JPH09208962A - Apparatus for dry-distillation treatment of industrial waste - Google Patents
Apparatus for dry-distillation treatment of industrial wasteInfo
- Publication number
- JPH09208962A JPH09208962A JP2157096A JP2157096A JPH09208962A JP H09208962 A JPH09208962 A JP H09208962A JP 2157096 A JP2157096 A JP 2157096A JP 2157096 A JP2157096 A JP 2157096A JP H09208962 A JPH09208962 A JP H09208962A
- Authority
- JP
- Japan
- Prior art keywords
- waste
- pipe
- dry distillation
- wall body
- air
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/78—Recycling of wood or furniture waste
Landscapes
- Processing Of Solid Wastes (AREA)
- Coke Industry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、廃タイヤ,プラス
チック等の合成樹脂,フィルム材,木片,包装紙材,紐
類,故紙,接着剤或いはリサイクル不能な廃材等の産業
廃棄物を乾留(燃焼)処理し、且つその乾留(燃焼)に
より生じたガスの熱エネルギーを有効に使用すことがで
きる産業廃棄物の乾留処理装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention dry-distills (combusts) industrial waste such as waste tires, synthetic resins such as plastics, film materials, wood chips, wrapping paper materials, strings, waste paper, adhesives, or non-recyclable waste materials. ) The present invention relates to a dry distillation treatment apparatus for industrial waste, which is capable of treating and effectively using thermal energy of gas generated by the dry distillation (combustion).
【0002】[0002]
【従来の技術】従来より廃タイヤ等の産業廃棄物を自燃
させて、そのときの燃焼により発生するガスを熱エネル
ギーとして再度利用する乾留炉が存在している。図13
は従来タイプの乾留炉であるが、これによると炉室20
の中に廃タイヤ等の廃棄物を入れ、蓋23を密封状に閉
じ、その廃タイヤ等の廃棄物をバーナー21にて強制或
いは自燃させて乾留(燃焼)処理する。そして、その廃
棄物の燃焼によるガスを排出口22からボイラー等に送
り込む。2. Description of the Related Art Conventionally, there is a dry distillation furnace in which industrial waste such as waste tires is self-combusted and the gas generated by combustion at that time is reused as thermal energy. FIG.
Is a conventional type carbonization furnace.
Waste such as a waste tire is put in the container, the lid 23 is hermetically closed, and the waste such as the waste tire is forcibly or self-combusted by the burner 21 for dry distillation (combustion) treatment. Then, the gas resulting from the combustion of the waste is sent from the exhaust port 22 to the boiler or the like.
【0003】[0003]
【発明が解決しようとする課題】従来タイプの乾留炉で
は、乾留炉室内において廃タイヤ等の廃棄物を乾留処理
するときに、炉室内に入れた廃棄物が一度に燃焼するこ
ととなり、その燃焼中において蓋を開けることが出来な
くなる。そのために、図13に示すように稼動中の炉室
20の蓋23を開けると強烈なる炎が広範囲に及ぶた
め、その周囲は極めて危険である。そのために稼動中の
炉室20の蓋23を開けて、次々に廃棄物を投入する作
業は、作業員にとって炉室20内の廃棄物からの燃焼に
よる炎を浴びる危険性があった。In the conventional type carbonization furnace, when the waste such as waste tires is carbonized in the carbonization furnace chamber, the wastes put in the furnace chamber are burned at once, and the combustion It becomes impossible to open the lid inside. Therefore, when the lid 23 of the furnace chamber 20 in operation is opened as shown in FIG. 13, an intense flame spreads over a wide area, and the surrounding area is extremely dangerous. For this reason, the work of opening the lid 23 of the furnace chamber 20 in operation and successively throwing in the waste has a risk that the worker is exposed to a flame due to combustion from the waste in the furnace chamber 20.
【0004】それゆえに、炉室20内の廃棄物の燃焼が
完了するまでは、炉室20の蓋23を開けて次の新たな
廃棄物を投入してゆくことができないという不都合があ
り、廃棄物の処理作業は大幅に遅れることとなる。ま
た、炉室内における廃棄物は、下層の部分より次第に上
層の部分の廃棄物に燃焼が移動してゆくこととなるが、
実際には廃棄物の燃焼が完全に行われないことが多く、
廃棄物の乾留(燃焼)処理作業の効率が低下し、ひいて
は廃棄物の乾留(燃焼)処理により発生するガスの熱エ
ネルギーの再利用も極めて効率の悪いものとなることが
多かった。Therefore, until the combustion of the waste in the furnace chamber 20 is completed, there is the inconvenience that the lid 23 of the furnace chamber 20 cannot be opened and the next new waste cannot be thrown in. The processing of goods will be significantly delayed. In addition, the combustion of the waste in the furnace chamber gradually moves to the waste in the upper layer from the lower layer,
In many cases waste is not completely burned in practice,
The efficiency of the dry distillation (combustion) treatment work of the waste was reduced, and the reuse of the thermal energy of the gas generated by the dry distillation (combustion) treatment of the waste was often extremely inefficient.
【0005】[0005]
【課題を解決するための手段】そこで、発明者は上記課
題を解決するために、鋭意,研究を重ねた結果、本発明
を筒状壁体の下部に底体を設け、前記筒状壁体の下部付
近のみに複数の送風流入孔を設け、前記筒状壁体の上端
に開閉可能な蓋体を設けて密閉可能な廃棄物貯蔵炉と、
該廃棄物貯蔵炉の下部付近周囲を適宜の間隔をおいて被
覆して前記送風流入孔に空気を送り込む空気送風室と、
管部の下端を前記底板上面に固着し、前記管部の上端は
前記筒状壁体の上部側より外部に連通させ、前記管部の
下部寄りに複数のガス流入孔を設けた乾留ガス外部供給
管とからなり、前記筒状壁体,底体及び管部には冷却水
を循環可能に構成してなる産業廃棄物の乾留処理装置と
したことにより、産業廃棄物の乾留処理をより効率的な
ものとし、且つ炉内において下層側の廃棄物のみが燃焼
し、上層側の産業廃棄物は不燃状態とし、稼動中におい
ても新たに廃棄物を安全に投入してゆくことができ、上
記課題を解決したものである。In order to solve the above-mentioned problems, the inventors of the present invention have made earnest studies, and as a result, according to the present invention, a bottom body is provided in the lower portion of the tubular wall body, and the above-mentioned tubular wall body is provided. A plurality of blower inflow holes only near the lower part of the, and a waste storage furnace that can be closed by providing an openable lid at the upper end of the tubular wall body;
An air blower chamber for covering the periphery of the lower part of the waste storage furnace at an appropriate interval and sending air to the blower inlet.
