JPH11267614A - Carbonization treatment of combustible organic matter and equipment therefor - Google Patents

Carbonization treatment of combustible organic matter and equipment therefor

Info

Publication number
JPH11267614A
JPH11267614A JP11001533A JP153399A JPH11267614A JP H11267614 A JPH11267614 A JP H11267614A JP 11001533 A JP11001533 A JP 11001533A JP 153399 A JP153399 A JP 153399A JP H11267614 A JPH11267614 A JP H11267614A
Authority
JP
Japan
Prior art keywords
gas
carbonization
chamber
heating
carbonization chamber
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
Application number
JP11001533A
Other languages
Japanese (ja)
Inventor
Kazunari Aida
一成 会田
Tetsushi Mita
哲史 三田
Masaki Date
正記 伊達
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.)
Showa Denko Materials Co Ltd
Original Assignee
Hitachi Chemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi Chemical Co Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP11001533A priority Critical patent/JPH11267614A/en
Publication of JPH11267614A publication Critical patent/JPH11267614A/en
Pending legal-status Critical Current

Links

Landscapes

  • Treating Waste Gases (AREA)
  • Processing Of Solid Wastes (AREA)
  • Incineration Of Waste (AREA)
  • Gasification And Melting Of Waste (AREA)

Abstract

PROBLEM TO BE SOLVED: To efficiently and completely combust a large amount of a gas generated in a carbonization process of combustible organic matter, in a second combustion chamber in the equipment so as to convert the gas into a smokeless and odorless gas. SOLUTION: This equipment is provided with: a carbonization chamber 5 having a charging port 3 and a take-out port 4; a first combustion chamber 7 which is placed in such a way that the carbonization chamber 5 is enclosed in the chamber 7 and has a first burner 6 for heating the chamber 5; and a second combustion chamber 12 which has a second burner 9 for combusting a gas generated by heating charged combustible organic matter 13 in the carbonization chamber 5 and also an exhaust gas passage 10 for discharging the exhaust gas after the combustion and is communicated with the carbonization chamber 5 through an ascending gas pipe 8 and further has a heat insulating material 11 placed on the inside and also a heating promotion material 15 placed above the ascending gas pipe 8.

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、木材、紙、合成樹
脂又は(台所等から出る)生ゴミ等の可燃性有機物(廃
棄物)の炭化処理方法及び炭化処理装置に関し、更に詳
しくは、前記可燃性有機物を炭化処理して得られる処理
物(炭)を吸着剤、土壌改良材等に再利用できるととも
に、炭化工程で発生するガスを完全燃焼させ、排気の無
煙無臭化を図る炭化処理方法及び炭化処理装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for carbonizing flammable organic substances (wastes) such as wood, paper, synthetic resin or garbage (e.g., from kitchens). A carbonization method that can reuse the treated product (charcoal) obtained by carbonizing combustible organic matter as an adsorbent, soil improvement material, etc., and completely combust the gas generated in the carbonization process to make the exhaust gas smokeless and odorless. And a carbonization apparatus.

【0002】[0002]

【従来の技術】従来の炭化処理装置の例を図12に示し
た。Aは正面断面図、Bは側面断面図で、この炭化処理
装置は、立設する4面、底面及び天井面が金属製板材で
成る方形のケーシング内に、可燃性有機物を投入する投
入口と処理物を取り出すための取出口を備えた炭化室
と、その炭化室を囲むようにして形成されるとともにそ
の炭化室を加熱する第一バーナを有する第一燃焼室と、
投入された可燃性有機物を炭化室で加熱することにより
発生したガスを燃焼させる第二バーナ並びに燃焼させた
後のガス(排ガス)を排出する排気通路を有し、前記炭
化室とはガス上昇管を介して連通し、かつ、その内部に
は断熱材(図示せず)が設けられた第二燃焼室、とを備
えている。
2. Description of the Related Art FIG. 12 shows an example of a conventional carbonization apparatus. A is a front sectional view, and B is a side sectional view. This carbonization apparatus has an inlet for charging flammable organic matter in a rectangular casing whose four surfaces, a bottom surface, and a ceiling surface are made of a metal plate. A carbonization chamber having an outlet for taking out the processed material, and a first combustion chamber formed to surround the carbonization chamber and having a first burner for heating the carbonization chamber,
It has a second burner for burning gas generated by heating the charged combustible organic matter in the carbonization chamber and an exhaust passage for discharging gas (exhaust gas) after combustion, and the carbonization chamber is a gas riser And a second combustion chamber provided with a heat insulating material (not shown) therein.

