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JP4434305B2 - Plastic decomposition apparatus and cleaning method thereof - Google Patents
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JP4434305B2 - Plastic decomposition apparatus and cleaning method thereof - Google Patents

Plastic decomposition apparatus and cleaning method thereof Download PDF

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JP4434305B2
JP4434305B2 JP2009044020A JP2009044020A JP4434305B2 JP 4434305 B2 JP4434305 B2 JP 4434305B2 JP 2009044020 A JP2009044020 A JP 2009044020A JP 2009044020 A JP2009044020 A JP 2009044020A JP 4434305 B2 JP4434305 B2 JP 4434305B2
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cleaning liquid
decomposition tank
decomposition
cleaning
plastic
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JP2009227983A (en
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伸 真継
敏博 宮崎
宏 矢野
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Panasonic Corp
Panasonic Electric Works Co Ltd
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Matsushita Electric Works Ltd
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    • 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
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/54Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

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  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Description

本発明は、プラスチックの分解装置とその洗浄方法に関するものである。 The present invention relates to a plastic decomposing apparatus and a cleaning method thereof .

従来より、FRP(繊維強化プラスチック)に代表されるプラスチック成形品中の無機有価物及び有機有価物を回収して再利用できるようにするために、超臨界又は亜臨界状態の水熱反応によって分解する方法(例えば、特許文献1参照)が提案されている。   Conventionally, in order to recover and reuse inorganic and organic valuables in plastic molded products represented by FRP (fiber reinforced plastics), they are decomposed by a supercritical or subcritical hydrothermal reaction. A method (for example, see Patent Document 1) has been proposed.

このような方法は、一般的には、耐圧性の分解槽にFRP及び溶媒となる水を投入し、これを超臨界又は亜臨界状態で分解した後、分解槽から分解液を排出して回収している。ここで、分解槽内での分解率向上と分解液の排出性等の観点から、FRPを前処理として2〜20mm程度の大きさに粉砕して分解槽に投入している。FRPとともに投入される水と事前混合して投入してもよいが別途混合槽が必要になるため、経済性の観点から、分解槽に接続された原料供給管路より分解槽に直接、FRPを投入することが行われている。   In such a method, in general, FRP and water as a solvent are put into a pressure-resistant decomposition tank, and after decomposition in a supercritical or subcritical state, the decomposition liquid is discharged from the decomposition tank and recovered. is doing. Here, from the viewpoint of improving the decomposition rate in the decomposition tank and discharging the decomposition solution, FRP is pulverized into a size of about 2 to 20 mm as a pretreatment and put into the decomposition tank. FRP may be pre-mixed with water added together with FRP, but a separate mixing tank is required. Therefore, from the viewpoint of economy, the FRP is directly applied to the decomposition tank from the raw material supply line connected to the decomposition tank. It has been done.

しかしながら、FRPには一般に、無機物としてガラス繊維などの無機繊維の他に、炭酸カルシウムや水酸化アルミニウムなどの無機粉体が含有されており、これを分解槽で攪拌しながら亜臨界水又は超臨界水で分解処理を行うと、分解槽の内壁、特に喫水面に無機物を主成分とする固形分が付着して加熱性能が低下し、次バッチにおいて分解効率が低下するという問題があった。また、分解槽の排出管路においても、無機物を主成分とする固形分が付着して閉塞が生じるという問題があった。   However, FRP generally contains inorganic powder such as calcium carbonate and aluminum hydroxide in addition to inorganic fiber such as glass fiber as an inorganic substance, and is subcritical water or supercritical while stirring this in a decomposition tank. When the decomposition treatment is performed with water, there is a problem that the solid content mainly composed of inorganic substances adheres to the inner wall of the decomposition tank, particularly the draft surface, the heating performance is lowered, and the decomposition efficiency is lowered in the next batch. In addition, there is a problem in that the solid content mainly composed of an inorganic substance adheres to the discharge pipe of the decomposition tank, causing clogging.

国際公開第2004/041917号パンフレットInternational Publication No. 2004/041917 Pamphlet

本発明は、上記のとおりの背景から、従来の問題点を解消し、分解槽及び排出管路内に付着した固形分を容易にかつ確実に洗浄除去することができるプラスチックの分解装置とその洗浄方法を提供することを課題としている。 In view of the above background, the present invention eliminates the conventional problems, and easily and reliably removes the solid content adhering to the decomposition tank and the discharge pipe, and its cleaning. The challenge is to provide a method .

本発明は以下のことを特徴としている。   The present invention is characterized by the following.

