JP2876455B2 - Method for producing carbide and production apparatus used for same - Google Patents

Method for producing carbide and production apparatus used for same

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Publication number
JP2876455B2
JP2876455B2 JP6103499A JP10349994A JP2876455B2 JP 2876455 B2 JP2876455 B2 JP 2876455B2 JP 6103499 A JP6103499 A JP 6103499A JP 10349994 A JP10349994 A JP 10349994A JP 2876455 B2 JP2876455 B2 JP 2876455B2
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JP
Japan
Prior art keywords
radiant
carbide
furnace
outer furnace
producing
Prior art date
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JP6103499A
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Japanese (ja)
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JPH07280226A (en
Inventor
洋司 平井
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Individual
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Individual
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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、産業廃棄物(例えば各
種プラスチック類、各種ゴム類、石油残渣、石油ピッ
チ、ヤシ殻・砂糖きびの絞滓・木材又は籾殻等の農産廃
棄物等)を燃焼させ活性炭の原料として使用される炭化
物の製造方法及びこれに用いる製造装置に関する。
The present invention relates to the burning of industrial waste (eg, various plastics, various rubbers, petroleum residues, petroleum pitch, agricultural waste such as coconut shells, sugar cane slag, wood, rice husk, etc.). The present invention relates to a method for producing a carbide used as a raw material of activated carbon and a production apparatus used for the same.

【0002】[0002]

【従来の技術】従来、炭化物を得るにあたって、炭素質
材料の自燃若しくは外熱型の熱分解又はこれらの併用方
法が用いられ、高温で炭化すると炭素細孔の収縮がおこ
り、この炭化物を用いての活性炭賦活活性作業は困難性
をともなっていた。また、低温での炭化は、炭素生成結
晶体の表面及びその相互間の裂け目や細孔部にタールの
一部が残存したり、組織の壊れた炭素によって閉鎖され
ることが多く、この炭化物を用いた活性炭は吸着能力及
び硬度等の性能低下をともなっていた。このため、活性
炭の原料として使用される炭化物は、ヤシ殻・おがくず
・石炭又は石油ピッチ等の如く炭素生成が安定している
炭素質材料が用いられ、プラスチック類及びゴム類の使
用は困難性をともなっていた。特に、プラスチック類及
びゴム類の焼却には1000℃〜1300℃にも達する
高温によるNOx、SOxの発生が問題であり、燃焼温
度が過熱しない様にするため水蒸気を共存させることが
行われ、例えば1993年6月10日 株式会社 明現
社発行『廃棄物焼却炉−計画と設計』 第97頁4.1
4.2に記載がある。この記載の場合は燃焼に必要な適
性空気量を確保することが必須条件とされている。この
ためこの方法では水蒸気の導入により過熱防止は可能で
あるが、空気導入により燃焼後得られる炭化物に灰分が
残り、発生するNOx、SOxを極端に減らすことは困
難であり、活性炭の原料として使用される炭化物の製造
方法としては不十分なものである。
2. Description of the Related Art Conventionally, in order to obtain carbide, self-combustion of carbonaceous material or pyrolysis of an external heat type or a combination thereof has been used. When carbonized at a high temperature, carbon pores shrink, and this carbide is used. Activated carbon activation work was difficult. In addition, carbonization at a low temperature often causes a portion of tar to remain on the surface of the carbon-forming crystals and cracks and pores between them, and is closed by carbon whose structure has been broken, and this carbide is The activated carbon used had a decrease in performance such as adsorption capacity and hardness. For this reason, the carbonaceous material used as the raw material of the activated carbon is a carbonaceous material such as coconut shell, sawdust, coal or petroleum pitch, whose carbon generation is stable, and the use of plastics and rubbers is difficult. It was with. In particular, in the incineration of plastics and rubbers, the generation of NOx and SOx due to high temperatures of as high as 1000 ° C. to 1300 ° C. is a problem. In order to prevent the combustion temperature from overheating, steam is coexisted. June 10, 1993 Meijigen Co., Ltd. “Waste Incinerator-Planning and Design” p. 97 4.1
See 4.2. In this case, it is an essential condition to secure an appropriate amount of air necessary for combustion. Therefore, in this method, overheating can be prevented by introducing steam, but ash remains in the carbide obtained after combustion by introducing air, and it is difficult to extremely reduce NOx and SOx generated. However, it is not sufficient as a method for producing carbides.