【0003】[0003]

【発明が解決しようとする課題】炭化処理装置では、炭
化室で発生するガスを効率よく完全燃焼させ無煙無臭化
するためには、このガスをすべて第二燃焼室において、
通常、700℃〜1000℃の温度で十分に熱する必要
がある。しかし、前記した従来の処理装置では、ガスの
流れる方向により炭化室からのガスがすべて第二バーナ
で燃焼処理されるとは限らない。
In the carbonization treatment apparatus, in order to efficiently and completely combust the gas generated in the carbonization chamber to make it smokeless and odorless, all of the gas is supplied to the second combustion chamber.
Usually, it is necessary to heat sufficiently at a temperature of 700C to 1000C. However, in the conventional processing apparatus described above, not all of the gas from the coking chamber is burned by the second burner depending on the direction in which the gas flows.

【0004】また、第二燃焼室内が冷えきっている状
態、例えば、低温下での運転開始時等においては断熱材
表面の温度上昇速度が遅く、第二燃焼室内が700℃〜
1000℃の高温域に達するまでに時間を要するため、
炭化室からのガスが第二燃焼室内で十分に燃焼処理され
ず不完全燃焼の状態で排出されてしまう。さらに、生ご
み等の水分を多く含む可燃性有機物の場合は、炭化処理
工程で炭化室が熱せられることにより可燃性有機物の水
分が蒸発し、これが第二燃焼室へ流入するとともに第二
燃焼室の断熱材表面に付着し、断熱材に湿気を帯びさ
せ、第二燃焼室内の温度が高温状態を保持できない問題
がある。
In a state where the second combustion chamber is completely cooled, for example, when the operation is started at a low temperature, the temperature rise rate of the surface of the heat insulating material is slow, and the temperature of the second combustion chamber is 700 ° C.
Because it takes time to reach the high temperature range of 1000 ° C,
The gas from the carbonization chamber is not sufficiently burned in the second combustion chamber and is discharged in an incomplete combustion state. Furthermore, in the case of flammable organic substances containing a large amount of water such as garbage, the water of the flammable organic substances evaporates due to the heating of the carbonization chamber in the carbonization treatment step, which flows into the second combustion chamber and the second combustion chamber. On the surface of the heat insulating material, causing the heat insulating material to be moist, and the temperature in the second combustion chamber cannot be maintained at a high temperature.

【0005】一方、可燃性有機物を一度に大量に処理し
ようとする場合には、炭化室が大型化するとともに、そ
れに伴い第二燃焼室も大型化する。第二燃焼室には炭化
室からのガスを燃焼させるための第二バーナを設けてい
るが、第二燃焼室の容積が大きくなればなるほど、燃焼
室内の温度分布のバラツキが大きくなり、高温域と低温
域が生じる。これを防ぐ方策としては、バーナを複数個
設けたり、燃焼能力の大きいバーナを取り付けなくては
ならない。本発明は、可燃性有機物の炭化工程で発生す
る多量のガスを第二燃焼室で効率よく完全燃焼させ、こ
れを無煙無臭化できる炭化処理方法又は炭化処理装置を
提供することを目的とする。
On the other hand, when a large amount of combustible organic matter is to be treated at one time, the size of the carbonization chamber is increased and the size of the second combustion chamber is also increased accordingly. Although the second combustion chamber is provided with a second burner for burning gas from the carbonization chamber, the larger the volume of the second combustion chamber, the greater the variation in the temperature distribution in the combustion chamber, and the higher the temperature And a low temperature region occurs. As measures to prevent this, it is necessary to provide a plurality of burners or attach a burner having a large combustion capacity. An object of the present invention is to provide a carbonization method or a carbonization apparatus capable of efficiently and completely combusting a large amount of gas generated in a carbonization step of a combustible organic substance in a second combustion chamber to make it smokeless and odorless.