The lower end of the pipe portion is fixed to the upper surface of the bottom plate, the upper end of the pipe portion communicates with the outside from the upper side of the tubular wall body, and the dry distillation gas externally provided with a plurality of gas inflow holes near the lower portion of the pipe portion. A dry distillation treatment device for industrial waste, which is composed of a supply pipe, and in which the cooling water can be circulated in the cylindrical wall body, the bottom body and the pipe portion, makes the dry distillation treatment of industrial waste more efficient. In addition, only the lower-layer waste is burned in the furnace, the upper-layer industrial waste is in a non-combustible state, and new waste can be safely input even during operation. It is a solution to the problem.
【0006】[0006]
【発明の実施の形態】以下、本発明の実施形態を図面に
基づいて説明する。まず、主に廃棄物貯蔵炉A,空気送
風室B及び乾留ガス外部供給管Cから構成されている。
本発明の第1実施形態については、その廃棄物貯蔵炉A
は、図1乃至図3等に示すように、筒状壁体1と底体2
とから円筒形状に構成されている。その筒状壁体1は、
二重構造となっており、内壁部1aと外壁部1bとを適
宜の間隔をおいて構成したものである。また、底体2も
前記筒状壁体1と同様に二重構造であり、図1,図3に
示すように、上面底部2aと下面底部2bとから構成さ
れている。Embodiments of the present invention will be described below with reference to the drawings. First, it mainly comprises a waste storage furnace A, an air blowing chamber B, and a dry distillation gas external supply pipe C.
Regarding the first embodiment of the present invention, the waste storage furnace A
Is a cylindrical wall body 1 and a bottom body 2 as shown in FIGS.
It has a cylindrical shape. The cylindrical wall 1 is
It has a double structure in which the inner wall portion 1a and the outer wall portion 1b are formed with an appropriate interval. The bottom body 2 also has a double structure similar to the tubular wall body 1, and is composed of an upper surface bottom portion 2a and a lower surface bottom portion 2b, as shown in FIGS.
【0007】その筒状壁体1及び底体2は、図1に示す
ように、冷却水Wを循環可能に貯蔵しており、廃棄物貯
蔵炉Aの外部に設置した冷却水循環部13を介して筒状
壁体1及び底体2内を冷却水Wが循環するものである。
その冷却水循環部13は循環管路13aと冷却水タンク
13bから構成されており、その循環管路13aが廃棄
物貯蔵炉Aの下部より上部に向かって連結しており、廃
棄物貯蔵炉Aの下部側にて高温になった冷却水Wが筒状
壁体1の上部側に移動し、循環管路13aを通過して再
度廃棄物貯蔵炉Aの下部に移動するもので、このよう
な、冷却水Wの循環は熱対流として自然に行われる。冷
却水Wの補給は、冷却水タンク13bから行う。また、
冷却水タンク13bにはポンプ等を装着し、強制的に冷
却水Wを循環させてもよい。As shown in FIG. 1, the cylindrical wall body 1 and the bottom body 2 store cooling water W in a circulatory manner, and through a cooling water circulating portion 13 installed outside the waste storage furnace A. The cooling water W circulates in the cylindrical wall body 1 and the bottom body 2.
The cooling water circulation unit 13 is composed of a circulation pipe line 13a and a cooling water tank 13b, and the circulation pipe line 13a is connected from the lower part of the waste storage furnace A toward the upper part of the waste storage furnace A. Cooling water W that has become hot on the lower side moves to the upper side of the tubular wall body 1, passes through the circulation pipe 13a, and moves again to the lower part of the waste storage furnace A. The cooling water W is naturally circulated as heat convection. The cooling water W is supplied from the cooling water tank 13b. Also,
A pump or the like may be attached to the cooling water tank 13b to forcibly circulate the cooling water W.
【0008】その廃棄物貯蔵炉Aの筒状壁体1の下部側
と底体2には複数の送風流入孔3,3,…が形成されて
いる。該送風流入孔3は、具体的には、図3に示すよう
に、筒状壁体1の内壁部1aと外壁部1bとの間に送風
パイプ3aが水密状態に設けられたものである。さら
に、底体2においても、前記筒状壁体1と同様に送風パ
イプ3aが上面底部2aと下面底部2bとの間に水密状
態に設けられたものである。筒状壁体1及び底体2の内
部の冷却水Wは、送風パイプ3a,3a,の間を通り抜
けて流れるものであり、筒状壁体1及び底体2の外部に
洩れないようになっている。In the waste storage furnace A, a plurality of blast inflow holes 3, 3, ... Are formed in the bottom side of the cylindrical wall 1 and the bottom 2. Specifically, as shown in FIG. 3, the blower inflow hole 3 is formed by providing a blower pipe 3a in a watertight state between the inner wall portion 1a and the outer wall portion 1b of the tubular wall body 1. Further, also in the bottom body 2, the blower pipe 3a is provided in a watertight state between the upper surface bottom portion 2a and the lower surface bottom portion 2b similarly to the cylindrical wall body 1. The cooling water W inside the cylindrical wall body 1 and the bottom body 2 flows through between the blower pipes 3a, 3a, and is prevented from leaking to the outside of the cylindrical wall body 1 and the bottom body 2. ing.
【0009】その廃棄物貯蔵炉Aの筒状壁体1の下部周
囲で、且つ前記送風流入孔3,3,…の形成箇所には、
図1乃至図3等に示すように、空気送風室Bが設けられ
ている。即ち、空気送風室Bは、廃棄物貯蔵炉Aの送風
流入孔3,3,…部分を外部から囲むようにして設けら
れものである。さらに具体的には、その空気送風室B
は、空気室壁5及び空気送風口部6から構成され、その
空気室壁5が廃棄物貯蔵炉Aの筒状壁体1下部周囲及び
底体2を密閉状態に被覆しており、廃棄物貯蔵炉Aと空
気室壁5との間に室内空間5aが構成される〔図1,図
2(A),図3等参照〕。In the periphery of the lower portion of the cylindrical wall 1 of the waste storage furnace A, and at the locations where the blower inflow holes 3, 3, ... Are formed,
As shown in FIGS. 1 to 3 and the like, an air blowing chamber B is provided. That is, the air blower chamber B is provided so as to surround the blower inlet holes 3, 3, ... Of the waste storage furnace A from the outside. More specifically, the air blowing chamber B
Is composed of an air chamber wall 5 and an air blowing port 6, and the air chamber wall 5 covers the lower part of the cylindrical wall body 1 and the bottom body 2 of the waste storage furnace A in a sealed state. An indoor space 5a is formed between the storage furnace A and the air chamber wall 5 [see FIGS. 1, 2 (A), 3 and the like].
