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JPS621638B2 - - Google Patents
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JPS621638B2 - - Google Patents

Info

Publication number
JPS621638B2
JPS621638B2 JP55069195A JP6919580A JPS621638B2 JP S621638 B2 JPS621638 B2 JP S621638B2 JP 55069195 A JP55069195 A JP 55069195A JP 6919580 A JP6919580 A JP 6919580A JP S621638 B2 JPS621638 B2 JP S621638B2
Authority
JP
Japan
Prior art keywords
container
plastic waste
wire mesh
mesh cage
furnace
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
Application number
JP55069195A
Other languages
Japanese (ja)
Other versions
JPS56166290A (en
Inventor
Kinji Ito
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP6919580A priority Critical patent/JPS56166290A/en
Publication of JPS56166290A publication Critical patent/JPS56166290A/en
Publication of JPS621638B2 publication Critical patent/JPS621638B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock
    • Y02P20/143Feedstock the feedstock being recycled material, e.g. plastics

Landscapes

  • Gasification And Melting Of Waste (AREA)
  • Coke Industry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

【発明の詳細な説明】 本発明はプラスチツク廃棄物を加熱分解し油と
ガスとに分離するようにして処理するプラスチツ
ク廃棄物の処理装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a plastic waste treatment apparatus for treating plastic waste by thermally decomposing it and separating it into oil and gas.

従来、プラスチツク廃棄物を加熱分解して蒸気
化させ、この蒸気を凝縮液化させて油とガスとを
回収する手段、あるいはプラスチツク廃棄物を加
熱溶融させ、無分解反応炉に送り込み分解と乾溜
とを同時に行つて液化させる手段等がある。
Conventionally, plastic waste is thermally decomposed and vaporized, and this vapor is condensed and liquefied to recover oil and gas, or plastic waste is heated and melted and sent to a non-decomposition reactor to undergo decomposition and dry distillation. There are means to liquefy the liquid at the same time.

然して、これらの手段に用いる装置は大型であ
り、特に熱分解炉の構造、機能、保守、耐久度等
に問題があつた。
However, the equipment used for these means is large-sized, and there have been problems, particularly with respect to the structure, function, maintenance, durability, etc. of the pyrolysis furnace.

本発明はプラスチツク廃棄物を加熱溶融して塊
状体とし、次いでかかる塊状体を熱分解炉に装入
して蒸気化させ、この蒸気を冷却して凝縮液化さ
せ油とガスを分離させるようにした処理装置にお
いて、特に独特な熱分解炉を備えることを特徴と
したものであり、上端を開口した金網製篭状物を
容体に内設し、前記金網製篭状物と容体の内周壁
および内底壁との間に荒目砂、珪燥土、活性炭、
酸化鉄等を充填して容体の内周および内底に所要
厚さの間接伝熱域を形成してなる収容器を備えた
熱分解炉を設け、溶融固化したプラスチツク廃棄
物の塊状体を前記収容器内に装入し加熱分解して
蒸気化させたのち凝縮液化させて油とガスとに分
離するようにしたことを特徴とするプラスチツク
廃棄物の処理装置である。
The present invention heats and melts plastic waste to form a lump, then charges the lump into a pyrolysis furnace to vaporize it, and cools the vapor to condense and liquefy it to separate oil and gas. This processing equipment is characterized by being equipped with a particularly unique pyrolysis furnace, in which a wire mesh cage-like object with an open upper end is installed inside the container, and the wire mesh cage-like object and the inner circumferential wall of the container and the inner surface of the container are connected. Coarse sand, siliceous soil, activated carbon,
A pyrolysis furnace equipped with a container filled with iron oxide, etc. to form an indirect heat transfer zone of a required thickness on the inner periphery and inner bottom of the container is installed, and the melted and solidified lumps of plastic waste are This is a processing apparatus for plastic waste characterized in that it is charged into a container, thermally decomposed and vaporized, and then condensed and liquefied to separate oil and gas.