【0003】[0003]

【発明が解決しようとする課題】本発明は、産業廃棄物
を燃焼させ、燃焼温度を低く保ちながら十分炭化がなさ
れ、燃焼ガス中のNOx、SOxの発生を極力抑えるこ
とができ、非炭素生成分の含有が抑えられた高品位な炭
化物の製造方法及びこれに用いる製造装置を得ることを
目的とする。
SUMMARY OF THE INVENTION The present invention is intended to burn industrial waste, sufficiently carbonize it while keeping the combustion temperature low, minimize the generation of NOx and SOx in the combustion gas, and reduce non-carbon generation. It is an object of the present invention to obtain a method for producing high-quality carbide in which the content of carbon is suppressed and a production apparatus used for the method.

【0004】[0004]

【課題を解決するための手段】本発明は前記目的を達成
するものであって、次のようなものである。すなわち、
請求項1に係るものは、燃焼炉内において外気遮断下で
水蒸気を噴霧しつつ産業廃棄物を燃焼させるようにした
炭化物の製造方法において、燃焼炉を外側外炉と内側輻
射缶の二重構造とし前記外炉と前記輻射缶との間隙に向
けて燃料を噴射着火し前記輻射缶内に向けて水蒸気を噴
霧しつつ前記輻射缶内に収納された産業廃棄物を輻射熱
により燃焼させることを特徴とする炭化物の製造方法で
ある。請求項2に係るものは、燃焼炉内において外気遮
断下で不活性ガス又は不活性ガスと水蒸気の混合ガスを
噴霧しつつ産業廃棄物を燃焼させるようにした炭化物の
製造方法において、燃焼炉を外側外炉と内側輻射缶の二
重構造とし前記外炉と前記輻射缶との間隙に向けて燃料
を噴射着火し前記輻射缶内に向けて不活性ガス又は不活
性ガスと水蒸気の混合ガスを噴霧しつつ前記輻射缶内に
収納された産業廃棄物を輻射熱により燃焼させることを
特徴とする炭化物の製造方法である。請求項3に係るも
のは、燃焼炉の外側の円筒状外炉内側に円筒状輻射缶が
固着され、前記輻射缶の上端に着脱可能な蓋が嵌着さ
れ、前記外炉下部外側より前記外炉と前記輻射缶との間
隙に向けて設けたガスバーナーと、前記外炉底面外側よ
り前記外炉及び前記輻射缶を貫通し前記輻射缶内に向け
て設けた噴霧ノズルと、前記輻射缶の上面部と前記ガス
バーナー吸込み側に連通する煙道と、前記外炉外側に設
けた排気管と、前記ガスバーナーと連動可能に設けた前
記外炉内及び前記輻射缶内に突出する温度センサーと、
前記噴霧ノズルと連動可能に設けた前記輻射缶内に突出
する温度センサーとよりなることを特徴とする炭化物の
製造装置である。請求項4に係るものは、請求項3のも
のにおいて、輻射缶内下底に設けた台座と、前記台座上
に載置した籠形の火格子と、前記台座と前記火格子の間
隙に向けて設けた噴霧ノズルとよりなることを特徴とす
るものである。
SUMMARY OF THE INVENTION The present invention achieves the above object and is as follows. That is,
The method according to claim 1 is a method for producing carbide in which industrial waste is burned while spraying water vapor in a combustion furnace while shutting off outside air, wherein the combustion furnace has a double structure of an outer outer furnace and an inner radiant can. The fuel is injected and ignited toward the gap between the outer furnace and the radiant can, and the industrial waste stored in the radiant can is burned by radiant heat while spraying steam toward the radiant can. It is a method for producing carbide. The method according to claim 2 is a method for producing a carbide in which an industrial gas is burned while spraying an inert gas or a mixed gas of an inert gas and water vapor in a combustion furnace while shutting off the outside air. Injecting and igniting fuel toward the gap between the outer furnace and the radiant can with a double structure of an outer outer furnace and an inner radiant can, and inert gas or a mixed gas of inert gas and steam toward the radiant can. A method for producing a carbide, comprising burning industrial waste stored in the radiant can by radiant heat while spraying. According to the third aspect, a cylindrical radiant can is fixed to the inside of a cylindrical outer furnace outside the combustion furnace, a detachable lid is fitted to an upper end of the radiant can, and the outer side of the lower part of the outer furnace is attached to the outside. A gas burner provided toward the gap between the furnace and the radiant can, a spray nozzle provided through the outer furnace and the radiant can from outside the bottom of the outer furnace, and provided toward the inside of the radiant can, A flue communicating with the upper surface and the gas burner suction side, an exhaust pipe provided outside the outer furnace, and a temperature sensor protruding into the outer furnace and the radiant can provided in conjunction with the gas burner. ,
An apparatus for producing a carbide, comprising: a temperature sensor protruding into the radiant can provided in cooperation with the spray nozzle. According to a fourth aspect, in the third aspect, a pedestal provided at a lower bottom in the radiant can, a basket-shaped grate placed on the pedestal, and a gap between the pedestal and the grate. And a spray nozzle provided with the spray nozzle.