【0010】そして、その空気送風室Bの空気送風口部
6から室内空間5aに乾留(燃焼)処理に必要な空気a
を送り込み、さらに室内空間5a内の空気aを前記送風
流入孔3,3,…を介して廃棄物貯蔵炉A内に送り込む
ものである(図5参照)。また、廃棄物貯蔵炉Aの下部
の底体2側寄りにはバーナー12が装着され(図1参
照)、廃棄物の燃焼を強制開始させる(図7参照)。Then, the air a necessary for the dry distillation (combustion) process from the air blowing port 6 of the air blowing chamber B to the indoor space 5a.
, And further, the air a in the indoor space 5a is sent into the waste storage furnace A through the air blowing inlets 3, 3, ... (See FIG. 5). Further, a burner 12 is attached to the bottom of the waste storage furnace A near the bottom body 2 (see FIG. 1) to compulsorily start the combustion of the waste (see FIG. 7).
【0011】次に、乾留ガス外部供給管Cは、底体2の
略中央箇所箇所から筒状壁体1の上方箇所にスロート1
0を介して連通しているものである〔図1,図2
(A),(B)及び図4(A)等参照〕。この乾留ガス
外部供給管Cは、廃棄物貯蔵炉A内の廃棄物を乾留(燃
焼)処理したときに発生する乾留ガスGを熱エネルギー
として廃棄物貯蔵炉Aの外部に送り出す役目をなすもの
である。その乾留ガス外部供給管Cは、管部7とガス流
入孔8,8,…から構成されたものであり、さらに、そ
の管部7は、外管部7a及び内管部7bとから構成され
ている。その外管部7aと内管部7bとの間には、前記
筒状壁体1或いは底体2と同様に内部に冷却水Wが循環
可能に貯蔵される構造となっている。Next, the dry distillation gas external supply pipe C extends from the central portion of the bottom body 2 to the upper portion of the cylindrical wall body 1 by the throat 1.
0 through [0] [Fig. 1, Fig. 2
(A), (B) and FIG. 4 (A) etc.]. The dry distillation gas external supply pipe C serves to send out the dry distillation gas G generated when the waste in the waste storage furnace A is dry-distilled (combusted) to the outside of the waste storage furnace A as thermal energy. is there. The dry distillation gas external supply pipe C is composed of a pipe portion 7 and gas inflow holes 8, 8, ... And the pipe portion 7 is composed of an outer pipe portion 7a and an inner pipe portion 7b. ing. Between the outer pipe portion 7a and the inner pipe portion 7b, cooling water W is circulated and stored in the inside similarly to the cylindrical wall body 1 or the bottom body 2.
【0012】この場合に、管部7は筒状壁体1とは冷却
水連通管11を介して連通され、また管部7の下部は底
体2と直接連通し、前記冷却水連通管11とともに冷却
水Wが筒状壁体1,底体2及び管部7内を自由に対流す
ることができるようになっている(図1参照)。また、
ガス流入孔8は、前記送風流入孔3の送風パイプ3aの
構造と略同様にガス流入パイプ8aが外管部7aと内管
部7bとの間に水密状態に装着されたものである〔図4
(B)参照〕。In this case, the pipe portion 7 is communicated with the cylindrical wall body 1 through the cooling water communication pipe 11, and the lower portion of the pipe portion 7 is directly communicated with the bottom body 2, so that the cooling water communication pipe 11 is provided. At the same time, the cooling water W can freely convect inside the tubular wall body 1, the bottom body 2 and the pipe portion 7 (see FIG. 1). Also,
The gas inflow hole 8 is formed by mounting the gas inflow pipe 8a between the outer pipe portion 7a and the inner pipe portion 7b in a watertight manner in substantially the same manner as the structure of the air blow pipe 3a of the air blow inlet hole 3 [Fig. Four
(B)].
【0013】その乾留ガス外部供給管Cの管部7の上部
端は筒状壁体1の上部箇所よりスロート10を介して廃
棄物貯蔵炉Aの外部に廃棄物が燃焼して発生する乾留ガ
スGを排出する構造となっている。そのスロート10
は、円筒形状をなし、その内径は管部7の外形よりも大
きくなっている。それゆえに、スロート10内周面と管
部7の外周面との間に隙間が存在し、その隙間からも廃
棄物貯蔵炉A内の廃棄物の乾留(燃焼)処理により発生
した乾留ガスGを廃棄物貯蔵炉Aの外部に送りだすこと
ができる構造となっている。また、乾留ガス外部供給管
Cは、スロート10を使用しないで、管部7先端を廃棄
物貯蔵炉Aの筒状壁体1に直接貫通させる構造も存在す
る〔図12(A)参照〕。The upper end of the tube portion 7 of the dry distillation gas external supply pipe C is a dry distillation gas generated by burning the waste from the upper portion of the tubular wall 1 through the throat 10 to the outside of the waste storage furnace A. It has a structure for discharging G. That throat 10
Has a cylindrical shape, and its inner diameter is larger than the outer shape of the tube portion 7. Therefore, there is a gap between the inner peripheral surface of the throat 10 and the outer peripheral surface of the pipe portion 7, and the dry distillation gas G generated by the dry distillation (combustion) treatment of the waste in the waste storage furnace A is also generated from the clearance. The structure is such that it can be sent out of the waste storage furnace A. The dry distillation gas external supply pipe C also has a structure in which the tip of the pipe portion 7 is directly passed through the cylindrical wall body 1 of the waste storage furnace A without using the throat 10 (see FIG. 12 (A)).