本発明装置の実施例を図面について説明すれ
ば、先づプラスチツク廃棄物イを加熱し溶融させ
る加熱炉1と、加熱炉1において加熱され溶融さ
れたのち塊状体ロとなつたものを蒸気化させる熱
分解炉2と、この熱分解炉2によつて生成された
蒸気を冷却し凝縮液化させるための冷却槽3と、
この冷却槽3内の冷媒によつて凝縮液化した油を
貯溜する油タンク4と、分離したガスを貯えるガ
スタンク5とを有し、熱分解炉2と冷却槽3とを
導管6で連結するとともに導管6の途中にストツ
プバルブ7、微粒子除去装置8、フアン装置9を
介在させ、冷却槽3と油タンク4とを導管10で
連結し、さらに油タンク4とガスタンク5とを導
管11で連結してある。
An embodiment of the apparatus of the present invention will be described with reference to the drawings. First, there is a heating furnace 1 that heats and melts plastic waste (a), and that vaporizes the material that has been heated and melted in the heating furnace (1) and turned into a lump (b). a pyrolysis furnace 2; a cooling tank 3 for cooling and condensing the steam generated by the pyrolysis furnace 2;
It has an oil tank 4 that stores oil condensed and liquefied by the refrigerant in this cooling tank 3, and a gas tank 5 that stores separated gas, and connects the pyrolysis furnace 2 and the cooling tank 3 with a conduit 6. A stop valve 7, a particulate removal device 8, and a fan device 9 are interposed in the middle of the conduit 6, the cooling tank 3 and the oil tank 4 are connected by a conduit 10, and the oil tank 4 and the gas tank 5 are connected by a conduit 11. be.

加熱炉1は第3図示のように、上部一側に投入
口12を有し、この投入口12には開閉自在な扉
体13を備え、炉体14の外周および外底を繞り
炎道15を有し、下部一側に焚口16を備え、炉
体14の底部に連なり開閉自在な遮閉板17を備
えた取出路18を設けてあり、架構19に懸吊し
たホイスト20により上下自在とした撹拌機構2
1を炉体14内に下降させ作動させるようにして
ある。
As shown in the third figure, the heating furnace 1 has an inlet 12 on one side of the upper part, and the inlet 12 is equipped with a door body 13 that can be opened and closed, and a flame path that extends around the outer periphery and outer bottom of the furnace body 14. 15, a firing port 16 is provided on one side of the lower part, and an outlet passage 18 is provided that is connected to the bottom of the furnace body 14 and is equipped with a shielding plate 17 that can be opened and closed, and can be freely raised and lowered by a hoist 20 suspended from a frame 19. Stirring mechanism 2
1 is lowered into the furnace body 14 and operated.

熱分解炉2は第1図、第2図および第4図に示
すように、上部に開口22を有する角形の炉壁2
3の内側に、上端を開放した装入口24の周縁を
前記開口22に止着した有底囲繞体25を設け、
この有底囲繞体25の内部空間に四個の収容器2
6,26,26,26を設定自在としており、下
部一側に焚口27を設け、前記有底囲繞体25の
外周と炉壁23内面との間の空隙を炎道28と
し、この炎道28を煙突29に連通させてあり、
前記有底囲繞体25の装入口24に着脱自在な蓋
体30を備え、かつ各々の収容器26を隔離する
とともに中間にも充分な空間を有する炎道31を
形成してある。
As shown in FIGS. 1, 2, and 4, the pyrolysis furnace 2 has a rectangular furnace wall 2 with an opening 22 at the top.
3 is provided with a bottomed enclosure body 25 in which the periphery of the charging port 24 whose upper end is open is fixed to the opening 22,
Four containers 2 are placed in the inner space of this bottomed enclosure 25.
6, 26, 26, 26 can be freely set, a combustion port 27 is provided on one side of the lower part, and a flame path 28 is defined as a gap between the outer periphery of the bottomed enclosure 25 and the inner surface of the furnace wall 23. is connected to the chimney 29,
A removable lid 30 is provided on the charging port 24 of the bottomed enclosure 25, and a flame path 31 is formed which isolates each container 26 and has a sufficient space in the middle.

この場合、前記導管6を三本とし、これら導管
6,6,6の端部を、炉壁23を通り有底囲繞体
25の上部一側に連結し開口させてある。
In this case, there are three conduits 6, and the ends of these conduits 6, 6, 6 are connected to one side of the upper part of the bottomed enclosure 25 through the furnace wall 23 and opened.

前記収容器26は第5図乃至第7図に示すよう
に上部を開口した金網製篭状物32を剛性容体3
3に内設する。この場合、金網製篭状物32を比
較的目の荒いものとしたので外周および外底に
100メツシユ程度の比較的目の細かい別の金網3
4を添着してある。
As shown in FIGS. 5 to 7, the container 26 is a rigid container 3 made of a wire mesh cage-like object 32 with an open top.
Installed in 3. In this case, since the wire mesh cage-like object 32 is made relatively coarse, the outer periphery and outer bottom are
Another relatively fine wire mesh of about 100 mesh 3
4 is attached.