第1には、プラスチックを超臨界又は亜臨界の状態で溶媒にて分解する分解槽を備え、この分解槽にプラスチックを供給する原料供給管路と、前記分解槽で分解されたプラスチックの分解液を取り出す排出管路と、排出管路に開閉弁が形成されている分解装置で開閉弁を閉止した状態でプラスチックを分解処理し、次いで開閉弁を開放して分解槽から分解液を取り出した後、前記分解槽に洗浄液を供給して分解槽及び排出管路を洗浄する方法であって、分解槽から分解液を取り出した後、開閉弁を閉止状態にして分解槽に洗浄液を供給し、分解槽内に洗浄液を貯留しつつその洗浄液で分解槽内部を洗浄し、次いで、分解槽の内圧が大気圧を超える圧力になるまで分解槽に空気を供給した後、開閉弁を開き、その分解槽の内圧によって分解槽内の洗浄液を排出管路に排出して排出管路内部を洗浄することを特徴とする。
第2には、原料供給管路から洗浄液を分解槽に供給することを特徴とし、第3には、分解槽の安全弁の2次側から洗浄液を分解槽に供給することを特徴とする。また、第4には、分解槽の内圧によって分解槽内の洗浄液を排出管路に排出する前に、分解槽に加えてさらに排出管路にも洗浄液を供給して排出管路内に洗浄液を予め貯留しておくことを特徴とし、第5には、排出管路の下流側から上流側に向かって洗浄液を供給して排出管路内に洗浄液を貯留する。そして、第6には、分解槽への空気の供給は、分解槽の内圧が150〜500kPaの範囲の圧力になるまで行われることを特徴とする。
First, a decomposition tank that decomposes plastic with a solvent in a supercritical or subcritical state is provided, a raw material supply pipe that supplies the plastic to the decomposition tank, and a plastic decomposition solution decomposed in the decomposition tank After disassembling the plastic in a state where the open / close valve is closed with a discharge pipe that takes out the discharge pipe and the open / close valve in the discharge pipe , and then opening the open / close valve and taking out the decomposition solution from the decomposition tank The cleaning liquid is supplied to the decomposition tank to clean the decomposition tank and the discharge pipe. After the decomposition liquid is taken out from the decomposition tank, the on-off valve is closed and the cleaning liquid is supplied to the decomposition tank. Washing the inside of the decomposition tank with the cleaning liquid while storing the cleaning liquid in the tank, and then supplying air to the decomposition tank until the internal pressure of the decomposition tank exceeds the atmospheric pressure, then opening the on-off valve and opening the decomposition tank In the decomposition tank by the internal pressure of Characterized by washing the internal discharge line to discharge the cleaning liquid discharge line.
Second, the cleaning liquid is supplied to the decomposition tank from the raw material supply line, and third, the cleaning liquid is supplied to the decomposition tank from the secondary side of the safety valve of the decomposition tank. Fourth, before the cleaning liquid in the decomposition tank is discharged to the discharge pipe by the internal pressure of the decomposition tank, the cleaning liquid is further supplied to the discharge pipe in addition to the decomposition tank. Fifth, the cleaning liquid is supplied from the downstream side to the upstream side of the discharge pipe, and the cleaning liquid is stored in the discharge pipe. Sixthly, the supply of air to the decomposition tank is performed until the internal pressure of the decomposition tank reaches a pressure in the range of 150 to 500 kPa.

