JPS634447B2 - - Google Patents
Info
- Publication number
- JPS634447B2 JPS634447B2 JP58007371A JP737183A JPS634447B2 JP S634447 B2 JPS634447 B2 JP S634447B2 JP 58007371 A JP58007371 A JP 58007371A JP 737183 A JP737183 A JP 737183A JP S634447 B2 JPS634447 B2 JP S634447B2
- Authority
- JP
- Japan
- Prior art keywords
- reaction vessel
- treated
- mineral
- gas
- feeder
- 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.)
- Expired
Links
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 39
- 239000011707 mineral Substances 0.000 claims description 39
- 239000000463 material Substances 0.000 claims description 38
- 238000006243 chemical reaction Methods 0.000 claims description 36
- 238000003756 stirring Methods 0.000 claims description 13
- 239000000126 substance Substances 0.000 claims description 13
- 238000000605 extraction Methods 0.000 claims description 10
- 238000000197 pyrolysis Methods 0.000 claims description 3
- 239000007789 gas Substances 0.000 description 24
- 238000005979 thermal decomposition reaction Methods 0.000 description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 239000002699 waste material Substances 0.000 description 6
- 229910052799 carbon Inorganic materials 0.000 description 5
- 238000000354 decomposition reaction Methods 0.000 description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000004215 Carbon black (E152) Substances 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 150000001247 metal acetylides Chemical class 0.000 description 2
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000010909 process residue Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000010801 sewage sludge Substances 0.000 description 1
- 230000001568 sexual effect Effects 0.000 description 1
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 229920003051 synthetic elastomer Polymers 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 229920001059 synthetic polymer Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000005061 synthetic rubber Substances 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J6/00—Heat treatments such as Calcining; Fusing ; Pyrolysis
- B01J6/008—Pyrolysis reactions
Landscapes
- Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Processing Of Solid Wastes (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
【発明の詳細な説明】
本発明は、下水スラツジ、人畜糞尿、各種食品
加工廃棄物、農林産業廃棄物等の有機性廃棄物、
廃合成繊維、廃合成樹脂、廃合成ゴム等の廃合成
高分子化合物、更には石炭等を加熱分解して油や
可燃性ガスを取得するに用いる熱分解反応装置に
関する。更に詳しくは、流動床焼却炉を応用した
熱分解反応装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to organic wastes such as sewage sludge, human and animal manure, various food processing wastes, agricultural and forestry industry wastes,
The present invention relates to a thermal decomposition reaction device used to thermally decompose waste synthetic polymer compounds such as waste synthetic fibers, waste synthetic resins, and waste synthetic rubbers, as well as coal and the like to obtain oil and flammable gas. More specifically, the present invention relates to a pyrolysis reactor using a fluidized bed incinerator.
従来、残渣取出用のマンホールを備えた反応容
器の上部に、被処理物供給用のホツパーとガス抽
出管を連結し、反応容器の下方にバーナーを設
け、更に反応容器内で回転する翼板を設けた熱分
解反応装置が知られている（実開昭50−79736
号）。この装置は、適量の被処理物をホツパーか
ら反応容器内に投入し、これを翼板で撹拌しなが
ら蒸し焼き状に加熱分解し、発生したガスをガス
抽出管から取出して凝縮させ、油と可燃性ガスを
分離取得しようとするものである。また、分解残
渣は、反応容器が十分冷えてから、マンホールか
ら取出されるものである。 Conventionally, a hopper for supplying the material to be treated and a gas extraction pipe were connected to the upper part of the reaction vessel equipped with a manhole for taking out the residue, a burner was provided below the reaction vessel, and a vane rotating inside the reaction vessel was installed. A thermal decomposition reactor is known (Utility Model No. 50-79736
issue). This equipment charges an appropriate amount of the material to be treated from a hopper into a reaction vessel, heats and decomposes it into a steaming state while stirring it with blades, and extracts the generated gas from a gas extraction tube and condenses it to form oil and combustibles. This is an attempt to separate and obtain sexual gases. Further, the decomposition residue is taken out from the manhole after the reaction vessel has sufficiently cooled down.
しかしながら、従来の装置ではバツチ処理とな
るため、運転効率が悪い問題がある。 However, since the conventional apparatus performs batch processing, there is a problem of poor operational efficiency.