このようにして外側に目の細かい金網34を添
着して金網製篭状物32とし、容体32の内底面
に荒目砂、珪燥土、活性炭、酸化鉄等を所要厚さ
に載積させて層状としたのち、金網34を添着し
た金網製篭状物32を容体33内に嵌入させ、外
底を前記層状上に載せ、次いで容体33の内周面
33aと金網製篭状物32の外周との間に荒目
砂、珪燥土、活性炭、酸化鉄等を充填して所要厚
さの周層状とする。
In this way, a fine wire mesh 34 is attached to the outside to form a wire mesh cage-like object 32, and coarse sand, siliceous earth, activated carbon, iron oxide, etc. are piled on the inner bottom surface of the container 32 to a required thickness. After that, the wire mesh cage 32 to which the wire mesh 34 is attached is fitted into the container 33, the outer bottom is placed on the layer, and then the inner circumferential surface 33a of the container 33 and the wire mesh cage 32 are separated. Coarse sand, siliceous earth, activated carbon, iron oxide, etc. are filled between the outer circumference and the outer circumference to form a circumferential layer of the required thickness.

この場合、金網製篭状物32に添着した目の細
かい金網34は荒目砂等が金網製篭状物32内に
侵入するのを防止するものである。
In this case, the fine wire mesh 34 attached to the wire mesh cage 32 prevents coarse sand and the like from entering the wire mesh cage 32.

かくして、収容器26は容体33の内周壁およ
び内底壁と金網製篭状物32との間に荒目砂、珪
燥土、活性炭、酸化鉄等を充填して容体33の内
周および内底に所要厚さの間接伝熱域35を形成
してある。
Thus, the container 26 is constructed by filling coarse sand, siliceous earth, activated carbon, iron oxide, etc. between the inner circumferential wall and inner bottom wall of the container 33 and the wire mesh cage 32. An indirect heat transfer region 35 of a required thickness is formed at the bottom.

前記有底囲繞体25内に設定した収容器26,
26,26,26の各々上端26aは導管6,
6,6の開口より僅か下位としてある。
a container 26 set within the bottomed enclosure 25;
Each upper end 26a of 26, 26, 26 is connected to the conduit 6,
It is set slightly lower than the opening of 6,6.

この場合、熱分解炉2から蒸気を導出する導管
6を三本としたから、これに対応して冷却槽3内
の冷却管36を三本としてあり、導管6,6,6
にはそれぞれストツプバルブ7、微粉子除去装置
8、フアン装置9を介在させてある。
In this case, since there are three conduits 6 for leading out steam from the pyrolysis furnace 2, there are correspondingly three cooling pipes 36 in the cooling tank 3, and the conduits 6, 6, 6
A stop valve 7, a particulate removal device 8, and a fan device 9 are interposed in each.

また、冷却槽3は角形とし、冷却管36,3
6,36は、各々上下方向に蛇行状とし、冷却管
36の上部始端を導入端36aとし、下部終端を
導出端36bとしてある。
In addition, the cooling tank 3 is square, and the cooling pipes 36, 3
6 and 36 each have a meandering shape in the vertical direction, and the upper starting end of the cooling pipe 36 is an inlet end 36a, and the lower end is an outlet end 36b.

前記冷却管36の導出端36bにそれぞれ一端
を連結した導管10,10,10の他端は油タン
ク4に連結してあり、油タンク4にはレベル計3
7およびドレンコツク38を備える。
The other ends of the conduits 10, 10, 10 each having one end connected to the outlet end 36b of the cooling pipe 36 are connected to the oil tank 4, and the oil tank 4 is equipped with a level meter 3.
7 and a drain kettle 38.

油タンク4およびガスタンク5は密閉状として
あり、油タンク4、ガスタンク5の適宜部位には
それぞれ取出口(図示しない)を有する。
The oil tank 4 and the gas tank 5 are sealed, and each has an outlet (not shown) at an appropriate location.

本発明装置は前記のように構成するから、プラ
スチツク廃棄物イを加熱炉1に入れ、加熱溶融さ
せたのち取出路18を経て炉外に取出し、放置し
て適宜大きさの数個の塊状体ロ,ロ……とする。
Since the apparatus of the present invention is constructed as described above, the plastic waste A is put into the heating furnace 1, heated and melted, and then taken out of the furnace through the take-out passage 18, and left to form several lumps of appropriate size. B, B...