第7には、プラスチックを超臨界又は亜臨界の状態で溶媒にて分解する分解槽を備え、この分解槽にプラスチックを供給する原料供給管路と、前記分解槽で分解されたプラスチックの分解液を取り出す排出管路が形成されているプラスチックの分解装置において、分解槽内部及び排出管路内部を洗浄液で洗浄する洗浄装置と、分解槽内の洗浄液量を検出する洗浄液検出手段と、分解槽内の内圧を検出する圧力検出手段と、排出管路への洗浄液の流入を制御する手段とを備え、前記洗浄装置は、洗浄液を分解槽に供給する第1の洗浄液供給手段と空気を分解槽に供給する空気供給手段とを有し、第1の洗浄液供給手段は、洗浄液検出手段で検出される洗浄液量に基づいて所定量の洗浄液を供給するものであり、空気供給手段は、分解槽内に所定量の洗浄液が供給されている状態で、圧力検出手段で検出される分解槽内の内圧に基づいて分解槽内の内圧が大気圧を超える圧力になるように空気を供給するものであり、排出管路への洗浄液の流入を制御する手段は、排出管路に設けられた開閉弁が、分解槽内に所定量の洗浄液が供給されている状態において分解槽内の内圧が大気圧を超える圧力になるように空気供給手段から分解槽への空気の供給中は閉状態とされ、分解槽内の内圧が大気圧を超える圧力に達した後は開状態とされて分解槽内の加圧された洗浄液が排出管路に排出されるように制御されることを特徴とする。 Seventh, a decomposition tank for decomposing plastic in a supercritical or subcritical state with a solvent is provided, a raw material supply pipe for supplying the plastic to the decomposition tank, and a plastic decomposition solution decomposed in the decomposition tank In a plastic decomposing apparatus in which a discharge pipe is formed, a cleaning apparatus for cleaning the inside of the decomposition tank and the inside of the discharge pipe with the cleaning liquid, a cleaning liquid detecting means for detecting the amount of the cleaning liquid in the decomposition tank, and the decomposition tank A pressure detecting means for detecting the internal pressure of the liquid and a means for controlling the inflow of the cleaning liquid into the discharge pipe, wherein the cleaning device includes a first cleaning liquid supply means for supplying the cleaning liquid to the decomposition tank and air to the decomposition tank. An air supply means for supplying, and the first cleaning liquid supply means supplies a predetermined amount of cleaning liquid based on the amount of cleaning liquid detected by the cleaning liquid detection means, and the air supply means is provided in the decomposition tank. Predetermined In a state where the cleaning liquid is being supplied, which pressure decomposition tank based on the internal pressure in the decomposition vessel detected by the pressure detecting means to supply air to a pressure above atmospheric pressure, the discharge pipe The means for controlling the inflow of the cleaning liquid into the passage is such that the on-off valve provided in the discharge pipe causes the internal pressure in the decomposition tank to exceed the atmospheric pressure in a state where a predetermined amount of cleaning liquid is supplied into the decomposition tank. The air supply means is closed during the supply of air to the decomposition tank, and after the internal pressure in the decomposition tank reaches a pressure exceeding the atmospheric pressure , it is opened and the decomposition tank is pressurized. Control is performed such that the cleaning liquid is discharged to the discharge pipe.

には、第の発明において、洗浄装置における第1の洗浄液供給手段の洗浄液供給口が、原料供給管路に設けられていることを特徴とする。 Eighth , in the seventh invention, the cleaning liquid supply port of the first cleaning liquid supply means in the cleaning apparatus is provided in the raw material supply pipe.

には、第の発明において、洗浄装置における第1の洗浄液供給手段の洗浄液供給口が、分解槽の安全弁の2次側に設けられていることを特徴とする。 Eighth , in the seventh invention, the cleaning liquid supply port of the first cleaning liquid supply means in the cleaning device is provided on the secondary side of the safety valve of the decomposition tank.

には、第の発明において、洗浄装置における第1の洗浄液供給手段の洗浄液供給口から分解槽内に延びる配管の先端に噴射ノズルが設けられ、分解槽内部の特定部位を洗浄液の噴射によって洗浄することを特徴とする。 Ninth , in the seventh invention, an injection nozzle is provided at the tip of a pipe extending into the decomposition tank from the cleaning liquid supply port of the first cleaning liquid supply means in the cleaning device, and the cleaning liquid is injected to a specific part inside the decomposition tank. It is characterized by washing by.

11には、第の発明から第10の発明のいずれかの発明において、排出管路の出口側に排液貯槽を有し、分解槽から排出された洗浄液を再利用可能に貯留していることを特徴とする。 Eleventh , in any one of the seventh to tenth aspects of the invention, it has a drainage storage tank on the outlet side of the discharge pipe, and stores the cleaning liquid discharged from the decomposition tank so that it can be reused. It is characterized by being.

12には、第11の発明において、分解槽の後段に分解液から固形分を分離する固形分分離装置を有し、排液貯槽に貯留された洗浄液を、該固形分分離装置に通水し、固形分を洗浄液中から分離し、固形分が除去された洗浄液を、溶媒や洗浄液として再利用可能にしていることを特徴とする。 The first 12, water flow in the eleventh invention, had a solids separation device for separating solids from decomposition solution downstream of the decomposition tank, the cleaning liquid stored in the waste solution storage tank, the solid content separation device Then, the solid content is separated from the cleaning liquid, and the cleaning liquid from which the solid content has been removed is made reusable as a solvent or a cleaning liquid .