【0006】[0006]

【課題を解決するための手段】上記目的を達成するた
め、本発明における可燃性有機物の炭化処理方法では次
の構成をとった。すなわち、本発明の炭化処理方法にお
いては、可燃性有機物を炭化室で加熱し、発生したガス
をガス上昇管を介して第二燃焼室に導き、燃焼させ、そ
の排ガスを排気通路から排出させる際、前記ガス上昇管
の上方に加熱促進材を設置し炭化室からのガスの完全燃
焼を促進させながら、可燃性有機物を処理することを特
徴とする。ここで、加熱促進材としては、耐熱性金属又
は耐熱性セラミック製で、その形状が平板状、円筒状、
多面体状、球状あるいは網状の部材からなる加熱促進材
を用いることができる。
Means for Solving the Problems In order to achieve the above object, the method for carbonizing combustible organic substances according to the present invention has the following configuration. That is, in the carbonization method of the present invention, when combustible organic matter is heated in the carbonization chamber, the generated gas is guided to the second combustion chamber via the gas riser, burned, and the exhaust gas is discharged from the exhaust passage. In addition, a heat-promoting material is provided above the gas riser to treat the combustible organic matter while promoting complete combustion of the gas from the carbonization chamber. Here, the heat-promoting material is made of a heat-resistant metal or a heat-resistant ceramic, and has a flat plate shape, a cylindrical shape,
A heating accelerator made of a polyhedral, spherical or net-like member can be used.

【0007】また、本発明の炭化処理装置では次の構成
をとった。すなわち、本発明の炭化処理装置1は、可燃
性有機物の投入口3及び処理物の取出口4を有する炭化
室5と、前記炭化室5を囲むようにして形成されるとと
もにその炭化室5を加熱する第一バーナ6を有する第一
燃焼室7と、投入された可燃性有機物13を炭化室5で
加熱することにより発生したガスを燃焼させる第二バー
ナ9並びに燃焼させた後のガスを排出する排気通路10
を有し、前記炭化室5とはガス上昇管8を介して連通
し、かつその内部には断熱材11が設けられた第二燃焼
室12、とを備える可燃性有機物の炭化処理装置であっ
て、炭化室5と第二燃焼室12とを接続しているガス上
昇管8の上方に加熱促進材15が設置された構造であ
る。なお、加熱促進材15としては、耐熱性金属又は耐
熱性セラミック製で、その形状が平板状、円筒状、多面
体状、球状あるいは網状の部材から選ぶことができる。
[0007] The carbonization apparatus of the present invention has the following configuration. That is, the carbonization treatment apparatus 1 of the present invention is formed so as to surround the carbonization chamber 5 and has the carbonization chamber 5 having the flammable organic substance inlet 3 and the processed material outlet 4, and heats the carbonization chamber 5. A first combustion chamber 7 having a first burner 6; a second burner 9 for burning gas generated by heating the charged combustible organic substance 13 in the carbonization chamber 5; and an exhaust for discharging gas after combustion. Passage 10
And a second combustion chamber 12 in communication with the carbonization chamber 5 through a gas riser pipe 8 and having a heat insulating material 11 provided therein. Thus, the structure is such that the heating promoting material 15 is installed above the gas riser pipe 8 connecting the carbonization chamber 5 and the second combustion chamber 12. The heating accelerator 15 is made of a heat-resistant metal or a heat-resistant ceramic, and can be selected from flat, cylindrical, polyhedral, spherical or net-like members.