一方、本発明者は、熱分解反応を行うに際し、
粉粒状鉱物質と高温下で接触させながら行うと、
油や可燃性ガスの回収率が極めて向上することを
見出した。これは、粉粒状鉱物質を被処理物と共
に反応容器内に投入することにより、前記従来の
装置でも行うことができる。しかし、前記従来の
装置では、分解残渣の排出と共に粉粒状鉱物質も
入れ替えなければならなくなり、無駄が多くなつ
て経済的な運転は望めなくなる。 On the other hand, when carrying out a thermal decomposition reaction, the present inventor
When carried out in contact with granular mineral materials at high temperatures,
It was found that the recovery rate of oil and flammable gas was significantly improved. This can also be done with the conventional apparatus by introducing the granular mineral material into the reaction vessel together with the material to be treated. However, in the conventional apparatus, as well as discharging the decomposition residue, the particulate mineral must also be replaced, resulting in a large amount of waste and making it impossible to expect economical operation.
本発明は、粉粒状鉱物質を用いて熱分解反応を
行うに際し、連続的な処理と、分解残渣である炭
化物と粉粒状鉱物質の分別排出を可能にすること
を目的とする。 An object of the present invention is to enable continuous treatment and separate discharge of carbides and granular minerals, which are decomposition residues, when carrying out a thermal decomposition reaction using granular minerals.
本発明は、流動床式焼却炉の原理と応用して上
記目的を達成したものである。即ち、本発明は、
粉粒状鉱物質が入れられて少なくとも底面から加
熱を受ける反応容器と、この反応容器の一側端部
上方から、外気から反応容器内を遮断した状態で
被処理物を反応容器内へ送り込む供給機と、反応
容器の他側端部の、粉粒状鉱物質の上面よりやや
上方に開口された排出シユーターと、反応容器の
上部に開口された、発生ガスを取出すためのガス
抽出管と、供給機の設けられた反応容器の一側端
部側から排出シユーターの設けられた反応容器の
他側端部側へと被処理物を押しながら粉粒状鉱物
質を撹拌する撹拌羽根とを有する粉粒状鉱物質を
用いた熱分解反応装置である。 The present invention achieves the above object by applying the principle of a fluidized bed incinerator. That is, the present invention
A reaction vessel in which a granular mineral substance is placed and heated at least from the bottom, and a feeder that feeds the material to be treated into the reaction vessel from above one end of the reaction vessel, with the inside of the reaction vessel being shut off from the outside air. , a discharge shooter at the other end of the reaction vessel that opens slightly above the top surface of the powdery mineral, a gas extraction pipe that opens at the top of the reaction vessel to take out the generated gas, and a supply machine. A granular mineral having a stirring blade that stirs the granular mineral while pushing the object to be treated from one end of the reaction container provided with a discharge shooter to the other end of the reaction container provided with a discharge shooter. This is a pyrolysis reactor using high quality materials.
以下、本発明の実施例を示す図面に基づいて本
発明を更に詳細に説明する。 DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in more detail below based on drawings showing embodiments of the present invention.
第１図は本発明に係る熱分解反応装置の一実施
例を示す縦断面図、第２図はそのＡ−A′断面図
である。 FIG. 1 is a longitudinal cross-sectional view showing an embodiment of the thermal decomposition reactor according to the present invention, and FIG. 2 is a cross-sectional view taken along the line A-A'.
図中１は底面がＵ字形を成す反応容器で、この
反応容器の下方には、バーナー２から炎が送り込
まれる燃焼室３が形成されている。反応容器１内
には、粉粒状鉱物質４が入れられており、この粉
粒状鉱物質４をバーナー２によつて底面から直接
加熱するものとなつている。 In the figure, reference numeral 1 denotes a reaction vessel whose bottom surface is U-shaped, and a combustion chamber 3 into which flame is sent from a burner 2 is formed below this reaction vessel. A granular mineral substance 4 is contained in the reaction vessel 1, and the granular mineral substance 4 is heated directly from the bottom surface by a burner 2.
反応容器１の最上段にはガス抽出管５、ガス抽
出管５のやや下方に供給機６、粉粒状鉱物質４の
上面のやや上方に回転軸７が各々設けられてい
る。 A gas extraction pipe 5 is provided at the top of the reaction vessel 1, a feeder 6 is provided slightly below the gas extraction pipe 5, and a rotating shaft 7 is provided slightly above the upper surface of the powdery mineral material 4.