【0014】その乾留ガス外部供給管Cの管部7の下部
周囲には補助管部9,9,…が放射状に配置されるタイ
プが存在する〔図9(A)及び(C)参照〕。このタイ
プでは、補助管部9の下面側に複数のガス流入孔8,
8,…が設けられている〔図9(B)及び図10参
照〕。そして、乾留ガス外部供給管Cは、管部7ととも
に補助管部9,9,…にても廃棄物の乾留(燃焼)処理
から生ずる乾留ガスGを吸入することができる(図10
参照)。There is a type in which auxiliary pipe portions 9, 9, ... Are radially arranged around the lower portion of the pipe portion 7 of the dry distillation gas external supply pipe C (see FIGS. 9A and 9C). In this type, a plurality of gas inlet holes 8 are formed on the lower surface side of the auxiliary pipe portion 9,
Are provided [see FIG. 9 (B) and FIG. 10]. Further, the dry distillation gas external supply pipe C can suck the dry distillation gas G generated from the dry distillation (combustion) process of the waste into the auxiliary pipe portions 9, 9, ... Together with the pipe portion 7 (FIG. 10).
reference).
【0015】その補助管部9も冷却水Wが循環可能なよ
うに二重構造としたものであり、図10及び図11
(A),(B)に示すように、補助管部外殻9a及び補
助管部内殻9b、より構成され、両補助管部外殻9a及
び補助管部内殻9bの間に冷却水Wが循環可能に貯蔵さ
れる。また、補助管部9,9の頂部箇所の断面形状は略
三角形状〔図11(A)参照〕,或いは逆U字形状〔図
11(B)参照〕等の形状としたものが存在する。この
ように補助管部9の頂部を三角形状或いは逆U字形状等
とすることで、廃棄物を投入したときに、補助管部9の
頂部に廃棄物が引っ掛かりにくくすることができる。ま
た、補助管部9の断面形状は図示しないが、管部7と同
様に円形状のタイプも存在し、このタイプの補助管部9
も下面側に複数のガス流入孔8,8,…が設けられてい
る。The auxiliary pipe portion 9 also has a double structure so that the cooling water W can be circulated.
As shown in (A) and (B), it is composed of an outer shell 9a and an inner shell 9b of the auxiliary pipe, and the cooling water W circulates between the outer shell 9a of the auxiliary pipe and the inner shell 9b of the auxiliary pipe. Stored as possible. In addition, the cross-sectional shape of the top portions of the auxiliary pipe portions 9 and 9 may be a substantially triangular shape (see FIG. 11A) or an inverted U-shape (see FIG. 11B). By thus forming the top portion of the auxiliary pipe portion 9 into a triangular shape or an inverted U shape, it is possible to prevent the waste material from being caught on the top portion of the auxiliary pipe portion 9 when the waste material is input. Further, although the sectional shape of the auxiliary pipe portion 9 is not shown, there is also a circular type similar to the pipe portion 7, and the auxiliary pipe portion 9 of this type is present.
, A plurality of gas inflow holes 8, 8, ... Are provided on the lower surface side.
【0016】次に、本発明の第2実施形態では、図12
(A)に示すように、廃棄物貯蔵炉Aの筒状壁体1の下
部のみに複数の送風流入孔3,3,…を設け、底体2に
は送風流入孔3,3,…を設けないもので、乾留ガス外
部供給管Cは第1実施形態と同様である。また、本発明
の第3実施形態では、図12(B)示すように、廃棄物
貯蔵炉Aの底体2のみに複数の送風流入孔3,3,…を
設け、筒状壁体1の下部には送風流入孔3,3,…を設
けないもので、乾留ガス外部供給管Cは第1実施形態と
同様である。Next, in the second embodiment of the present invention, FIG.
As shown in (A), a plurality of blast inlet holes 3, 3, ... Are provided only in the lower portion of the cylindrical wall body 1 of the waste storage furnace A, and the bottom body 2 is provided with blast inlet holes 3, 3 ,. The dry distillation gas external supply pipe C, which is not provided, is the same as in the first embodiment. In addition, in the third embodiment of the present invention, as shown in FIG. 12 (B), only the bottom body 2 of the waste storage furnace A is provided with a plurality of air flow inlet holes 3, 3, ... The blower inflow holes 3, 3, ... Are not provided in the lower part, and the dry distillation gas external supply pipe C is the same as in the first embodiment.
【0017】[0017]
【作用】まず、廃棄物貯蔵炉Aの蓋体4を開けて廃タイ
ヤ(その他の廃棄物としてはプラスチック等の合成樹
脂,フィルム材,木片,包装紙材,紐類,故紙,接着剤
或いはリサイクル不能な廃材等も含まれる)等の廃棄物
を入れる〔図6(A)参照〕。そして、蓋体4を密封状
に閉じ、バーナー12により廃棄物を強制燃焼させると
ともに、空気送風室Bの空気送風口部6より空気aを送
り込み、該空気aは送風流入孔3,3,…を介して廃棄
物貯蔵炉A内に入り込み底体2の付近の下層部分の廃棄
物のみの乾留(燃焼)処理を促進させる〔図6(B)参
照〕。First, the lid 4 of the waste storage furnace A is opened to dispose of waste tires (as other wastes, synthetic resins such as plastics, film materials, wood chips, wrapping paper materials, cords, waste paper, adhesives or recycling). Waste such as unusable waste is also included [see FIG. 6 (A)]. Then, the lid 4 is closed hermetically, the burner 12 compulsorily combusts the waste, and the air a is sent from the air blower port portion 6 of the air blower chamber B, and the air a is blown into the air inlets 3, 3, ... Through the inside of the waste storage furnace A to accelerate the dry distillation (combustion) process of only the waste in the lower layer near the bottom body 2 (see FIG. 6B).
【0018】この廃棄物の乾留(燃焼)処理により発生
する乾留ガスGは乾留ガス外部供給管Cのガス流入孔
8,8,…より管内部7cに入り込み、乾留ガスGは管
内部7cに沿って廃棄物貯蔵炉Aの外部に送りだされる
(図7参照)。また、乾留ガス外部供給管Cに補助管部
9,9,…を設けたタイプでは、廃棄物の乾留(燃焼)
処理により発生した乾留ガスGを管部7のガス流入孔
8,8,…から吸入するとともに、補助管部9,9,…
側のガス流入孔8,8,…からも吸入し、乾留ガスGは
補助管内部9cを通過して管内部7cに流入し吸入効率
を上げることもある(図10参照)。The dry distillation gas G generated by the dry distillation (combustion) treatment of this waste enters the inside 7c of the pipe through the gas inlet holes 8, 8, ... Of the dry distillation gas external supply pipe C, and the dry distillation gas G follows the inside 7c of the pipe. And is sent out of the waste storage furnace A (see FIG. 7). Further, in the type in which the auxiliary pipe parts 9, 9, ... Are provided in the dry distillation gas external supply pipe C, the dry distillation (combustion) of waste is carried out.