【0008】[0008]

【発明の実施の形態】以下に、本発明に係る炭化処理方
法及び炭化処理装置の実施の形態を図を用いて説明す
る。図1は、本発明の一実施例の炭化処理装置で、Aは
正面断面図、Bは側面断面図である。炭化処理装置1に
は、可燃性有機物の投入口3及び処理物(炭)の取出口
4を有する炭化室5と、前記炭化室5を囲むようにして
形成されるとともにその炭化室5を加熱する第一バーナ
6を有する第一燃焼室7と、投入された可燃性有機物
(廃棄物)13を炭化室5で加熱することにより発生し
たガスを燃焼させる第二バーナ9並びに燃焼させた後の
ガス(排ガス)を排出する排気通路10を有し、前記炭
化室5とはガス上昇管8を介して連通し、かつその内部
には断熱材11が配された第二燃焼室12が設けられ、
これらはケーシング2内に収納されている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of a carbonization method and a carbonization apparatus according to the present invention will be described below with reference to the drawings. FIG. 1 is a carbonization apparatus according to one embodiment of the present invention, wherein A is a front sectional view and B is a side sectional view. The carbonization treatment apparatus 1 includes a carbonization chamber 5 having an inlet 3 for combustible organic matter and an outlet 4 for treated material (char), and a carbonization chamber 5 formed to surround the carbonization chamber 5 and heating the carbonization chamber 5. A first combustion chamber 7 having one burner 6, a second burner 9 for burning gas generated by heating the charged combustible organic matter (waste) 13 in the carbonization chamber 5, and a gas after burning ( A second combustion chamber 12 provided with an exhaust passage 10 for discharging exhaust gas, communicating with the carbonization chamber 5 via a gas rising pipe 8, and having a heat insulating material 11 disposed therein.
These are accommodated in the casing 2.

【0009】炭化室5に投入された可燃性有機物13
は、第一燃焼室7に設けられた第一バーナ6で炭化室5
を加熱することにより無酸素状態で蒸し焼きされる。第
二燃焼室12は、炭化室5の上方に位置し、ガス上昇管
8を介して第二燃焼室12と炭化室5とは連通するよう
に構成されている。
The flammable organic substance 13 charged into the carbonization chamber 5
Is the first burner 6 provided in the first combustion chamber 7 and the carbonization chamber 5
Is heated and steamed in an oxygen-free state. The second combustion chamber 12 is located above the carbonization chamber 5 and is configured to communicate with the second combustion chamber 12 and the carbonization chamber 5 via the gas rising pipe 8.

【0010】第二燃焼室12では、炭化室5内の可燃性
有機物13から発生するガスを燃焼する第二バーナ9を
備える他、その燃焼後のガス(排ガス)を排気放出する
ための排気通路10を有し、排気通路10は第二燃焼室
12の上部に設けられている。可燃性有機物13から発
生する水分や不完全燃焼ガスは、炭化室5と第二燃焼室
12とを接続するガス上昇管8内を通り第二燃焼室へ流
入する。
The second combustion chamber 12 includes a second burner 9 for burning gas generated from the combustible organic matter 13 in the carbonization chamber 5 and an exhaust passage for discharging the burned gas (exhaust gas). The exhaust passage 10 is provided above the second combustion chamber 12. Moisture and incomplete combustion gas generated from the combustible organic matter 13 flow into the second combustion chamber through the gas rising pipe 8 connecting the carbonization chamber 5 and the second combustion chamber 12.

【0011】第二燃焼室の内部には、加熱促進材14
(図1では3枚)がガス上昇管8の上方(直上又はその
近傍)に所定の間隔でスペーサ15を介し底面に対し平
行に配置されている。
[0011] Inside the second combustion chamber, a heating promoting material 14 is provided.
1 (three in FIG. 1) are disposed above (directly above or in the vicinity of) the gas riser tube 8 at predetermined intervals in parallel with the bottom surface via a spacer 15.