第13には、第7から第12のいずれかの発明において、さらに、洗浄装置は、洗浄液を排出管路に供給する第2の洗浄液供給手段を備えており、第2の洗浄液供給手段は、排出管路の容積に応じた所定量の洗浄液を供給するものであり、前記排出管路への洗浄液の流入を制御する手段は、開閉弁が、分解槽内に所定量の洗浄液が供給されている状態において空気供給手段からの空気の供給により分解槽内の内圧が大気圧を超える圧力に達し、かつ、第2の洗浄液供給手段から排出管路に所定量の洗浄液が供給された後に開状態とされて、排出管路内の洗浄液が分解槽内の加圧された洗浄液により排出されるように制御されることを特徴とする。 In a thirteenth aspect, in any one of the seventh to twelfth inventions, the cleaning device further includes a second cleaning liquid supply unit that supplies the cleaning liquid to the discharge conduit, and the second cleaning liquid supply unit includes: Supplying a predetermined amount of cleaning liquid according to the volume of the discharge pipe, and the means for controlling the flow of the cleaning liquid into the discharge pipe includes an on-off valve, and a predetermined amount of cleaning liquid is supplied into the decomposition tank. In an open state after the internal pressure in the decomposition tank reaches a pressure exceeding the atmospheric pressure due to the supply of air from the air supply means and a predetermined amount of cleaning liquid is supplied from the second cleaning liquid supply means to the discharge pipe The cleaning liquid in the discharge pipe is controlled so as to be discharged by the pressurized cleaning liquid in the decomposition tank.

第1から第6の発明によれば、分解槽内部及び排出管路の内部に付着した固形分を容易にかつ確実に除去することができる。 According to the first to the sixth invention, the solid adhering to the inside of the decomposition vessel interior and the discharge pipe can be easily and reliably removed.

の発明によれば、分解槽は、この分解槽内部及び排出管路の内部を洗浄する洗浄装置を有することにより、分解槽内部及び排出管路の内部に付着した固形分を容易にかつ確実に除去することができる。 According to the seventh invention, the decomposition tank has a cleaning device for cleaning the inside of the decomposition tank and the inside of the discharge pipe, so that the solid content attached to the inside of the decomposition tank and the inside of the discharge pipe can be easily and It can be removed reliably.

の発明によれば、洗浄装置における第1の洗浄液供給手段の洗浄液供給口が、原料供給管路に設けられていることにより、上記第の発明の効果に加えて、原料供給管路の内部の洗浄を行うことができ、原料供給管路の閉塞を防止することができる。 According to the eighth invention, the cleaning liquid supply port of the first cleaning liquid supply means in the washing apparatus, by which is provided in the material supply line, in addition to the seventh inventions of the effect, the raw material supply pipe The inside of the passage can be cleaned, and blockage of the raw material supply conduit can be prevented.

の発明によれば、洗浄装置における第1の洗浄液供給手段の洗浄液供給口が、分解槽の安全弁の2次側に設けられていることにより、上記第の発明の効果に加えて、安全弁の洗浄を行うことができ、安全弁の閉塞を防止することができる。 According to the ninth invention, the cleaning liquid supply port of the first cleaning liquid supply means in the washing apparatus, by which is provided on the secondary side of the safety valve of the decomposition vessel, in addition to the seventh inventions of the effect The safety valve can be cleaned and the safety valve can be prevented from being blocked.

10の発明によれば、洗浄装置における第1の洗浄液供給手段の洗浄液供給口から分解槽内に延びる配管の先端に噴射ノズルが設けられ、分解槽内部の特定部位を洗浄液の噴射によって洗浄することにより、上記第の発明の効果に加えて、分解槽内において特定部位に付着した固形分を容易にかつ確実に洗浄除去することができる。 According to the tenth invention, the injection nozzle is provided at the tip of the pipe extending from the cleaning liquid supply port of the first cleaning liquid supply means in the cleaning apparatus into the decomposition tank, and the specific part inside the decomposition tank is cleaned by the injection of the cleaning liquid. it makes it possible in addition to the seventh inventions of the effect, easily and reliably cleaned and removed solids adhering to the specific site in the decomposition tank.

11の発明によれば、排出管路の出口側に排液貯槽を有していることにより、分解槽から排出された洗浄液を再利用することができる。 According to the eleventh aspect , since the drainage storage tank is provided on the outlet side of the discharge pipe, the cleaning liquid discharged from the decomposition tank can be reused.

12の発明によれば、分解槽の後段に分解液から固形分を分離する固形分分離装置を有していることにより、洗浄液から固形分が確実に除去され、洗浄液を有効に再利用することができる。 According to the twelfth invention, the solid content separation device that separates the solid content from the decomposition liquid is provided at the subsequent stage of the decomposition tank, so that the solid content is reliably removed from the cleaning liquid, and the cleaning liquid is effectively reused. be able to.

13の発明によれば、上記第から第12の発明の効果に加えて、排出管路の内部に付着した固形分をさらに一層確実に除去することができる。 According to the thirteenth invention, in addition to the effects of the seventh to twelfth inventions, the solid content adhering to the inside of the discharge pipe can be further reliably removed.