The dry distillation gas G generated by the treatment is sucked from the gas inflow holes 8, 8, ... Of the pipe portion 7, and the auxiliary pipe portions 9, 9 ,.
, The dry distillation gas G may pass through the auxiliary pipe interior 9c and flow into the pipe interior 7c to improve the suction efficiency (see FIG. 10).
【0019】この廃棄物貯蔵炉A内の廃棄物の燃焼は、
筒状壁体1下部及び底体2に設けた送風流入孔3,3,
…により、貯蔵された廃棄物の下層側部分のみが燃焼す
ることとなる。これは、乾留ガス外部供給管Cの管部7
の下部箇所にガス流入孔8,8,…を設けているので、
廃棄物の燃焼から発生した乾留ガスGはガス流入孔8,
8,…に次々に送り込まれるため、その燃焼は貯蔵した
廃棄物の上層側に至らないものである。The combustion of the waste in the waste storage furnace A is
Blower inflow holes 3, 3, provided in the lower portion of the cylindrical wall body 1 and the bottom body 2.
... causes only the lower part of the stored waste to burn. This is the pipe portion 7 of the dry distillation gas external supply pipe C.
Since the gas inlet holes 8, 8, ... Are provided in the lower part of
The dry distillation gas G generated from the combustion of the waste gas is the gas inflow hole 8,
The combustion is not sent to the upper layer side of the stored waste because it is sent to 8, ...
【0020】そして、図6(B),図7に示すように、
廃棄物貯蔵炉A内に貯蔵された廃棄物においては、燃焼
エリアHb と不燃焼エリアHs の部分とが存在し、燃焼
エリアHb で廃棄物が乾留(燃焼)処理され、次々に乾
留ガスGとなるにしたがい、上部側の廃棄物が底体2側
に向かって移動し、燃焼エリアHb にたっした廃棄物の
みが乾留(燃焼)処理されてゆく〔図8(A)参照〕。Then, as shown in FIGS. 6 (B) and 7,
In the waste stored in the waste storage furnace A, there are a combustion area H b and a non-combustion area H s , and the waste is dry-distilled (combusted) in the combustion area H b , and then successively dry-distilled. As the gas becomes G, the waste on the upper side moves toward the bottom body 2 side, and only the waste accumulated in the combustion area H b is subjected to dry distillation (combustion) treatment (see FIG. 8 (A)). .
【0021】そして、不燃焼エリアHs では、廃棄物の
燃焼が行われていないために、蓋体4を開けても、廃棄
物貯蔵炉Aの開口部分には炎が存在せず、作業員は、新
たなる廃棄物を次々に廃棄物貯蔵炉A内に投入する作業
を行うことができる〔図8(B)参照〕。そして、乾留
ガス外部供給管Cを介して廃棄物貯蔵炉Aの外部に産業
廃棄物の乾留(燃焼)処理により発生した乾留ガスGを
送り出し、ボイラ14を稼動させるための熱エネルギー
とするものである(図1参照)。In the non-combustion area H s , since the waste is not burned, even if the lid 4 is opened, there is no flame in the opening of the waste storage furnace A, and the worker Can perform the operation of charging new waste one after another into the waste storage furnace A [see FIG. 8 (B)]. Then, the dry distillation gas G generated by the dry distillation (combustion) process of the industrial waste is sent to the outside of the waste storage furnace A through the dry distillation gas external supply pipe C, and is used as thermal energy for operating the boiler 14. Yes (see Figure 1).
【0022】[0022]
【発明の効果】請求項1の発明においては、筒状壁体1
の下部に底体2を設け、前記筒状壁体1の下部付近のみ
に複数の送風流入孔3,3,…を設け、前記筒状壁体1
の上端に開閉可能な蓋体4を設けて密閉可能な廃棄物貯
蔵炉Aと、該廃棄物貯蔵炉Aの下部付近周囲を適宜の間
隔をおいて被覆して前記送風流入孔3,3,…に空気を
送り込む空気送風室Bと、管部7の下端を前記底体2上
面に固着し、前記管部7の上端は前記筒状壁体1の上部
側より外部に連通させ、前記管部7の下部寄りに複数の
ガス流入孔8,8,…を設けた乾留ガス外部供給管Cと
からなり、前記筒状壁体1,底体2及び管部7には冷却
水Wを循環可能に構成してなる廃棄物の乾留処理装置と
したことにより、先ず第1に廃棄物の乾留処理の効率を
向上させることができるし、第2に作業員の安全性をよ
り一層確保することができる等の効果を奏する。According to the invention of claim 1, the cylindrical wall body 1 is provided.
, A bottom body 2 is provided in the lower part of the cylindrical wall body 1, and a plurality of air blowing inflow holes 3, 3, ... Are provided only near the lower part of the cylindrical wall body 1.
The waste storage furnace A which can be closed by providing a lid 4 which can be opened and closed at the upper end of the waste storage furnace A, and the periphery of the lower part of the waste storage furnace A which are covered at appropriate intervals by the blower inlets 3, 3, An air blowing chamber B for feeding air to the ... And a lower end of the pipe portion 7 is fixed to the upper surface of the bottom body 2, and an upper end of the pipe portion 7 is communicated with the outside from an upper side of the tubular wall body 1. A dry distillation gas external supply pipe C provided with a plurality of gas inflow holes 8, 8, ... Near the lower part of the portion 7, and the cooling water W is circulated through the cylindrical wall body 1, the bottom body 2 and the pipe portion 7. By adopting a dry distillation treatment apparatus for wastes configured as possible, firstly, the efficiency of dry distillation treatment of wastes can be improved, and secondly, the safety of workers can be further ensured. There is an effect such as being able to.