【0012】用いる加熱促進材14は、炭化室5で発生
する水分やガスの加熱・燃焼を助けるものであって、耐
熱性があり熱伝導性能の良い材質が好ましい。金属製、
セラミック製、黒鉛(カーボン)等から選ばれ、例え
ば、ステンレスやチタニウム等がある。またその形状
は、その加熱促進材表面にガスができる限り多く接触す
る構造が好ましく、穴付き平板状、円筒状、多面体、球
状、網状等がある。
The heating accelerator 14 is used to assist the heating and combustion of moisture and gas generated in the carbonization chamber 5, and is preferably made of a material having heat resistance and good heat conduction performance. metallic,
The material is selected from ceramics, graphite (carbon), and the like, for example, stainless steel and titanium. The shape is preferably such that the gas contacts the surface of the heating accelerator as much as possible, and may be a flat plate with a hole, a cylinder, a polyhedron, a sphere, a net, or the like.

【0013】図2は、用いられる加熱促進材の一例(角
穴付き平板)で、Aは図1に示したような3枚構成とし
た場合における1枚目と3枚目の形状の平面図を示し、
Bは2枚目(中間)の形状の平面図を示す。図2に示す
ように任意の大きさの平板に複数の穴が設けられてお
り、1枚目と2枚目の穴は千鳥となるように穴が配置さ
れ、2枚目と3枚目も同じように各々の穴が千鳥の位置
となるように配置されている。
FIG. 2 is an example (a flat plate with square holes) of a heating accelerating material to be used, and A is a plan view of the first and third shapes in the case of a three-sheet structure as shown in FIG. Indicates that
B shows a plan view of the second (middle) shape. As shown in FIG. 2, a plurality of holes are provided in a flat plate of an arbitrary size, holes are arranged so that the first and second holes are staggered, and the second and third holes are also provided. Similarly, the holes are arranged so as to be in a staggered position.

【0014】この加熱促進材は第二燃焼室12に設けら
れた第二バーナ9により高温に熱せられる。炭化室5に
投入した可燃性有機物13が蒸し焼きされることにより
発生する水分や不完全燃焼のガスが、ガス上昇管8を通
り第二燃焼室12内に流入した際、この加熱促進材に接
触し、水分の高温加熱や不完全燃焼ガスの完全燃焼が効
率よく起こる。また、前述の通り3枚設けた平板の穴は
各々が千鳥の位置となるよう配置されているため、上昇
ガスは前記加熱促進材の表面に効果的に接触する。
The heating accelerator is heated to a high temperature by a second burner 9 provided in the second combustion chamber 12. When moisture or incompletely combusted gas generated by the burning of the combustible organic substance 13 charged into the carbonization chamber 5 flows into the second combustion chamber 12 through the gas riser tube 8, it contacts the heating promoting material. Then, high-temperature heating of moisture and complete combustion of incomplete combustion gas occur efficiently. Further, as described above, since the holes of the three flat plates are arranged at the staggered positions, the rising gas effectively contacts the surface of the heating promoting material.

【0015】上記の例においては、平板状加熱促進材は
3枚の構成としたが、3枚に限定されない。1〜2枚又
は4枚以上の複数枚の構成としても差し支えない。ま
た、平板状加熱促進材には、図2に示すような角穴のほ
かに図3に示すような丸穴が設けられているものでもよ
く、また図4に示すような網状物等でもよい。
In the above-described example, the number of the plate-shaped heating accelerators is three, but the number is not limited to three. A configuration of one or two or four or more sheets may be used. Further, the flat heating accelerator may be provided with a round hole as shown in FIG. 3 in addition to the square hole as shown in FIG. 2, or may be a mesh or the like as shown in FIG. .