本発明に係るプラスチックの分解装置の一実施形態を示した概要構成図である。It is the outline | summary block diagram which showed one Embodiment of the plastics decomposition | disassembly apparatus based on this invention. 本発明に係るプラスチックの分解装置の別の一実施形態を示した概要構成図である。It is the outline | summary block diagram which showed another one Embodiment of the plastics decomposition | disassembly apparatus based on this invention. 本発明に係るプラスチックの分解装置のさらに別の一実施形態を示した概要構成図である。It is the outline | summary block diagram which showed another one Embodiment of the plastics decomposition | disassembly apparatus based on this invention. 本発明に係るプラスチックの分解装置のさらに別の一実施形態を示した概要構成図である。It is the outline | summary block diagram which showed another one Embodiment of the plastics decomposition | disassembly apparatus based on this invention. 本発明に係るプラスチックの分解装置のさらに別の一実施形態を示した概要構成図である。It is the outline | summary block diagram which showed another one Embodiment of the plastics decomposition | disassembly apparatus based on this invention. 本発明に係るプラスチックの分解装置のさらに別の一実施形態を示した概要構成図である。It is the outline | summary block diagram which showed another one Embodiment of the plastics decomposition | disassembly apparatus based on this invention. 本発明に係るプラスチックの分解装置のさらに別の一実施形態を示した概要構成図である。It is the outline | summary block diagram which showed another one Embodiment of the plastics decomposition | disassembly apparatus based on this invention.

図1は、本発明に係るプラスチックの分解装置の一実施形態を示した概要構成図である。   FIG. 1 is a schematic configuration diagram showing an embodiment of a plastic disassembling apparatus according to the present invention.

本実施形態のプラスチックの分解装置は、プラスチックを超臨界又は亜臨界の状態で溶媒にて分解する円筒形で耐圧性の分解槽1を備えており、この分解槽1の上部にプラスチックを供給する配管が接続され、原料供給管路2が形成されている。原料供給管路2の分解槽1側には供給弁21が設けられており、供給弁21を開放することによってプラスチックが分解槽1に供給される。プラスチックは、例えば、炭酸カルシウム、水酸化アルミニウム等の無機充填材やガラス繊維等の無機繊維を含むFRP等のプラスチック成形品であり、分解槽1内での溶媒との攪拌混合性を高めて反応効率を向上させるために、粒径が1−20mm程度、好ましくは最大粒子径が10mm以下になるように粉砕して使用するのが好ましい。このように粉砕された粉粒状のプラスチックが原料供給管路2を通じて分解槽1に供給される。   The plastic decomposition apparatus according to the present embodiment includes a cylindrical pressure-resistant decomposition tank 1 that decomposes plastic with a solvent in a supercritical or subcritical state, and supplies the plastic to the upper part of the decomposition tank 1. Pipes are connected to form a raw material supply pipe 2. A supply valve 21 is provided on the side of the raw material supply pipe 2 on the decomposition tank 1, and the plastic is supplied to the decomposition tank 1 by opening the supply valve 21. The plastic is, for example, a plastic molded product such as FRP containing inorganic fillers such as calcium carbonate and aluminum hydroxide, and inorganic fibers such as glass fibers, and reacts by increasing the stirring and mixing properties with the solvent in the decomposition tank 1. In order to improve the efficiency, it is preferable to use after pulverizing so that the particle size is about 1-20 mm, preferably the maximum particle size is 10 mm or less. The pulverized powdery plastic is supplied to the decomposition tank 1 through the raw material supply pipe 2.

分解槽1の底部には配管で構成される排出管路3が形成され、その途中に排出用開閉弁31が設けられている。排出用開閉弁31を開放することによって、分解槽1の内容物が排出される。   A discharge pipe 3 composed of piping is formed at the bottom of the decomposition tank 1, and a discharge opening / closing valve 31 is provided in the middle thereof. The contents of the decomposition tank 1 are discharged by opening the discharge on-off valve 31.