【0023】上記効果を詳述すると、廃棄物貯蔵炉A
は、下部付近のみに複数の送風流入孔3,3,…を設
け,且つ密閉可能としたものであり、廃棄物貯蔵炉Aの
下部周囲を空気送風室Bにて被覆し、前記複数の送風流
入孔3,3,…に空気aを送り込む構造としたものであ
る。そして、空気送風室Bから送り込んだ空気aは、送
風流入孔3,3,…より廃棄物貯蔵炉Aの下部にのみ入
り込むこととなり、廃棄物貯蔵炉A内においては、貯蔵
した廃棄物の下層側のみの乾留(燃焼)処理が促進され
る。The above effect will be described in detail. Waste storage furnace A
Are provided with a plurality of air blow-in holes 3, 3, ... Only near the lower part and can be hermetically sealed. The lower part of the waste storage furnace A is covered with an air blower chamber B, and the plurality of air blowers are provided. The structure is such that the air a is sent to the inflow holes 3, 3, .... Then, the air a sent from the air blowing chamber B enters only into the lower part of the waste storage furnace A through the air blowing inflow holes 3, 3, ..., In the waste storage furnace A, a lower layer of the stored waste is stored. The dry distillation (combustion) process only on the side is promoted.
【0024】さらに、乾留ガス外部供給管Cは管部7と
ガス流入孔8,8,…とからなり、管部7が底体2の略
中央箇所より筒状壁体1の上方を介して廃棄物貯蔵炉A
外部に連通したものであるため、廃棄物貯蔵炉A内の下
層側の廃棄物の燃焼から発生した乾留ガスGがガス流入
孔8,8,…から廃棄物貯蔵炉Aの外部に排出されるこ
ととなるので、廃棄物貯蔵炉A内に貯蔵した廃棄物は常
時下層側から燃焼し、上層部の廃棄物は不燃状態のまま
で、次第に底体2に向かって降下するものである。それ
ゆえに、廃棄物貯蔵炉Aの蓋体4を開けて、新たなる廃
棄物を次々に投入する作業を比較的簡単に行うことがで
き、且つその作業も、従来よりさらに安全性を確保する
ことができる。Further, the dry distillation gas external supply pipe C is composed of a pipe portion 7 and gas inflow holes 8, 8, ..., And the pipe portion 7 is provided above the cylindrical wall body 1 from a substantially central portion of the bottom body 2. Waste storage furnace A
Since it is communicated with the outside, the dry distillation gas G generated from the combustion of the lower-layer waste in the waste storage furnace A is discharged to the outside of the waste storage furnace A through the gas inflow holes 8, 8, .... Therefore, the waste stored in the waste storage furnace A always burns from the lower layer side, and the waste in the upper layer remains incombustible and gradually descends toward the bottom body 2. Therefore, it is possible to relatively easily perform the work of opening the lid 4 of the waste storage furnace A and introducing new waste one after another, and the work is also more secure than before. You can
【0025】次に、請求項2の発明は、請求項1におい
て、前記底体2には複数の送風流入孔3,3,…を設け
てなる廃棄物の乾留処理装置としたことより、前記筒状
壁体1の送風流入孔3,3,…とともに空気送風室Bか
ら空気aを多量に送り込むことができ、廃棄物の乾留
(燃焼)処理を一層促進し、発生する乾留ガスGの供給
効率を向上させることができる。Next, the invention of claim 2 provides the waste carbonization treatment device according to claim 1, wherein the bottom body 2 is provided with a plurality of air blowing inflow holes 3, 3 ,. A large amount of air a can be sent from the air blowing chamber B together with the air blow-in holes 3, 3, ... Of the cylindrical wall body 1, further promoting dry distillation (combustion) treatment of waste, and supply of dry distillation gas G generated. The efficiency can be improved.
【0026】次に、請求項3の発明は、請求項1又は2
において、前記管部7の下部付近の周囲に放射状に補助
管部9,9,…を設け、該補助管部9,9,…の下面側
に複数のガス流入孔8,8,…を設けてなる廃棄物の乾
留処理装置としたことにより、乾留ガス外部供給管Cに
おける、廃棄物貯蔵炉A内の廃棄物の乾留(燃焼)処理
により発生した乾留ガスGの吸入量を大きくすることが
できる。Next, the invention of claim 3 relates to claim 1 or 2.
In the above, the auxiliary pipe portions 9, 9, ... Are provided radially around the lower portion of the pipe portion 7, and a plurality of gas inflow holes 8, 8, ... Are provided on the lower surface side of the auxiliary pipe portions 9, 9 ,. By using the dry distillation treatment apparatus for wastes as described above, the suction amount of the dry distillation gas G generated by the dry distillation (combustion) treatment of the waste in the waste storage furnace A in the dry distillation gas external supply pipe C can be increased. it can.
【0027】次に、請求項4の発明は、請求項1又は2
において、前記乾留ガス外部供給管Cの管部7と筒状壁
体1との間には、管部7の外形より大なる内径を有する
スロート10を設けてなる廃棄物の乾留処理装置とした
ことにより、乾留ガス外部供給管Cの管部7の外周面と
スロート10の内周面との間に隙間を形成することがで
き、廃棄物の乾留(燃焼)処理により生ずる乾留ガスG
は乾留ガス外部供給管Cの管部7の下部に設けたガス流
入孔8,8,…だけからではなく、そのスロート10と
管部7との隙間からも廃棄物貯蔵炉A外部に送りだすこ
とができ、廃棄物内の乾留(燃焼)処理により発生した
乾留ガスGを無駄なく廃棄物貯蔵炉Aの外部に送りだす
ことができる。Next, the invention of claim 4 relates to claim 1 or 2.
In the dry distillation treatment apparatus for waste, a throat 10 having an inner diameter larger than the outer shape of the pipe portion 7 is provided between the pipe portion 7 of the dry distillation gas external supply pipe C and the tubular wall 1. As a result, a gap can be formed between the outer peripheral surface of the pipe portion 7 of the dry distillation gas external supply pipe C and the inner peripheral surface of the throat 10, and the dry distillation gas G generated by the dry distillation (combustion) treatment of the waste is performed.
Is sent to the outside of the waste storage furnace A not only from the gas inflow holes 8, 8 provided in the lower part of the tube portion 7 of the dry distillation gas external supply pipe C, but also from the gap between the throat 10 and the tube portion 7. Therefore, the dry distillation gas G generated by the dry distillation (combustion) process in the waste can be sent to the outside of the waste storage furnace A without waste.