【0005】[0005]

【作用】各種プラスチック類、各種ゴム類、各種石油残
渣類及び各種農産廃棄物等の産業廃棄物は通常主として
炭素C、水素H、硫黄Sの三元素のいずれか又はそれら
の組合わせより成っているが、炭素成分の燃焼と水蒸気
との反応は、 式 C+HO=CO+H−2350Kcal/Kg で示される還元吸熱反応作用により炭素成分の発熱を吸
熱し温度上昇を抑制するよう作用する。産業廃棄物中の
非炭素生成分が炭化される過程で、水蒸気に接すると、
非炭素生成分又は組織の壊れた炭素は水蒸気に包み込ま
れ、炭素成分とは分離し、このため非炭素生成分又は組
織の壊れた炭素を含まない炭化物が得られるように作用
する。産業廃棄物に直接燃料を噴射着火せず外炉と輻射
缶の二重構造とし外炉と輻射缶との間隙に向けて燃料を
噴射着火し、輻射缶内に向けて水蒸気を噴霧しつつ空気
遮断下で輻射熱により燃焼させるので、輻射缶内温度は
300℃〜500℃の比較的低い温度に保つことがで
き、産業廃棄物の燃焼は輻射熱による熱分解によるた
め、灰分が極端に少なく有害物をほとんど含まない炭化
物が得られ、燃焼ガス中のNOx、SOxの発生を極力
抑えるように作用する。また、水蒸気に代えて不活性ガ
ス(例えば窒素ガス又は炭酸ガス)又は不活性ガスと水
蒸気の混合ガスを噴霧することにより、水蒸気噴霧の場
合と同様に温度の異常上昇を抑制し、生成される炭化物
が程よく多孔質化されて連続気泡型の通路を形成し活性
炭の原料として好適になるように作用する。また、輻射
缶内が台座と籠形の火格子よりなる二重構造であって、
燃焼終了後得られた火格子内に収納された炭化物及び残
存したワイヤー等を容易に他の容器に移動することが可
能である。
[Function] Industrial wastes such as various plastics, various rubbers, various petroleum residues, and various agricultural wastes usually mainly consist of one of the three elements of carbon C, hydrogen H and sulfur S or a combination thereof. However, the reaction between the combustion of the carbon component and the water vapor acts so as to absorb the heat of the carbon component and suppress the temperature rise by the reduction endothermic reaction represented by the formula C + H 2 O = CO + H 2 -2350 Kcal / Kg. In the process of carbonizing non-carbon products in industrial waste, when exposed to steam,
Non-carbon-producing or tissue-broken carbon is entrapped in water vapor and separates from the carbon component, thereby acting to obtain a non-carbon-producing or tissue-broken carbon-free carbide. The fuel is not injected directly into the industrial waste and the fuel is injected and ignited toward the gap between the outer furnace and the radiant can, and the air is sprayed into the radiant can while air is sprayed. Burning by radiant heat under cutoff, the temperature inside the radiant can can be kept at a relatively low temperature of 300 to 500 ° C. The burning of industrial waste is due to thermal decomposition by radiant heat, so ash content is extremely small and harmful substances Is obtained, and acts to minimize the generation of NOx and SOx in the combustion gas. Further, by spraying an inert gas (for example, a nitrogen gas or a carbon dioxide gas) or a mixed gas of an inert gas and steam in place of steam, an abnormal rise in temperature is suppressed and generated as in the case of steam spraying. The carbide is moderately made porous to form an open-cell-type passage and acts so as to be suitable as a raw material for activated carbon. The radiant can has a double structure consisting of a pedestal and a basket-shaped grate,
It is possible to easily move the carbide and the remaining wires and the like stored in the grate obtained after the end of combustion to another container.