【0016】また、加熱促進材の形状は、図5に示すよ
うな波状板や図6に示すような平板に切り起こしを設け
た形状でもよい。更に、加熱促進材の形状は、図7〜図
9に示すような円筒状、多面体、球状のものであっても
よい。配置の方法については、図11のように平板状加
熱促進材を底面に垂直に配置したり、傾斜をつけて配置
(図示せず)してもよい。
The shape of the heating accelerator may be a corrugated plate as shown in FIG. 5 or a flat plate as shown in FIG. Further, the shape of the heating promoting material may be cylindrical, polyhedral, or spherical as shown in FIGS. Regarding the arrangement method, the plate-shaped heating promoting material may be arranged perpendicular to the bottom surface as shown in FIG. 11 or may be arranged with an inclination (not shown).

【0017】[0017]

【発明の効果】本発明の炭化処理方法又は炭化処理装置
により、以下の効果を奏する。 (1)第二燃焼室の構造・容積に大きく左右されずに、
炭化室からの水分及び発生ガスを効率よく加熱・燃焼で
きる。 (2)第二燃焼室内の温度が高温域に達しない場合で
も、炭化室からの水分又は発生ガスを加熱・燃焼でき
る。 (3)第二燃焼室内に高温域と低温域の温度分布のバラ
ツキが生じた場合でも、それに大きく左右されずに炭化
室からの水分又は発生ガスを加熱・燃焼できる。 (4)炭化室で発生したガスが効率よく高温に熱せられ
ることにより、排ガスの無煙無臭化を図ることができ
る。
According to the carbonizing method or the carbonizing apparatus of the present invention, the following effects can be obtained. (1) Without being greatly influenced by the structure and volume of the second combustion chamber,
Moisture and generated gas from the carbonization chamber can be efficiently heated and burned. (2) Even when the temperature in the second combustion chamber does not reach the high temperature range, the water or generated gas from the carbonization chamber can be heated and burned. (3) Even when the temperature distribution in the high temperature range and the low temperature range varies in the second combustion chamber, the moisture or generated gas from the carbonization chamber can be heated and burned without being largely influenced by the variation. (4) Since the gas generated in the carbonization chamber is efficiently heated to a high temperature, smokeless and odorless exhaust gas can be achieved.

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

【図1】本発明の一実施例の炭化処理装置で、Aは正面
断面図、Bは側面断面図である。
FIG. 1 is a carbonization apparatus according to one embodiment of the present invention, wherein A is a front sectional view and B is a side sectional view.

【図2】本発明の加熱促進材の一例(角穴付き平板)の
平面図を示す。Aは図1に示したような3枚構成とした
場合における1枚目と3枚目の形状を示し、Bは2枚目
(中間)の形状を示す。
FIG. 2 shows a plan view of an example of the heating accelerating material of the present invention (a flat plate with square holes). A shows the shape of the first and third sheets in the case of a three-sheet configuration as shown in FIG. 1, and B shows the shape of the second (middle) sheet.

【図3】本発明の加熱促進材の他の例(丸穴付き平板)
の平面図を示す。
FIG. 3 shows another example of the heating accelerator of the present invention (a flat plate with a round hole).
FIG.

【図4】本発明の加熱促進材の他の例(網状物)の平面
図を示す。
FIG. 4 shows a plan view of another example (net-like material) of the heating accelerator of the present invention.

【図5】本発明の加熱促進材の他の例(波状板)の平面
図を示す。
FIG. 5 is a plan view of another example (corrugated plate) of the heating accelerator of the present invention.

【図6】本発明の加熱促進材の他の例(切り起こしを設
けた平板)の平面図を示す。
FIG. 6 is a plan view of another example (a flat plate provided with cut-and-raised portions) of the heating accelerator of the present invention.

【図7】本発明の加熱促進材の他の例(多面体)の平面
図(A)及び正面図(B)である。
FIG. 7 is a plan view (A) and a front view (B) of another example (polyhedron) of the heating accelerating material of the present invention.

【図8】本発明の加熱促進材の他の例(多面体)の平面
図(A)及び正面図(B)である。
FIG. 8 is a plan view (A) and a front view (B) of another example (polyhedron) of the heating accelerating material of the present invention.