【0028】次に、請求項5の発明は、筒状壁体1の下
部に底体2を設け、該底体2のみに複数の送風流入孔
3,3,…を設け、前記筒状壁体1の上端に開閉可能な
蓋体4を設けて密閉可能な廃棄物貯蔵炉Aと、該廃棄物
貯蔵炉Aの下部付近周囲を適宜の間隔をおいて被覆して
前記送風流入孔3,3,…に空気を送り込む空気送風室
Bと、管部7の下端を前記底体2上面に固着し、前記管
部7の上端は前記筒状壁体1の上部側より外部に連通さ
せ、前記管部7の下部寄りに複数のガス流入孔8,8,
…を設けた乾留ガス外部供給管Cとからなり、前記筒状
壁体1,底体2及び管部7には冷却水を循環可能に構成
してなる廃棄物の乾留処理装置としたことにより、特
に、底体2に直接接触する廃棄物の乾留(燃焼)処理を
良好に行うことができる。Next, in the invention of claim 5, the bottom body 2 is provided in the lower portion of the cylindrical wall body 1, and only the bottom body 2 is provided with a plurality of air flow inlet holes 3, 3 ,. A waste storage furnace A that can be closed by providing a lid 4 that can be opened and closed on the upper end of the body 1 and the periphery of the lower part of the waste storage furnace A are covered at appropriate intervals and the blower inlets 3, An air blower chamber B for sending air to 3, and a lower end of a pipe portion 7 are fixed to the upper surface of the bottom body 2, and an upper end of the pipe portion 7 is communicated with the outside from an upper side of the tubular wall body 1, A plurality of gas inflow holes 8, 8, near the lower part of the pipe portion 7,
By providing a dry distillation gas external supply pipe C provided with ..., And a dry distillation treatment apparatus for wastes in which the cooling water can be circulated through the cylindrical wall body 1, the bottom body 2 and the pipe portion 7. In particular, the dry distillation (combustion) treatment of the waste that comes into direct contact with the bottom body 2 can be favorably performed.
【0029】次に、請求項6の発明は請求項5におい
て、前記管部7の下部付近の周囲に放射状に補助管部
9,9,…を設け、該補助管部9,9,…の下面側に複
数のガス流入孔8,8,…を設けてなる乾留処理装置と
したことにより、より一層乾留ガスGの吸入効率を向上
させることができる。Next, according to the invention of claim 6, in claim 5, auxiliary pipe portions 9, 9, ... Are provided radially around the lower portion of the pipe portion 7, and the auxiliary pipe portions 9, 9 ,. By using the dry distillation treatment apparatus in which the plurality of gas inflow holes 8, 8, ... Are provided on the lower surface side, it is possible to further improve the suction efficiency of the dry distillation gas G.
【図1】本発明を含む一部断面とした構成図FIG. 1 is a partial cross-sectional configuration diagram including the present invention.
【図2】(A)は図1のX1 −X1 矢視断面略示図 (B)は図1のX2 −X2 矢視断面略示図2A is a schematic cross-sectional view taken along the line X 1 -X 1 of FIG. 1, and FIG. 2B is a schematic cross-sectional view taken along the line X 2 -X 2 of FIG.
【図3】本発明の筒状壁体及び底体部分の要部斜視図FIG. 3 is a perspective view of a main part of a tubular wall body and a bottom body portion of the present invention.
【図4】(A)は乾留ガス外部供給管及び底体部分の斜
視図 (B)は乾留ガス外部供給管の一部断面とした要部斜視
図FIG. 4 (A) is a perspective view of a dry distillation gas external supply pipe and a bottom portion. FIG. 4 (B) is a partial perspective view of a partial cross section of the dry distillation gas external supply pipe.
【図5】本発明の廃棄物貯蔵炉下部及び空気送風室部分
の縦断側面図FIG. 5 is a vertical cross-sectional side view of the lower part of the waste storage furnace and the air blower chamber of the present invention.
【図6】(A)は廃棄物貯蔵炉に廃棄物を投入した状態
を示す縦断側面図 (B)は廃棄物貯蔵炉内の下層部の廃棄物の乾留(燃
焼)処理を開始した状態を示す縦断側面図FIG. 6 (A) is a vertical cross-sectional side view showing a state in which the waste is put into the waste storage furnace, and FIG. 6 (B) shows a state in which the dry distillation (combustion) treatment of the waste in the lower layer in the waste storage furnace is started. Vertical side view showing
【図7】廃棄物貯蔵炉内の廃棄物の乾留(燃焼)処理状
態を示す要部の縦断側面図FIG. 7 is a vertical cross-sectional side view of essential parts showing a state of dry distillation (combustion) treatment of waste in a waste storage furnace.
【図8】(A)は廃棄物貯蔵炉内の廃棄物の下層部分の
乾留(燃焼)が進行し、上層部分の廃棄物が下方に移動
する状態を示す縦断側面図 (B)は廃棄物貯蔵炉に新たな廃棄物を投入する状態を
示す縦断側面図FIG. 8A is a vertical cross-sectional side view showing a state in which dry distillation (combustion) of the lower layer of the waste in the waste storage furnace proceeds and the waste of the upper layer moves downward. Vertical side view showing the state of charging new waste into the storage furnace
【図9】(A)は別のタイプの乾留ガス外部供給管及び
補助管部の斜視図 (B)は補助管部の下部から見た要部斜視図 (C)はさらに別のタイプの乾留ガス外部供給管及び補
助管部の要部斜視図9A is a perspective view of another type of dry distillation gas external supply pipe and an auxiliary pipe section. FIG. 9B is a perspective view of a main part seen from the lower part of the auxiliary pipe section. FIG. 9C is a further type of dry distillation. Perspective view of main parts of gas external supply pipe and auxiliary pipe
【図10】補助管部を装着した乾留ガス外部供給管を備
えた廃棄物貯蔵炉内の廃棄物の乾留(燃焼)状態を示す
要部の縦断側面図FIG. 10 is a vertical cross-sectional side view of a main part showing a state of dry distillation (combustion) of waste in a waste storage furnace equipped with a dry distillation gas external supply pipe equipped with an auxiliary pipe portion.
【図11】(A)は補助管部の断面図 (B)は別のタイプの補助管部の断面図FIG. 11A is a sectional view of an auxiliary pipe portion, and FIG. 11B is a sectional view of another type of auxiliary pipe portion.
【図12】(A)は第2実施形態の廃棄物貯蔵炉の縦断
側面図 (B)は第3実施形態の廃棄物貯蔵炉の要部縦断側面図FIG. 12 (A) is a vertical sectional side view of the waste storage furnace of the second embodiment. FIG. 12 (B) is a vertical sectional side view of a main part of the waste storage furnace of the third embodiment.
【図13】従来タイプの縦断側面図FIG. 13 is a vertical side view of a conventional type.