【0006】[0006]

【実施例】本発明のを図面を参照して説明する。図1
は、本発明の炭化物の製造装置の一実施例の断面正面略
図である。図1において、円筒状の外炉1の上端内側に
円筒状の輻射缶2が固着され、輻射缶2の上端を外炉1
上端より突出させて着脱可能な輻射缶蓋4が嵌着されて
二重構造の燃焼炉18が構成されている。輻射缶2内下
底に台座14を設け、台座14上に輻射缶2上端付近に
まで達するメッシュ状籠形の火格子3が載置されてい
る。外炉1下部外側より外炉1と輻射缶2との間隙に向
けてガスバーナー10が設けられ、外炉1底面外側より
外炉1及び輻射缶2を貫通し輻射缶2内に向けて水蒸気
の噴霧ノズル11が複数個設けられている。尚台座14
及びメッシュ状籠形の火格子3は燃焼完了後の作業性向
上のために設けられてあり、必ずしも必要ではない。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described with reference to the drawings. FIG.
1 is a schematic cross-sectional front view of an embodiment of a carbide manufacturing apparatus according to the present invention. In FIG. 1, a cylindrical radiant can 2 is fixed to the inside of the upper end of a cylindrical outer furnace 1, and the upper end of the radiant can 2 is
A detachable radiant can lid 4 protruding from the upper end is fitted to form a combustion furnace 18 having a double structure. A pedestal 14 is provided at the lower bottom inside the radiant can 2, and the mesh-shaped basket-shaped grate 3 reaching near the upper end of the radiant can 2 is mounted on the pedestal 14. A gas burner 10 is provided from a lower outer side of the outer furnace 1 toward a gap between the outer furnace 1 and the radiant can 2, and steam passes through the outer furnace 1 and the radiant can 2 from the outer side of the bottom of the outer furnace 1 toward the inside of the radiant can 2. Are provided. Pedestal 14
The mesh-shaped grate 3 is provided for improving workability after the completion of combustion, and is not always necessary.

【0007】外炉1内に突出する温度センサー9と輻射
缶2内に突出する温度センサー8に連動作動する補助燃
料供給装置7と連結した混合ガスのガスバーナー10
と、輻射缶2内に突出する温度センサー8に連動作動す
る噴霧ノズル11が設けられている。輻射缶蓋4の上面
部に煙道13を設け煙道13の他端に着脱可能なジョイ
ント6を通じてガスバーナー10のフアン17の吸込み
側に煙道16を連通している。煙道13の輻射缶蓋4近
傍にフック5が固着されている。外炉1上部に排気管1
2が設られ、下流の熱交換器(図示省略)に連通してい
る。
A gas burner 10 of a mixed gas connected to an auxiliary fuel supply device 7 which operates in conjunction with a temperature sensor 9 projecting into the outer furnace 1 and a temperature sensor 8 projecting into the radiant can 2.
And a spray nozzle 11 that operates in conjunction with a temperature sensor 8 that protrudes into the radiation can 2. A flue 13 is provided on the upper surface of the radiation can lid 4, and the flue 16 is connected to the suction side of the fan 17 of the gas burner 10 through a detachable joint 6 at the other end of the flue 13. A hook 5 is fixed to the flue 13 near the radiation can lid 4. Exhaust pipe 1 on top of outer furnace 1
2 are provided and communicate with a downstream heat exchanger (not shown).