分解槽1は、この分解槽1内部及び排出管路3の内部を洗浄する洗浄装置4を有しており、この洗浄装置4は、例えば、加圧ポンプ等によって洗浄液100を供給する洗浄液供給手段とコンプレッサ等によって空気を供給する空気供給手段とから構成される。具体的には、この洗浄装置4は、洗浄液供給手段として洗浄液100を供給する洗浄液供給口5と、空気供給手段として分解槽1に空気を供給して分解槽1の内圧を高める空気供給口6を有している。このような洗浄液供給口5は、分解槽1内に洗浄液100を供給することができれば分解槽1のいかなる箇所に配設されていてもよく特に制限されない。同様に、空気供給口6についても、分解槽1内に空気を供給することができれば分解槽1のいかなる箇所に配設されていてもよく、特に制限されない。洗浄液供給口5から加圧ポンプ等によって所定量の洗浄液100を分解槽1に供給することによって分解槽1の内壁に付着した固形分を洗浄除去する。次いで分解槽1の内圧が所定の圧力になるまで空気供給口6からコンプレッサ等によって空気を供給する。分解槽1の内圧が所定の圧力になった後は、空気の供給を停止して排出管路3の排出用開閉弁31を開放する。排出用開閉弁31が開放されると、分解槽1の内圧によって洗浄液100が勢いよく排出管路3を通じて外部に排出される。したがって、このように分解槽1の内圧により排出される洗浄液100によって排出管路3の内部に付着した固形分を洗浄除去することができる。ここで、所定の圧力とは、分解槽1内の洗浄液100が全て排出管路3に排出されるような分解槽1の内圧であり、例えば、常圧(大気圧)を超える圧力であってもよいが、排出管路3の洗浄効果を考慮すると、150〜500kPa程度とすることができる。   The decomposition tank 1 has a cleaning device 4 for cleaning the inside of the decomposition tank 1 and the inside of the discharge pipe 3, and the cleaning device 4 is a cleaning liquid supply means for supplying the cleaning liquid 100 by a pressure pump, for example. And air supply means for supplying air by a compressor or the like. Specifically, the cleaning device 4 includes a cleaning liquid supply port 5 that supplies the cleaning liquid 100 as cleaning liquid supply means, and an air supply port 6 that increases the internal pressure of the decomposition tank 1 by supplying air to the decomposition tank 1 as air supply means. have. Such a cleaning liquid supply port 5 is not particularly limited as long as it can supply the cleaning liquid 100 into the decomposition tank 1 and may be disposed at any location of the decomposition tank 1. Similarly, the air supply port 6 may be disposed at any location in the decomposition tank 1 as long as it can supply air into the decomposition tank 1 and is not particularly limited. By supplying a predetermined amount of the cleaning liquid 100 from the cleaning liquid supply port 5 to the decomposition tank 1 by a pressure pump or the like, the solid content adhering to the inner wall of the decomposition tank 1 is cleaned and removed. Next, air is supplied from the air supply port 6 by a compressor or the like until the internal pressure of the decomposition tank 1 reaches a predetermined pressure. After the internal pressure of the decomposition tank 1 reaches a predetermined pressure, the supply of air is stopped and the discharge on-off valve 31 of the discharge pipe 3 is opened. When the discharge opening / closing valve 31 is opened, the cleaning liquid 100 is vigorously discharged to the outside through the discharge pipe 3 by the internal pressure of the decomposition tank 1. Therefore, the solid content adhering to the inside of the discharge pipe 3 can be washed and removed by the cleaning liquid 100 discharged by the internal pressure of the decomposition tank 1 in this way. Here, the predetermined pressure is an internal pressure of the decomposition tank 1 such that all the cleaning liquid 100 in the decomposition tank 1 is discharged to the discharge pipe 3, for example, a pressure exceeding normal pressure (atmospheric pressure). However, considering the cleaning effect of the discharge pipe 3, it can be about 150 to 500 kPa.

洗浄液100の種類としては、プラスチックの分解に用いられる溶媒と同様のものを用いることができ、例えば、水やアルコール等の流体を挙げることができる。この流体に水酸化ナトリウム等のアルカリが共存されていてもよい。   As the type of the cleaning liquid 100, the same solvent as that used for decomposing plastics can be used, and examples thereof include fluids such as water and alcohol. An alkali such as sodium hydroxide may coexist in this fluid.

本実施形態では、図1に示すように、空気供給口6を有する配管が原料供給管路2を構成する配管に供給弁21の上流側で接続され、洗浄液供給口5を有する配管が空気供給口6を有する配管の途中に接続されている。このように本実施形態では洗浄液供給口5が原料供給管路2に設けられているため、洗浄液供給口5から洗浄液100を分解槽1に向けて供給することにより、原料供給管路2の内部も洗浄することができ、原料供給管路2の閉塞を防止することができる。   In the present embodiment, as shown in FIG. 1, a pipe having an air supply port 6 is connected to a pipe constituting the raw material supply pipe 2 on the upstream side of the supply valve 21, and a pipe having the cleaning liquid supply port 5 is supplied with air. It is connected in the middle of the pipe having the port 6. Thus, in this embodiment, since the cleaning liquid supply port 5 is provided in the raw material supply line 2, the cleaning liquid 100 is supplied from the cleaning liquid supply port 5 toward the decomposition tank 1, whereby the inside of the raw material supply line 2. Can also be washed, and blockage of the raw material supply pipe 2 can be prevented.