ガス抽出管５は、図示されていないが、冷却器
に連結されていて、発生ガスを冷却器に導びいて
これを冷却し、液化成分とガス成分を分離取得す
るためのものである。そして、このガス抽出管５
は、粉粒状鉱物質４や発生する炭化物の侵入を防
止するためにできるだけ粉粒状鉱物質４から離し
ておくことが好ましい。 Although not shown, the gas extraction pipe 5 is connected to a cooler, and is used to guide the generated gas to the cooler, cool it, and separate and obtain a liquefied component and a gas component. And this gas extraction pipe 5
It is preferable to keep it as far away from the granular mineral material 4 as possible in order to prevent the intrusion of the granular mineral material 4 and the generated carbides.
供給機６は、被処理物８や粉粒状鉱物質４を反
応容器１に送り込むためのもので、外気から反応
容器１内を遮断した状態でこれらを供給できるも
のであることが必要である。図示される実施例に
おける供給機６はスクリユーコンベアとなつてお
り、供給機６内を移動される被処理物８によつて
反応容器１内を外気から遮断するものとなつてい
る。また、この供給機６としては、油圧シリンダ
ーによつて被処理物８を反応容器１内へと押し出
すもの等であつてもよい。 The feeder 6 is for feeding the material to be treated 8 and the powdery mineral substance 4 into the reaction vessel 1, and needs to be able to feed these while the inside of the reaction vessel 1 is shut off from the outside air. The feeder 6 in the illustrated embodiment is a screw conveyor, and the workpiece 8 moved within the feeder 6 isolates the inside of the reaction vessel 1 from outside air. Further, the feeder 6 may be one that pushes the material to be treated 8 into the reaction container 1 using a hydraulic cylinder.
回転軸７には撹拌羽根９が取付けられていて回
転軸７によつて回転されるものとなつている。撹
拌羽根９は、回転軸７に対して、やや傾斜して取
付けられた細長い板状を成すもので、粉粒状鉱物
質４を撹拌して、供給された被処理物８を粉粒状
鉱物質４と混合しつつ移動させると共に、粉粒状
鉱物質４並びに被処理物８の均一な加熱を図るた
めのものである。また、粉粒状鉱物質４は、撹拌
羽根９による撹拌効率を良好に保つ上で、回転軸
７以下の投入高さにしておくことが好ましい。 A stirring blade 9 is attached to the rotating shaft 7 and is rotated by the rotating shaft 7. The stirring blade 9 has an elongated plate shape attached at a slight angle with respect to the rotating shaft 7, and stirs the powdery granular mineral material 4 to transform the supplied material to be treated 8 into the powdery granular mineral material 4. This is for the purpose of uniformly heating the powdery mineral substance 4 and the object to be treated 8 while moving the mineral substance while mixing with the mineral substance 4 . Furthermore, in order to maintain good stirring efficiency by the stirring blades 9, it is preferable that the powdered mineral substance 4 is placed at a height equal to or lower than the rotating shaft 7.
供給機６の対向側には排出シユーター１０が形
成されており、粉粒状鉱物質４と混合されて分解
反応に供された被処理物８の残渣である炭化物１
１が堰部１２を越えて落下されると、スクリユー
１３でこれを排出機１４へと送つて取出せるよう
になつている。この排出機１４も前述の供給機６
と同様なスクリユーコンベアで、その中を移動す
る炭化物１１によつて外気から反応容器１内を遮
断しつつ炭化物１１を排出するものである。ま
た、炭化物１１に混じつて排出される粉粒状鉱物
質４は、排出後分別して供給機６へと戻すように
すればよい。 A discharge shooter 10 is formed on the opposite side of the feeder 6, and the carbide 1, which is the residue of the treated material 8 that has been mixed with the powdery mineral material 4 and subjected to a decomposition reaction, is disposed of.
1 is dropped over the dam 12, a screw 13 sends it to a discharger 14 so that it can be taken out. This discharger 14 also has the above-mentioned feeder 6.
This screw conveyor is similar to the above, and discharges the carbide 11 while shielding the inside of the reaction vessel 1 from the outside air by the carbide 11 moving inside. Moreover, the powdery mineral substance 4 discharged together with the carbide 11 may be separated and returned to the feeder 6 after being discharged.
まず、供給機６によつて被処理物８を供給する
と、供給された被処理物８は、撹拌羽根９によつ
て加熱された粉粒状鉱物質４と混合されつつ徐々
に排出シユーター１０方向へ移動される。そし
て、加熱された粉粒状鉱物質４の熱によつて熱分
解反応し、炭化水素系のガスが生成される。 First, when the material to be treated 8 is supplied by the feeder 6, the supplied material to be treated 8 gradually moves toward the discharge shooter 10 while being mixed with the powdery mineral material 4 heated by the stirring blade 9. will be moved. Then, the heat of the heated powdery mineral substance 4 causes a thermal decomposition reaction, and a hydrocarbon gas is generated.
