ダンパー39が、ガス化炉3内の圧力に応じて開度
を調節できる構成とすることもできる。
The waste gasification and melting apparatus according to the present invention is provided with bypass pipes 35 and 52 and is provided with a gas 2 upstream of the melting furnace 5.
Since it is sufficient that the pressure of the gasification furnace 3 can be reduced by sending the gas 2 to the induction ventilator 17 without passing through the melting furnace 5, it is not limited to the first and second embodiments, and various configurations may be used. can do. For example, in the first embodiment, the bypass line 35 is connected to the gasification furnace 3, but the bypass line 35 is connected to the gasification furnace outlet line 24 and the melting furnace outlet line 25. Can be configured to communicate with each other. Further, in the first and second embodiments, control is performed to open the damper 39 when the damper 34 is fully opened and the pressure in the gasification furnace 3 becomes higher than a predetermined negative pressure. However, regardless of the damper 34, when the pressure in the gasification furnace 3 becomes higher than a predetermined negative pressure,
9 can be controlled. In the first and second embodiments, the damper 39 opens and closes so that the gas 22 flows through the bypass pipes 35 and 52 to adjust the pressure in the gasification furnace 3. For example, it is also possible to adopt a configuration in which the opening degree of the damper 39 can be adjusted according to the pressure in the gasification furnace 3.

【0035】また、本実施形態では、誘引通風機17を
用いたが、誘引通風機17などのファン手段の代わり
に、例えば、誘引通風機入口管路30内の排ガス7をピ
ストンなどで吸引して煙突管路32へ送る装置を用いる
ことができる。また、誘引通風機17により誘引通風機
入口管路30内を通流する排ガス7の流量を調整できる
場合には、ダンパー34を設けない構成とすることがで
きる。さらに、ガス化炉3内の圧力を計測するために圧
力計37を設け、ダンパー39と電気的に接続された構
成となっているが、本発明ではガス化炉3内の圧力に応
じて、ダンパー39を開閉することができればよいの
で、ガス化炉3内の圧力をダンパー39へ伝えることが
できれば、圧力計37に限らず、様々な手段を用いるこ
とができる。
In the present embodiment, the induction ventilator 17 is used, but instead of the fan means such as the induction ventilator 17, for example, the exhaust gas 7 in the induction ventilator inlet pipe 30 is sucked by a piston or the like. A device that feeds to the chimney line 32 can be used. When the flow rate of the exhaust gas 7 flowing in the induction ventilator inlet duct 30 can be adjusted by the induction ventilator 17, the damper 34 can be omitted. Further, a pressure gauge 37 is provided to measure the pressure in the gasification furnace 3 and electrically connected to the damper 39. In the present invention, according to the pressure in the gasification furnace 3, It is only necessary to be able to open and close the damper 39, so that not only the pressure gauge 37 but also various means can be used as long as the pressure in the gasification furnace 3 can be transmitted to the damper 39.

【0036】本発明のバイパス管路は、第1及び第2の
実施形態の構成に限らず、ガス化炉、溶融炉及び誘引通
風機を備えた廃棄物ガス化溶融装置であれば、様々な構
成の廃棄物ガス化溶融装置に適用することができる。
The bypass conduit of the present invention is not limited to the constitutions of the first and second embodiments, but may be any of various waste gasification and melting apparatuses provided with a gasification furnace, a melting furnace and an induction ventilator. The present invention can be applied to a waste gasification and melting apparatus having the above configuration.

【0037】[0037]

【発明の効果】本発明によれば、廃棄物ガス化溶融装置
のガス化炉で発生するガスの量に関係無く、ガス化炉内
の圧力を負圧に保つことができる。
According to the present invention, the pressure in the gasification furnace can be maintained at a negative pressure regardless of the amount of gas generated in the gasification furnace of the waste gasification and melting apparatus.

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

【図1】本発明を適用してなる廃棄物ガス化溶融装置の
第1の実施形態の概略構成と動さとを示した概略断面図
である。
FIG. 1 is a schematic sectional view showing a schematic configuration and operation of a first embodiment of a waste gasification and melting apparatus to which the present invention is applied.

【図2】従来の廃棄物ガス化溶融装置の圧力の変化を示
したグラフである。
FIG. 2 is a graph showing a change in pressure of a conventional waste gasification and melting apparatus.

【図3】本発明を適用してなる廃棄物ガス化溶融装置の
第2の実施形態の概略構成と動さとを示した概略断面図
である。
FIG. 3 is a schematic cross-sectional view showing a schematic configuration and operation of a second embodiment of a waste gasification and melting apparatus to which the present invention is applied.