洗浄液供給口5を有する配管には洗浄液供給弁51が設けられており、これを開放することによって洗浄液100が洗浄液供給口5から高圧ポンプ等によって導入され、供給弁21を含む原料供給管路2の内部が洗浄されるとともに分解槽1内に供給されて分解槽1内部も洗浄される。原料供給管路2の口径が大きく、一定の洗浄液量で充分な洗浄効果が得られない場合には、一時的に原料供給管路2の供給弁21を閉止し、原料供給管路2に洗浄液100を貯留した上で、供給弁21を開放して洗浄するようにしてもよい。   The piping having the cleaning liquid supply port 5 is provided with a cleaning liquid supply valve 51. By opening this, the cleaning liquid 100 is introduced from the cleaning liquid supply port 5 by a high pressure pump or the like, and the raw material supply line 2 including the supply valve 21 is provided. The inside of the tank is washed and supplied to the decomposition tank 1 so that the inside of the decomposition tank 1 is also washed. When the diameter of the raw material supply pipe 2 is large and a sufficient cleaning effect cannot be obtained with a constant amount of cleaning liquid, the supply valve 21 of the raw material supply pipe 2 is temporarily closed, and the cleaning liquid is supplied to the raw material supply pipe 2. After storing 100, the supply valve 21 may be opened for cleaning.

空気供給口6を有する配管には空気供給弁61が設けられており、洗浄液100で原料供給管路2を洗浄した後は、空気供給弁61を開放して空気供給口6からコンプレッサ等によって乾燥空気を導入する。これによって、洗浄液100で濡れた原料供給管路2の内部を乾燥させ、次バッチでのプラスチックの供給時にプラスチックが原料供給管路2の内部に付着し易くなるのを防止できる。このような空気供給口6からの乾燥空気の供給は、上述したように、分解槽1の内圧が所定の圧力になるまで行われる。   The pipe having the air supply port 6 is provided with an air supply valve 61. After cleaning the raw material supply pipe 2 with the cleaning liquid 100, the air supply valve 61 is opened and dried from the air supply port 6 by a compressor or the like. Introduce air. As a result, the inside of the raw material supply pipe 2 wet with the cleaning liquid 100 is dried, and it is possible to prevent the plastic from being easily attached to the inside of the raw material supply pipe 2 when the plastic is supplied in the next batch. The supply of the dry air from the air supply port 6 is performed until the internal pressure of the decomposition tank 1 reaches a predetermined pressure as described above.

本実施形態の分解槽1の上部には、溶媒を供給する配管が接続され、溶媒供給弁71と溶媒供給口72を有する溶媒供給管路7が形成されている。溶媒は、溶媒供給弁71を開放して溶媒供給口72から溶媒供給管路7を通じて分解槽1内に供給され、超臨界又は亜臨界状態でプラスチックの反応触媒として作用してプラスチックが分解される。このような溶媒の種類としては、水やアルコール等の流体であり、この流体に水酸化ナトリウム等のアルカリが共存されていてもよい。   A pipe for supplying a solvent is connected to the upper part of the decomposition tank 1 of the present embodiment, and a solvent supply line 7 having a solvent supply valve 71 and a solvent supply port 72 is formed. The solvent is supplied into the decomposition tank 1 from the solvent supply port 72 through the solvent supply pipe 7 by opening the solvent supply valve 71, and acts as a plastic reaction catalyst in a supercritical or subcritical state to decompose the plastic. . Such a solvent is a fluid such as water or alcohol, and an alkali such as sodium hydroxide may coexist in this fluid.