【0008】次に図1に基づき本発明の炭化物の製造方
法を説明する。煙道13はフック5に外部のクレーン等
(図示省略)を係合して、矢印A方向及びB方向に移動
させると、ジョイント6はフアン17の吸込み側煙道1
6との係合がはずれ矢印C〜D及びE〜F方向のいずれ
の方向にも移動可能とされているので、煙道13ととも
に輻射缶蓋4が移動し輻射缶2との嵌着を解除し、輻射
缶2が開口する。開口した輻射缶2に産業廃棄物として
例えば古タイヤ15を投入し、輻射缶蓋4を閉じる。次
いで、ガスバーナー10に着火し、外炉1と輻射缶2と
の間隙を600〜800℃に過熱する。この設定温度は
外炉1内の温度センサー9と補助燃料供給装置7との連
動作動により保持される。このとき燃焼炉18には外気
の混入はなく、温度設定された状態はメッシュ状籠形の
火格子3の隙間を通して古タイヤ15に達し燃焼熱分解
される。古タイヤ15の熱分解により発生した熱分解ガ
スは、煙道13及び16を経てガスバーナー10に達し
火炎となる。 火炎温度は950〜1200℃に達する
ので、熱分解に必要な輻射熱としては600〜800℃
を十分満たせるものであり、補助燃料供給装置7からの
燃料供給は、通常燃焼開始後約30分と熱分解完了前約
30分だけ必要である。
Next, a method for producing a carbide according to the present invention will be described with reference to FIG. When the flue 13 is moved in the directions of arrows A and B by engaging an external crane or the like (not shown) with the hook 5, the joint 6 becomes the suction side flue 1 of the fan 17.
6 is disengaged from the radiant can 2 because the radiant can lid 4 moves together with the flue 13 because the radiant can lid 4 can move in any of the directions of the arrows C to D and EF. Then, the radiation can 2 opens. For example, old tires 15 are put into the opened radiation can 2 as industrial waste, and the radiation can lid 4 is closed. Next, the gas burner 10 is ignited, and the gap between the outer furnace 1 and the radiant can 2 is heated to 600 to 800 ° C. This set temperature is maintained by the interlocking operation of the temperature sensor 9 in the outer furnace 1 and the auxiliary fuel supply device 7. At this time, no outside air is mixed into the combustion furnace 18, and the temperature set state reaches the old tires 15 through the gaps of the mesh-shaped grate 3 and is burned and decomposed. The pyrolysis gas generated by the pyrolysis of the old tire 15 reaches the gas burner 10 via the flue 13 and 16 and becomes a flame. Since the flame temperature reaches 950 to 1200 ° C, the radiant heat required for thermal decomposition is 600 to 800 ° C.
Is sufficient, and the fuel supply from the auxiliary fuel supply device 7 usually requires only about 30 minutes after the start of combustion and about 30 minutes before the completion of thermal decomposition.

【0009】輻射熱により輻射缶2内が300〜500
℃に達したとき、輻射缶2内の温度センサー8と噴霧ノ
ズル11が連動作動し、噴霧ノズル11から水蒸気が輻
射缶2内に噴霧され、水蒸気の吸熱反応で輻射缶2内の
温度の異常上昇を防ぎ設定温度に保持される。輻射熱と
して利用後の熱分解ガスエネルギー及び排気は、外炉1
上部に設けられた排気管12により下流の熱交換器(図
示省略)に送られ、熱利用される。
Due to the radiant heat, the inside of the radiant can 2 is 300 to 500.
When the temperature reaches 0 ° C., the temperature sensor 8 in the radiation can 2 and the spray nozzle 11 operate in conjunction with each other, and steam is sprayed from the spray nozzle 11 into the radiation can 2, and the temperature in the radiation can 2 is abnormal due to an endothermic reaction of the steam. The rise is prevented and it is kept at the set temperature. The pyrolysis gas energy and exhaust gas used as radiant heat are supplied to the outer furnace 1
The gas is sent to a downstream heat exchanger (not shown) by an exhaust pipe 12 provided at an upper portion, and is used for heat.