上記被処理物８の熱分解反応時の挙動は必ずし
も明確ではないが、本発明者は次のように推測し
ている。即ち、被処理物８が加熱された粉粒状鉱
物質４と接触して加熱されることにより、被処理
物８中の有機成分の炭素連鎖が切断されて底分子
化されると共に、炭素に結合している水素やその
他の原子が分離され、更に水素と炭素が優先的に
結合する再合成反応が成されているのではないか
と考えられる。また、被処理物８に水が含まれて
いる場合、高温下において活成化されると共に、
被処理物８が高温にさらされることによつて生ず
る炭素と反応して水性ガス化される。そして、こ
の被処理物８の熱分解時に、粉粒状鉱物質４が炭
素と水素の再合成を助ける触媒的役割をもなすの
ではないかと考えられる。 Although the behavior of the object to be treated 8 during the thermal decomposition reaction is not necessarily clear, the inventor of the present invention conjectures as follows. That is, when the material to be treated 8 comes into contact with the heated granular mineral material 4 and is heated, the carbon chains of the organic components in the material to be treated 8 are cut and converted into basic molecules, and at the same time, they are bonded to carbon. It is thought that a resynthesis reaction occurs in which hydrogen and other atoms are separated, and hydrogen and carbon are combined preferentially. Furthermore, when the material to be treated 8 contains water, it is activated at high temperatures and
When the object 8 to be treated is exposed to high temperatures, it reacts with carbon generated and is turned into water gas. It is also considered that during the thermal decomposition of the material to be treated 8, the particulate mineral material 4 may also play a catalytic role to aid in the resynthesis of carbon and hydrogen.
このようにして被処理物８は撹拌羽根９によつ
て粉粒状鉱物質４と混合されて熱分解反応され、
生成される炭化物１１は比重差によつて粉粒状鉱
物質４上に浮き上げられつつ堰部１２付近に集積
される。堰部１２付近に集積された炭化物１１
は、次第に押されて排出シユーター１０へと落下
し、スクリユー１３によつて掻き集められて排出
後１４へと送られ、排出されることになる。 In this way, the material to be treated 8 is mixed with the powdery mineral material 4 by the stirring blade 9 and undergoes a thermal decomposition reaction.
The generated carbide 11 is accumulated near the weir part 12 while floating on the powdery mineral material 4 due to the difference in specific gravity. Carbide 11 accumulated near the weir part 12
The particles are gradually pushed down and fall into the discharge shooter 10, where they are scraped up by the screw 13 and sent to the discharger 14, where they are discharged.
一方、被処理物８の熱分解反応によつて生成さ
れた発生ガスは、ガス抽出管５から反応容器１外
へと取り出され、前述のように、冷却器に導びか
れて冷却され、液化成分とガスとに分離されるも
のである。液化成分は炭化水素系の油と水とに大
別され、ガス成分は炭化水素系のガスや水性ガス
を含む可燃性ガスとして取得し得る。 On the other hand, the generated gas generated by the thermal decomposition reaction of the material to be treated 8 is taken out of the reaction vessel 1 from the gas extraction pipe 5, and as described above, is led to the cooler and cooled, and is liquefied. It is separated into components and gas. The liquefied component is broadly classified into hydrocarbon oil and water, and the gas component can be obtained as a combustible gas including hydrocarbon gas and water gas.
以上のような本発明に係る装置によれば、反応
容器１内にことさら燃焼ガスを送る必要がないの
で取得される油の汚染を防ぐことができ、底部よ
りの直接加熱を利用しているので熱効率に優れ、
かつ装置を小型化し得るものである。 According to the apparatus according to the present invention as described above, there is no need to send combustion gas into the reaction vessel 1, so contamination of the obtained oil can be prevented, and direct heating from the bottom is used. Excellent thermal efficiency,
Moreover, the device can be made smaller.
本発明で用いる粉粒状鉱物質としては、砂、粘
土、クレー等が最適である。また炭素と水素の再
合成時の触媒として機能し得ると考えられる酸化
鉄、ケイ酸、モリブテン、亜鉛、酸化アルミニウ
ム等を添加することも好ましいことである。 Sand, clay, clay, etc. are most suitable as the particulate mineral material used in the present invention. It is also preferable to add iron oxide, silicic acid, molybdenum, zinc, aluminum oxide, etc., which are considered to be able to function as catalysts during the resynthesis of carbon and hydrogen.