【図9】本発明の加熱促進材の他の例(球状体)を示す
正面図である。
FIG. 9 is a front view showing another example (spherical body) of the heating accelerator of the present invention.

【図10】本発明の他の実施例の第二燃焼室の断面図を
示す。
FIG. 10 is a sectional view of a second combustion chamber according to another embodiment of the present invention.

【図11】本発明の別の実施例の第二燃焼室の断面図を
示す。
FIG. 11 shows a sectional view of a second combustion chamber according to another embodiment of the present invention.

【図12】従来の炭化処理装置で、Aは正面断面図、B
は側面断面図である。
FIG. 12 is a conventional carbonization apparatus, in which A is a front sectional view, and B is
Is a side sectional view.

【符号の説明】[Explanation of symbols]

1:炭化処理装置 2:ケーシング 3:投入口 4:取出口 5:炭化室 6:第一バーナ 7:第一燃焼室 8:ガス上昇管 9:第二バーナ 10:排気通路 11:断熱材 12:第二燃焼室 13:可燃性有機物(廃棄物) 14:加熱促進材 15:スペーサ 1: Carbonization treatment device 2: Casing 3: Inlet 4: Outlet 5: Carbonization chamber 6: First burner 7: First combustion chamber 8: Gas riser 9: Second burner 10: Exhaust passage 11: Heat insulating material 12 : Second combustion chamber 13: Combustible organic matter (waste) 14: Heating promoter 15: Spacer

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】可燃性有機物を炭化室で加熱し、発生した
ガスをガス上昇管を介して第二燃焼室に導き、燃焼さ
せ、その排ガスを排気通路から排出させる際、前記ガス
上昇管の上方に加熱促進材を設置し炭化室からのガスの
完全燃焼を促進させる、可燃性有機物の炭化処理方法。
1. When a combustible organic substance is heated in a carbonization chamber, generated gas is led to a second combustion chamber via a gas riser, burned, and the exhaust gas is discharged from an exhaust passage. A method for carbonizing combustible organic matter, in which a heating accelerator is provided above to promote complete combustion of gas from a carbonization chamber.
【請求項2】加熱促進材が、耐熱性金属又は耐熱性セラ
ミック製で、その形状が平板状、円筒状、多面体状、球
状あるいは網状の部材である、請求項1の炭化処理方
法。
2. The carbonization method according to claim 1, wherein the heat-promoting material is made of a heat-resistant metal or a heat-resistant ceramic, and has a shape of a plate, a cylinder, a polyhedron, a sphere, or a net.
【請求項3】可燃性有機物の投入口及び処理物の取出口
を有する炭化室と、 前記炭化室を囲むようにして形成されるとともにその炭
化室を加熱する加熱手段を有する第一燃焼室と、 投入された可燃性有機物を炭化室で加熱することにより
発生したガスを燃焼させる第二バーナ並びに燃焼させた
後のガスを排出する排気通路を有し、前記炭化室とはガ
ス上昇管を介して連通し、かつその内部には断熱材が設
けられた第二燃焼室とを備える可燃性有機物の炭化処理
装置であって、前記ガス上昇管の上方には加熱促進材が
設置された炭化処理装置。
3. A carbonization chamber having an inlet for flammable organic matter and an outlet for processed material, a first combustion chamber formed to surround the carbonization chamber and having heating means for heating the carbonization chamber. A second burner for burning the gas generated by heating the combustible organic matter in the carbonization chamber, and an exhaust passage for discharging the gas after the combustion, and communicating with the carbonization chamber via a gas riser. And a second combustion chamber provided with a heat insulating material therein. A carbonizing apparatus for combustible organic matter, wherein a heating accelerating material is provided above the gas riser.
【請求項4】加熱促進材が、耐熱性金属又は耐熱性セラ
ミック製で、その形状が平板状、円筒状、多面体状、球
状あるいは網状の部材である、請求項3の炭化処理装
置。
4. The carbonization apparatus according to claim 3, wherein the heat-promoting material is made of a heat-resistant metal or a heat-resistant ceramic and has a shape of a plate, a cylinder, a polyhedron, a sphere, or a net.
JP11001533A 1998-01-20 1999-01-07 Carbonization treatment of combustible organic matter and equipment therefor Pending JPH11267614A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11001533A JPH11267614A (en) 1998-01-20 1999-01-07 Carbonization treatment of combustible organic matter and equipment therefor