【符号の説明】[Explanation of symbols]

3 ガス化炉 5 溶融炉 22 ガス 25 溶融炉出口管路 35 バイパス管路 3 Gasifier 5 Melting furnace 22 Gas 25 Melting furnace outlet line 35 Bypass line

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) F23G 5/50 F23J 1/00 B F23J 1/00 B09B 3/00 303K Fターム(参考) 3K061 AB02 AB03 BA02 BA06 NB30 3K062 AB02 AB03 DA11 DB16 3K078 AA02 AA06 BA03 CA02 4D004 AA46 CA27 CA29 DA02 DA07──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI theme coat ゛ (reference) F23G 5/50 F23J 1/00 B F23J 1/00 B09B 3/00 303K F-term (reference) 3K061 AB02 AB03 BA02 BA06 NB30 3K062 AB02 AB03 DA11 DB16 3K078 AA02 AA06 BA03 CA02 4D004 AA46 CA27 CA29 DA02 DA07

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 廃棄物を熱分解するガス化炉と、前記熱
分解で生じたガスが通流するガス流路と、該ガス流路に
設けられ前記ガス流路内に前記ガスを誘引してを通流さ
せる誘引通風機と、前記ガス流路の前記ガス化炉及び前
記誘引通風機間の部分に設けられ前記ガス及び前記ガス
に同伴されている未燃分を燃焼させると共に灰分を溶融
する溶融炉とを備えた廃棄物ガス化溶融装置であって、 前記ガス化炉内で発生した前記ガスを、前記溶融炉をバ
イパスさせて前記ガス流路の前記溶融炉と前記誘引通風
機との間の部分に流入させるバイパス流路を設けたこと
を特徴とする廃棄物ガス化溶融装置。
1. A gasifier for thermally decomposing waste, a gas passage through which a gas generated by the pyrolysis flows, and a gas passage provided in the gas passage to attract the gas into the gas passage. And an unburned gas that is provided in a portion of the gas flow path between the gasification furnace and the induced draft fan that burns the gas and unburned components that accompany the gas, and melts ash. A waste gasification / melting apparatus comprising: a melting furnace; and the gas generated in the gasification furnace, wherein the melting furnace is bypassed to the melting furnace, A waste gasification / melting apparatus, wherein a bypass flow path is provided to flow into a portion between the two.
【請求項2】 廃棄物を熱分解するガス化炉と、該ガス
化炉に廃棄物を搬送する搬送路と、前記熱分解で生じた
ガスが通流するガス流路と、該ガス流路に設けられ前記
ガス流路内に前記ガスを誘引してを通流させる誘引通風
機と、前記ガス流路の前記ガス化炉及び前記誘引通風機
間の部分に設けられ前記ガス及び前記ガスに同伴されて
いる未燃分を燃焼させると共に灰分を溶融する溶融炉と
を備えた廃棄物ガス化溶融装置であって、 前記ガス化炉から前記搬送路へ流入した前記ガスを、前
記溶融炉をバイパスさせて前記ガス流路の前記溶融炉と
前記誘引通風機との間の部分に流入させるバイパス流路
を設けたことを特徴とする廃棄物ガス化溶融装置。
2. A gasifier for thermally decomposing waste, a transport path for transporting waste to the gasifier, a gas flow path through which gas generated by the pyrolysis flows, and a gas flow path. An induction ventilator that is provided in the gas flow path for inducing the gas to flow therethrough, and the gas and the gas that are provided in a portion of the gas flow path between the gasification furnace and the induction ventilator. A waste gasification and melting apparatus comprising: a melting furnace for burning entrained unburned components and melting ash, wherein the gas flowing from the gasification furnace to the transfer path is passed through the melting furnace. A waste gasification and melting apparatus, wherein a bypass flow path is provided to be bypassed and flow into a portion of the gas flow path between the melting furnace and the induction ventilator.
【請求項3】 前記ガス化炉内の圧力に応じて、前記バ
イパス流路の開閉を制御する開閉弁を備えたことを特徴
とする請求項1または2に記載の廃棄物ガス化溶融装
置。
3. The waste gasification and melting apparatus according to claim 1, further comprising an on-off valve for controlling opening and closing of the bypass flow passage in accordance with a pressure in the gasification furnace.
JP2001105105A 2001-04-03 2001-04-03 Waste gasifying melting device Withdrawn JP2002303410A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001105105A JP2002303410A (en) 2001-04-03 2001-04-03 Waste gasifying melting device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001105105A JP2002303410A (en) 2001-04-03 2001-04-03 Waste gasifying melting device

Publications (1)

Publication Number Publication Date
JP2002303410A true JP2002303410A (en) 2002-10-18

Family

ID=18957857

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001105105A Withdrawn JP2002303410A (en) 2001-04-03 2001-04-03 Waste gasifying melting device

Country Status (1)

Country Link
JP (1) JP2002303410A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012110882A (en) * 2010-11-22 2012-06-14 Th Elema Engineering Co Ltd Pyrolyzer for waste

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012110882A (en) * 2010-11-22 2012-06-14 Th Elema Engineering Co Ltd Pyrolyzer for waste

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