かかる塊状体ロ,ロ……を熱分解炉2内に設定
した収容器26,26,26,26にそれぞれ装
入する。
These lumps B, B, etc. are charged into containers 26, 26, 26, 26 set in the pyrolysis furnace 2, respectively.

即ち、蓋体30を取外し、収容器26の上端よ
り金網製篭状物32内に塊状体ロを入れ、蓋体3
0を取付けて有底囲繞体25を密閉状としたの
ち、焚口27にて燃料を燃焼させると、熱気は有
底囲繞体25の外周、外底、中間の炎道31を通
る。かかる熱気により有底囲繞体25内に設定し
た各収容器26も加熱され、各収容器26におい
ては容体33に形成した間接伝熱域35を介して
金網製篭状物32内の塊状体ロを加熱する。
That is, the lid 30 is removed, the lump 2 is put into the wire mesh cage 32 from the upper end of the container 26, and the lid 3 is removed.
0 is attached to make the bottomed enclosure 25 airtight, and when fuel is burned at the combustion port 27, hot air passes through the outer periphery, the outer bottom, and the intermediate flame path 31 of the bottomed enclosure 25. Each container 26 set in the bottomed enclosure 25 is also heated by this hot air, and in each container 26, the lumps inside the wire mesh cage 32 are heated through the indirect heat transfer region 35 formed in the container 33. heat up.

やがて、塊状体ロが徐々に気化温度になり蒸気
化すると、かかる蒸気は導管6,6,6内に吸引
され、冷却管36,36,36へ導かれる。冷却
管36内の蒸気は冷却槽3内の冷却液によつて
徐々に凝縮し液化して導出端36bより油タンク
4内へ流入する。
When the mass body gradually reaches the vaporization temperature and becomes vaporized, the vapor is drawn into the conduits 6, 6, 6 and guided to the cooling pipes 36, 36, 36. The steam in the cooling pipe 36 is gradually condensed and liquefied by the cooling liquid in the cooling tank 3, and flows into the oil tank 4 from the outlet end 36b.

この場合、油タンク4内の上部にあるガスは導
管11を経てガスタンク5へ入る。
In this case, the gas present in the upper part of the oil tank 4 enters the gas tank 5 via the conduit 11.

かくして、熱分解炉2内に設定した収容器26
に装入させた塊状体ロ、即ちプラスチツク廃棄物
を加熱溶融したのち固化させた塊状体ロは有底囲
繞体25、容体33、間接伝熱域35を介して伝
播熱によつて加熱された金網製篭状物32内雰囲
気により徐々に加熱され、塊状体ロは全体的かつ
平均的に加熱されるので蒸気化は極めて良好であ
る。
Thus, the container 26 set inside the pyrolysis furnace 2
The agglomerates charged into the container, that is, the agglomerates made by heating and melting the plastic waste and then solidifying them, were heated by propagated heat through the bottomed enclosure 25, the container 33, and the indirect heat transfer zone 35. The atmosphere inside the wire mesh cage 32 gradually heats the mass, and the mass is heated as a whole and evenly, so that the vaporization is extremely good.

換言すれば、塊状体ロは加熱雰囲気で熱を加え
られ、恰も蒸し蒸すようにして熱を加えられるの
で蒸気化される状態は極めて好ましい状態とな
る。
In other words, heat is applied to the lump material B in a heating atmosphere, and the heat is applied in a manner similar to steaming, so that the state of vaporization is extremely favorable.

本発明装置はプラスチツク廃棄物をを燃焼させ
ることなく、蒸し蒸すようにして加熱し蒸気化す
るから有毒ガスを発生せしめることなく、また容
体に蒸気が直接接触することなくして熱分解炉の
耐久性を大とする。
The device of the present invention heats and vaporizes plastic waste in a steaming manner without burning it, so it does not generate toxic gases and does not directly contact the container with steam, thereby increasing the durability of the pyrolysis furnace. be large.

塩化ビニル、ポリエチレン、ポリプロピレン等
のプラスチツク廃棄物を加熱炉において、80℃乃
至100℃で加熱溶融させ、取出して自然放置し重
量10Kgの塊状体としたのち、熱分解炉にて凡そ
130℃に加熱して蒸気化し、かかる蒸気を冷却管
を介して凝縮液化させたところ、約6の油と、
2.5Kgのガスとを回収することができ、残滓物は
1.5Kgであつた。
Plastic waste such as vinyl chloride, polyethylene, and polypropylene is heated and melted at 80 to 100 degrees Celsius in a heating furnace, taken out and left to stand naturally to form a lump of 10 kg in weight, and then processed into a pyrolysis furnace.
When heated to 130°C to vaporize and condensate the vapor through a cooling pipe, approximately 6 oil and
2.5Kg of gas can be recovered, and the residue is
It was 1.5Kg.