【0010】古タイヤ15の燃焼完了後輻射缶蓋4を開
きメッシュ状籠形の火格子3に外部のクレーン等(図示
省略)を係合して取出し、得られた古タイヤ15よりの
炭化物及び残存したワイヤー等を他の容器に移し後工程
の活性炭製造装置に投入される。本実施例の得られた炭
化物は、通電性は10Ω/10cm以下で、比重0.
55g/ml以下であって、十分炭化され、非炭素生成
分又は組織の壊れた炭素の含有が抑えられ、炭素細孔が
良好に保持されている。本実施例の噴霧ノズル11に水
蒸気に代えて不活性ガス(例えば窒素ガス又は炭酸ガ
ス)又は不活性ガスと水蒸気の混合ガスを噴射しても本
実施例と同様の好品質の炭化物が得られる。
After the burning of the old tire 15 is completed, the radiant can lid 4 is opened, and an external crane or the like (not shown) is engaged with the mesh-shaped grate 3 and taken out. The remaining wires and the like are transferred to another container and then charged into an activated carbon manufacturing device in a subsequent process. The carbide obtained in this example has an electrical conductivity of 10Ω / 10 cm 2 or less and a specific gravity of 0.1.
The content is 55 g / ml or less, the carbonization is sufficient, the content of non-carbon-producing components or broken carbon in the structure is suppressed, and the carbon pores are well retained. Even if an inert gas (for example, nitrogen gas or carbon dioxide gas) or a mixed gas of an inert gas and water vapor is injected into the spray nozzle 11 of this embodiment instead of water vapor, the same high-quality carbide as in this embodiment can be obtained. .

【0011】[0011]

【発明の効果】本発明によれば、産業廃棄物を燃焼させ
活性炭の原料として使用される炭化物の製造にあたり、
燃焼炉において、燃焼ガス中のNOx、SOxの発生を
極力抑えることができ、燃焼温度を低く保ちながら、十
分炭化され、非炭素生成分の含有が抑えられた高品位な
炭化物が効率良く得られる。特に各種プラスチック類、
各種ゴム類等の産業廃棄物からの炭化物の製造により、
産業廃棄物のリサイクルに大きく貢献することができ
る。
According to the present invention, in the production of carbide used as a raw material of activated carbon by burning industrial waste,
In the combustion furnace, the generation of NOx and SOx in the combustion gas can be suppressed as much as possible, and while maintaining the combustion temperature low, high-quality carbides that are sufficiently carbonized and contain less non-carbon generation components can be obtained efficiently. . Especially various plastics,
By producing carbides from industrial waste such as various rubbers,
It can greatly contribute to the recycling of industrial waste.

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

【図1】図1は、本発明の炭化物の製造装置の一実施例
の断面正面略図である。
FIG. 1 is a schematic cross-sectional front view of one embodiment of a carbide producing apparatus according to the present invention.

【符号の説明】[Explanation of symbols]

1 外炉 2 輻射缶 3 火格子 4 輻射缶蓋 5 フック 6 ジョイント 7 補助燃料供給装置 8、9 温度センサー 10 ガスバーナー 11 噴射ノズル 12 排気管 13、16 煙道 14 台座 15 古タイヤ 17 フアン 18 燃焼炉 Reference Signs List 1 outer furnace 2 radiant can 3 grate 4 radiant can lid 5 hook 6 joint 7 auxiliary fuel supply device 8, 9 temperature sensor 10 gas burner 11 injection nozzle 12 exhaust pipe 13, 16 flue 14 pedestal 15 old tire 17 fan 18 combustion Furnace

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI F23G 5/50 ZAB B09B 3/00 ZAB F23L 7/00 ZAB 302F ──────────────────────────────────────────────────の Continuation of front page (51) Int.Cl. 6 Identification code FI F23G 5/50 ZAB B09B 3/00 ZAB F23L 7/00 ZAB 302F