このように本発明においては、単に被処理物を
粉粒状鉱物質と接触させながら分解させるだけで
はなく、その分解残渣である炭化物の排出を連続
的に行うことができる。また、この炭化物は優先
的に排出され、炭化物と共に多量の粉粒状鉱物質
が排出されてしまうことがないので、粉粒状鉱物
質を無駄に消費することがない。従つて、粉粒状
鉱物質を用いた熱分解処理を、連続的にしかも経
済的に行えるものである。 As described above, in the present invention, not only can the material to be treated be decomposed while being brought into contact with the powdery mineral, but also the carbide that is the decomposition residue can be continuously discharged. Further, the carbide is preferentially discharged, and a large amount of granular mineral material is not discharged together with the carbide, so that the granular mineral material is not wasted. Therefore, the thermal decomposition treatment using granular mineral material can be carried out continuously and economically.
第１図は本発明に係る熱分解反応装置の縦断面
図、第２図はそのＡ−A′断面図である。
１：反応容器、２：バーナー、３：燃焼室、
４：粉粒状鉱物質、５：ガス抽出管、６：供給
機、７：回転軸、８：被処理物、９：撹拌羽根、
１０：排出シユーター、１１：炭化物、１２：堰
部、１３：スクリユー、１４：排出機。
FIG. 1 is a longitudinal cross-sectional view of a thermal decomposition reactor according to the present invention, and FIG. 2 is a cross-sectional view taken along line A-A'. 1: reaction vessel, 2: burner, 3: combustion chamber,
4: Powdered mineral substance, 5: Gas extraction pipe, 6: Supply machine, 7: Rotating shaft, 8: Processed object, 9: Stirring blade,
10: Discharge shooter, 11: Carbide, 12: Weir, 13: Screw, 14: Discharge machine.
Claims (1)
ら加熱を受ける反応容器と、 この反応容器の一側端部上方から、外気から反
応容器内を遮断した状態で被処理物を反応容器内
へ送り込む供給機と、 反応容器の他側端部の、粉粒状鉱物質の上面よ
りやや上方に開口された排出シユーターと、 反応容器の上部に開口された、発生ガスを取り
出すためのガス抽出管と、 供給機の設けられた反応容器の一側端部側から
排出シユーターの設けられた反応容器の他側端部
側へと被処理物を押しながら粉粒状鉱物質を撹拌
する撹拌羽根とを有することを特徴とする粉粒状
鉱物質を用いた熱分解反応装置。[Scope of Claims] 1. A reaction vessel in which a particulate mineral substance is placed and heated from at least the bottom surface, and a material to be treated is inserted from above one end of the reaction vessel with the inside of the reaction vessel being shut off from the outside air. A feeder for feeding into the reaction vessel, a discharge shooter at the other end of the reaction vessel that opens slightly above the top surface of the granular mineral, and an opening at the top of the reaction vessel for taking out generated gas. Stirring to stir the powdery mineral material while pushing the material to be treated from one end of the reaction vessel equipped with a gas extraction pipe and a feeder to the other end of the reaction vessel equipped with a discharge shooter. A pyrolysis reaction device using a powdery mineral substance, characterized by having a blade.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58007371A JPS59132933A (en) | 1983-01-21 | 1983-01-21 | Thermally decomposing reaction apparatus using particulate ore substance |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58007371A JPS59132933A (en) | 1983-01-21 | 1983-01-21 | Thermally decomposing reaction apparatus using particulate ore substance |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59132933A JPS59132933A (en) | 1984-07-31 |
| JPS634447B2 true JPS634447B2 (en) | 1988-01-29 |
Family
ID=11664108
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58007371A Granted JPS59132933A (en) | 1983-01-21 | 1983-01-21 | Thermally decomposing reaction apparatus using particulate ore substance |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59132933A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU2002951194A0 (en) * | 2002-09-04 | 2002-10-03 | Environmental Solutions International Ltd | Conversion of sludges and carbonaceous materials |
| JP3836112B2 (en) * | 2004-03-23 | 2006-10-18 | 株式会社御池鐵工所 | Waste plastic oil production facility |
-
1983
- 1983-01-21 JP JP58007371A patent/JPS59132933A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59132933A (en) | 1984-07-31 |
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