本発明はプラスチツク廃棄物の処理装置として
比較的小型化し得るとともに熱分解炉の構造の簡
素化をもたらし耐久性に秀れ、回収した油、ガス
を燃料等となし得て、プラスチツク廃棄物による
公害問題解決の手段としてその効果は大である。
The present invention can be made relatively compact as a plastic waste processing device, has a simplified structure of the pyrolysis furnace, has excellent durability, and can use recovered oil and gas as fuel, thereby reducing pollution caused by plastic waste. It is highly effective as a means of problem solving.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明装置の全体側面図であつて要部
を断面してある。第2図は同平面図であつて、要
部を断面してある。第3図は加熱炉の正面図、第
4図は第2図の−線相当部分から視た熱分解
炉の断面図、第5図は収容器の正面図、第6図は
同・側面図、第7図は同平面図である。 1……加熱炉、2……熱分解炉、3……冷却
槽、4……油タンク、5……ガスタンク、6,1
0,11……導管、23……炉壁、25……有底
囲繞体、26……収容器、30……蓋体、32…
…金網製篭状物、33……容体、35……間接伝
熱域、36……冷却管、イ……プラスチツク廃棄
物、ロ……塊状体。
FIG. 1 is an overall side view of the apparatus of the present invention, with main parts cut away. FIG. 2 is a plan view of the same, with main parts cut away. Figure 3 is a front view of the heating furnace, Figure 4 is a sectional view of the pyrolysis furnace seen from the part corresponding to the - line in Figure 2, Figure 5 is a front view of the container, and Figure 6 is a side view of the same. , FIG. 7 is a plan view of the same. 1...Heating furnace, 2...Pyrolysis furnace, 3...Cooling tank, 4...Oil tank, 5...Gas tank, 6,1
0, 11... Conduit, 23... Furnace wall, 25... Bottomed enclosure, 26... Container, 30... Lid, 32...
...Wire mesh cage, 33...Container, 35...Indirect heat transfer area, 36...Cooling pipe, A...Plastic waste, B...Lump.

Claims (1)

【特許請求の範囲】[Claims] 1 上端を開口した金網製篭状物を容体に内設
し、前記金網製篭状物と容体の内周壁および内底
壁との間に荒目砂、珪燥土、活性炭、酸化鉄等を
充填して容体の内周および内底に所要厚さの間接
伝熱域を形成してなる収容器を備えた熱分解炉を
設け、溶融固化したプラスチツク廃棄物の塊状体
を、前記収容器内に装入し加熱分解して蒸気化さ
せたのち凝縮液化させて油とガスとに分離するよ
うにしたことを特徴とするプラスチツク廃棄物の
処理装置。
1. A wire mesh cage-like object with an open top end is placed inside the container, and coarse sand, siliceous earth, activated carbon, iron oxide, etc. are placed between the wire mesh cage-like object and the inner peripheral wall and inner bottom wall of the container. A pyrolysis furnace is equipped with a container that is filled to form an indirect heat transfer zone of a required thickness on the inner periphery and bottom of the container, and a lump of melted and solidified plastic waste is placed inside the container. 1. An apparatus for processing plastic waste, characterized in that the plastic waste is charged into a container, heated and decomposed, vaporized, and then condensed and liquefied to separate oil and gas.
JP6919580A 1980-05-24 1980-05-24 Treating apparatus of plastic waste Granted JPS56166290A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6919580A JPS56166290A (en) 1980-05-24 1980-05-24 Treating apparatus of plastic waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6919580A JPS56166290A (en) 1980-05-24 1980-05-24 Treating apparatus of plastic waste

Publications (2)

Publication Number Publication Date
JPS56166290A JPS56166290A (en) 1981-12-21
JPS621638B2 true JPS621638B2 (en) 1987-01-14

Family

ID=13395696

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6919580A Granted JPS56166290A (en) 1980-05-24 1980-05-24 Treating apparatus of plastic waste

Country Status (1)

Country Link
JP (1) JPS56166290A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59124831U (en) * 1983-02-04 1984-08-22 藤森 実 combustion furnace

Also Published As

Publication number Publication date
JPS56166290A (en) 1981-12-21

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