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 燃焼炉内において外気遮断下で水蒸気を
噴霧しつつ産業廃棄物を燃焼させるようにした炭化物の
製造方法において、燃焼炉を外側外炉と内側輻射缶の二
重構造とし前記外炉と前記輻射缶との間隙に向けて燃料
を噴射着火し前記輻射缶内に向けて水蒸気を噴霧しつつ
前記輻射缶内に収納された産業廃棄物を輻射熱により燃
焼させることを特徴とする炭化物の製造方法。
1. A method for burning industrial waste while spraying steam in a combustion furnace while shutting off outside air .
In the manufacturing method, the combustion furnace is divided into an outer outer furnace and an inner radiant can.
Fuel to the gap between the outer furnace and the radiant can
While igniting and spraying water vapor into the radiant can
The industrial waste stored in the radiant can is burned by radiant heat.
A method for producing a carbide, characterized by firing .
【請求項2】 燃焼炉内において外気遮断下で不活性ガ
ス又は不活性ガスと水蒸気の混合ガスを噴霧しつつ産業
廃棄物を燃焼させるようにした炭化物の製造方法におい
て、燃焼炉を外側外炉と内側輻射缶の二重構造とし前記
外炉と前記輻射缶との間隙に向けて燃料を噴射着火し前
記輻射缶内に向けて不活性ガス又は不活性ガスと水蒸気
の混合ガスを噴霧しつつ前記輻射缶内に収納された産業
廃棄物を輻射熱により燃焼させることを特徴とする炭化
物の製造方法。
2. An inert gas in a combustion furnace under the cutoff of outside air.
Industry while spraying mixed gas of water or inert gas and steam
In the method for producing a carbide in which waste is burned , the combustion furnace has a double structure of an outer outer furnace and an inner radiant can, and fuel is injected and ignited toward a gap between the outer furnace and the radiant can to radiate the radiant can. Inert gas or inert gas and water vapor
A method for producing a carbide, characterized in that industrial waste stored in the radiant can is burned by radiant heat while spraying the mixed gas .
【請求項3】 燃焼炉の外側の円筒状外炉内側に円筒状
輻射缶が固着され、前記輻射缶の上端に着脱可能な蓋が
嵌着され、前記外炉下部外側より前記外炉と前記輻射缶
との間隙に向けて設けたガスバーナーと、前記外炉底面
外側より前記外炉及び前記輻射缶を貫通し前記輻射缶内
に向けて設けた噴霧ノズルと、前記輻射缶の上面部と前
記ガスバーナー吸込み側に連通する煙道と、前記外炉外
側に設けた排気管と、前記ガスバーナーと連動可能に設
けた前記外炉内及び前記輻射缶内に突出する温度センサ
ーと、前記噴霧ノズルと連動可能に設けた前記輻射缶内
に突出する温度センサーとよりなることを特徴とする炭
化物の製造装置。
3. A cylindrical radiant can is fixed to the inside of a cylindrical outer furnace outside the combustion furnace, and a detachable lid is fitted to an upper end of the radiant can. A gas burner provided toward the gap with the radiant can, a spray nozzle penetrating the outer furnace and the radiant can from the outside of the outer furnace bottom surface toward the inside of the radiant can, and an upper surface portion of the radiant can A flue communicating with the gas burner suction side, an exhaust pipe provided outside the outer furnace, a temperature sensor protruding into the outer furnace and the radiant can provided in cooperation with the gas burner, and An apparatus for producing carbide, comprising: a temperature sensor protruding into the radiant can provided so as to be interlocked with a nozzle.
【請求項4】 請求項3に記載の炭化物の製造装置にお
いて、輻射缶内下底に設けた台座と、前記台座上に載置
した籠形の火格子と、前記台座と前記火格子の間隙に向
けて設けた噴霧ノズルとよりなることを特徴とする炭化
物の製造装置。
4. The carbide manufacturing apparatus according to claim 3 , wherein a pedestal provided at a lower bottom in the radiant can, a basket-shaped grate placed on the pedestal, and a gap between the pedestal and the grate. An apparatus for producing carbide, comprising: a spray nozzle provided toward a surface.
JP6103499A 1994-04-06 1994-04-06 Method for producing carbide and production apparatus used for same Expired - Fee Related JP2876455B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6103499A JP2876455B2 (en) 1994-04-06 1994-04-06 Method for producing carbide and production apparatus used for same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6103499A JP2876455B2 (en) 1994-04-06 1994-04-06 Method for producing carbide and production apparatus used for same

Publications (2)

Publication Number Publication Date
JPH07280226A JPH07280226A (en) 1995-10-27
JP2876455B2 true JP2876455B2 (en) 1999-03-31

Family

ID=14355685

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6103499A Expired - Fee Related JP2876455B2 (en) 1994-04-06 1994-04-06 Method for producing carbide and production apparatus used for same

Country Status (1)

Country Link
JP (1) JP2876455B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3885905B2 (en) * 1997-06-05 2007-02-28 古河機械金属株式会社 Electric double layer capacitor
JP3409204B2 (en) * 1997-09-09 2003-05-26 日立造船株式会社 Processing method of waste rubber metal composite
JP2009012984A (en) * 2007-06-29 2009-01-22 Ihi Corp Method and apparatus for manufacturing functional material in power generating installation

Also Published As

Publication number Publication date
JPH07280226A (en) 1995-10-27

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