A…廃棄物貯蔵炉 1…筒状壁体 2…底体 3…送風流入孔 4…蓋体 B…空気送風室 C…乾留ガス外部供給管 7…管部 8…ガス流入孔 9…補助管部 10…スロート W…冷却水 A ... Waste storage furnace 1 ... Cylindrical wall 2 ... Bottom 3 ... Blow-in inlet 4 ... Lid B ... Air blower chamber C ... Dry distillation gas external supply pipe 7 ... Pipe section 8 ... Gas inlet 9 ... Auxiliary pipe Part 10 ... Throat W ... Cooling water
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 // C10G 1/02 B09B 3/00 302F 6958−4H C10L 3/00 A ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 6 Identification number Office reference number FI technical display location // C10G 1/02 B09B 3/00 302F 6958-4H C10L 3/00 A
Claims (6)
壁体の下部付近のみに複数の送風流入孔を設け、前記筒
状壁体の上端に開閉可能な蓋体を設けて密閉可能な廃棄
物貯蔵炉と、該廃棄物貯蔵炉の下部付近周囲を適宜の間
隔をおいて被覆して前記送風流入孔に空気を送り込む空
気送風室と、管部の下端を前記底板上面に固着し、前記
管部の上端は前記筒状壁体の上部側より外部に連通さ
せ、前記管部の下部寄りに複数のガス流入孔を設けた乾
留ガス外部供給管とからなり、前記筒状壁体,底体及び
管部には冷却水を循環可能に構成してなることを特徴と
する産業廃棄物の乾留処理装置。1. A bottom body is provided at a lower portion of the tubular wall body, a plurality of air blowing holes are provided only near a lower portion of the tubular wall body, and an openable / closable lid body is provided at an upper end of the tubular wall body. A heat-sealable waste storage furnace, an air blower chamber for covering the periphery of the lower part of the waste storage furnace at an appropriate interval and sending air to the air blow-in hole, and a lower end of a pipe portion on the bottom plate upper surface. The upper end of the tube portion is connected to the outside from the upper side of the tubular wall body, and the dry distillation gas external supply pipe is provided with a plurality of gas inflow holes near the lower portion of the tube portion. An apparatus for dry distillation of industrial waste, characterized in that cooling water can be circulated through the wall, bottom and pipe.
送風流入孔を設けてなることを特徴とする産業廃棄物の
乾留処理装置。2. The dry distillation treatment apparatus for industrial waste according to claim 1, wherein the bottom body is provided with a plurality of ventilation inlets.
部付近の周囲に放射状に補助管部を設け、該補助管部の
下面側に複数のガス流入孔を設けてなることを特徴とす
る産業廃棄物の乾留処理装置。3. The auxiliary pipe portion according to claim 1 or 2, wherein auxiliary pipe portions are radially provided around a lower portion of the pipe portion, and a plurality of gas inflow holes are provided on a lower surface side of the auxiliary pipe portion. Dry distillation treatment equipment for industrial waste.
外部供給管の管部と筒状壁体との間には、管部の外形よ
り大なる内径を有するスロートを設けてなることを特徴
とした産業廃棄物の乾留処理装置。4. The throat according to claim 1, wherein a throat having an inner diameter larger than an outer diameter of the pipe portion is provided between the pipe portion of the dry distillation gas external supply pipe and the cylindrical wall body. Dry distillation treatment equipment for industrial waste.
みに複数の送風流入孔を設け、前記筒状壁体の上端に開
閉可能な蓋体を設けて密閉可能な廃棄物貯蔵炉と、該廃
棄物貯蔵炉の下部付近周囲を適宜の間隔をおいて被覆し
て前記送風流入孔に空気を送り込む空気送風室と、管部
の下端を前記底板上面に固着し、前記管部の上端は前記
筒状壁体の上部側より外部に連通させ、前記管部の下部
寄りに複数のガス流入孔を設けた乾留ガス外部供給管と
からなり、前記筒状壁体,底体及び管部には冷却水を循
環可能に構成してなることを特徴とする産業廃棄物の乾
留処理装置。5. A waste material which can be hermetically sealed by providing a bottom body at the lower part of the tubular wall body, providing a plurality of air flow inlet holes only at the bottom plate, and providing an openable / closable lid body at the upper end of the tubular wall body. A storage furnace, an air blowing chamber for covering the periphery of the lower part of the waste storage furnace at an appropriate interval and sending air to the air blowing inlet, and a lower end of a pipe portion fixed to the upper surface of the bottom plate, and the pipe. The upper end of the section is composed of a dry distillation gas external supply pipe in which a plurality of gas inflow holes are provided near the lower part of the pipe portion, the upper end of the cylindrical wall body communicating with the outside, and the cylindrical wall body and the bottom body. An apparatus for dry distillation of industrial waste, characterized in that cooling water can be circulated in the pipe section.
の周囲に放射状に補助管部を設け、該補助管部の下面側
に複数のガス流入孔を設けてなることを特徴とする産業
廃棄物の乾留処理装置。6. The industry according to claim 5, wherein auxiliary pipe portions are radially provided around a lower portion of the pipe portion, and a plurality of gas inflow holes are provided on a lower surface side of the auxiliary pipe portion. Waste carbonization equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2157096A JPH09208962A (en) | 1996-02-07 | 1996-02-07 | Apparatus for dry-distillation treatment of industrial waste |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2157096A JPH09208962A (en) | 1996-02-07 | 1996-02-07 | Apparatus for dry-distillation treatment of industrial waste |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH09208962A true JPH09208962A (en) | 1997-08-12 |
Family
ID=12058695
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2157096A Pending JPH09208962A (en) | 1996-02-07 | 1996-02-07 | Apparatus for dry-distillation treatment of industrial waste |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH09208962A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006247437A (en) * | 2005-01-13 | 2006-09-21 | Okinawa Noren Kankyo Center | Thermal decomposition, carbonization and gasification treatment method for organic waste with no use of fuel |
JP2014504664A (en) * | 2011-01-05 | 2014-02-24 | パイラム イノベーションズ インターナショナル エス.エー. | Thermal reactor |
-
1996
- 1996-02-07 JP JP2157096A patent/JPH09208962A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006247437A (en) * | 2005-01-13 | 2006-09-21 | Okinawa Noren Kankyo Center | Thermal decomposition, carbonization and gasification treatment method for organic waste with no use of fuel |
JP2014504664A (en) * | 2011-01-05 | 2014-02-24 | パイラム イノベーションズ インターナショナル エス.エー. | Thermal reactor |
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