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP853698 1998-01-20
JP10-8536 1998-01-20
JP11001533A JPH11267614A (en) 1998-01-20 1999-01-07 Carbonization treatment of combustible organic matter and equipment therefor

Publications (1)

Publication Number Publication Date
JPH11267614A true JPH11267614A (en) 1999-10-05

Family

ID=26334757

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11001533A Pending JPH11267614A (en) 1998-01-20 1999-01-07 Carbonization treatment of combustible organic matter and equipment therefor

Country Status (1)

Country Link
JP (1) JPH11267614A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003053312A (en) * 2001-08-22 2003-02-25 Kyoritsu Kogyo Kk Carbonization and volume reduction plant
JPWO2005108866A1 (en) * 2004-05-11 2008-03-21 株式会社ダイソー Waste treatment equipment
JP2008111605A (en) * 2006-10-31 2008-05-15 Nikko Kinzoku Kk Gas igniting method and gas treatment furnace
JP2011021779A (en) * 2009-07-14 2011-02-03 Katsura Seiki Seisakusho:Kk Direct combustion type deodorization furnace

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003053312A (en) * 2001-08-22 2003-02-25 Kyoritsu Kogyo Kk Carbonization and volume reduction plant
JPWO2005108866A1 (en) * 2004-05-11 2008-03-21 株式会社ダイソー Waste treatment equipment
JP4735985B2 (en) * 2004-05-11 2011-07-27 株式会社ダイソー Waste treatment equipment
JP2008111605A (en) * 2006-10-31 2008-05-15 Nikko Kinzoku Kk Gas igniting method and gas treatment furnace
JP2011021779A (en) * 2009-07-14 2011-02-03 Katsura Seiki Seisakusho:Kk Direct combustion type deodorization furnace

Similar Documents

Publication Publication Date Title
JPH11267614A (en) Carbonization treatment of combustible organic matter and equipment therefor
JPH11286684A (en) Continuous carbonization furnace
CN116697359A (en) Folding three-effect fire grate process
JP2010005581A (en) Organic treating object decomposition apparatus, and organic matter decomposing method using the same
CN212584950U (en) Double-chamber temperature control device of incinerator
TWM626739U (en) Cooking and biochar production dual-purpose stove equipment
JPH08157832A (en) Treatment of bamboo material or the like
JP2674086B2 (en) Exhaust gas treatment equipment
RU2272960C1 (en) Fuel combustion device
CN109416220B (en) Externally heated pyrolysis furnace for processing solid carbonaceous materials (variants)
CN214664451U (en) Chemical industry residue treatment incinerator
JP2000144144A (en) Carbonization equipment having exhaust chamber
KR100823523B1 (en) A carbonizing apparatus for food waste
CN212566926U (en) Tunnel furnace waste tar gas combustion device
CN209341260U (en) A kind of plasma three wastes gasification process furnace
CN217441669U (en) Flue gas treatment device of low-temperature magnetization pyrolysis device
CN210717557U (en) Combustion chamber structure
CN216844705U (en) Heat-storage wind-equalizing functional incinerator
JPS6044758A (en) Method and apparatus for heating water
JPH0522809B2 (en)
CN219283341U (en) Domestic waste high temperature carbonization device
JP7190726B2 (en) Self-burning carbonization heat treatment apparatus, carbonization heat treatment system, and carbide production method using the same
KR880002343Y1 (en) Recombustion device
KR800001352B1 (en) Regeneration equipment for spent activated carbon
CN113719830A (en) Improved combustion furnace