本実施形態の分解槽1の外周にはヒーターや熱媒ジャケット等で形成される加熱手段8が設けてあり、温度センサー等で形成される温度検出器9が分解槽1内に差し込んで設けられている。また、分解槽1には内部の圧力を測定する圧力ゲージなどで形成される圧力検出手段10が設けられている。プラスチックの分解処理においては、この温度検出器9及び圧力検出手段10で分解槽1の温度、圧力をそれぞれ検出しながら、加熱手段8で分解槽1内を加熱することによって、検出される温度と圧力に基づいて加熱手段8を制御して最適温度での加熱を行うようにしている。この圧力検出手段10は、空気供給口6から空気を供給する際にも分解槽1の内圧を検出しており、検出される圧力に基づいて空気供給弁61を閉止して空気の供給を停止するようにしている。   A heating means 8 formed by a heater, a heat medium jacket or the like is provided on the outer periphery of the decomposition tank 1 of the present embodiment, and a temperature detector 9 formed by a temperature sensor or the like is provided by being inserted into the decomposition tank 1. ing. The decomposition tank 1 is provided with a pressure detecting means 10 formed by a pressure gauge for measuring the internal pressure. In the plastic decomposition process, the temperature detector 9 and the pressure detection means 10 detect the temperature and pressure of the decomposition tank 1, and the heating means 8 heats the decomposition tank 1 to detect the temperature. The heating means 8 is controlled based on the pressure to perform heating at the optimum temperature. The pressure detecting means 10 detects the internal pressure of the decomposition tank 1 even when air is supplied from the air supply port 6, and closes the air supply valve 61 based on the detected pressure to stop the supply of air. Like to do.

本実施形態の分解槽1には、分解槽1に供給されるプラスチックと溶媒を混合する攪拌装置20が設けられている。攪拌装置20は、回転軸201と、回転軸201に取り付けられた攪拌翼202を有しており、分解槽1の上部に設けたモータで回転軸201を回転駆動することにより、プラスチックの分解処理においては分解槽1内のプラスチックと溶媒を攪拌混合する。分解槽1内に洗浄液100が供給された際には、攪拌装置20の回転軸201をモータで回転駆動させることにより、分解槽1の内壁に付着した固形分を効果的に除去できるとともに、洗浄により剥離して分解槽1の底部に沈降していた固形分を攪拌し、洗浄液100の排出時に分解槽1内に残留しないようにする。   The decomposition tank 1 of the present embodiment is provided with a stirring device 20 for mixing the plastic and solvent supplied to the decomposition tank 1. The agitation device 20 has a rotating shaft 201 and an agitating blade 202 attached to the rotating shaft 201. By rotating the rotating shaft 201 with a motor provided in the upper part of the decomposition tank 1, the plastic decomposition process is performed. In, the plastic and solvent in the decomposition tank 1 are stirred and mixed. When the cleaning liquid 100 is supplied into the decomposition tank 1, the rotating shaft 201 of the stirring device 20 is driven to rotate by a motor, so that the solid content adhering to the inner wall of the decomposition tank 1 can be effectively removed and the cleaning liquid is washed. The solid content that has been peeled off and settled at the bottom of the decomposition tank 1 is stirred so that it does not remain in the decomposition tank 1 when the cleaning liquid 100 is discharged.

本実施形態の分解槽1には、配管で構成される安全弁管路30が形成されて、安全弁管路30の途中に安全弁301が設けられている。安全弁301は、プラスチックの分解処理時における高温高圧下において、内圧の異常上昇による分解槽1の破損などを防止するための安全機構を有する弁である。   In the decomposition tank 1 of the present embodiment, a safety valve line 30 constituted by piping is formed, and a safety valve 301 is provided in the middle of the safety valve line 30. The safety valve 301 is a valve having a safety mechanism for preventing damage to the decomposition tank 1 due to an abnormal increase in internal pressure under high temperature and high pressure during plastic decomposition.

本実施形態では、分解槽1が密閉された状態で洗浄液供給口5による洗浄液100の供給ができない。このため、開閉弁を別途設けてこれを開放することで分解槽1を外部に開放して洗浄液100を供給してもよいが、上記安全弁301を開放し分解槽1を外部に開放して洗浄液100を供給するようにしてもよい。洗浄液100を分解槽1内に供給した後は安全弁301を閉止し、空気供給口6より空気を供給して分解槽1の内圧を所定の圧力まで高める。   In the present embodiment, the cleaning liquid 100 cannot be supplied from the cleaning liquid supply port 5 in a state where the decomposition tank 1 is sealed. For this reason, a separate on-off valve may be provided and opened to open the decomposition tank 1 to the outside and supply the cleaning liquid 100. However, the safety valve 301 is opened to open the decomposition tank 1 to the outside and the cleaning liquid is supplied. 100 may be supplied. After supplying the cleaning liquid 100 into the decomposition tank 1, the safety valve 301 is closed and air is supplied from the air supply port 6 to increase the internal pressure of the decomposition tank 1 to a predetermined pressure.

本実施形態では、分解槽1にロードセル等の重量検出器40が設けられており、分解槽1に供給されたプラスチック、洗浄液100及び溶媒の重量を検出して重量管理ができるようになっている。例えば、所定量の洗浄液100を供給して分解槽1内の洗浄を行うが、この洗浄液100の量を分解槽1内に供給された洗浄液100の重量で検出し、所定重量になったら供給を停止するようにしている。このような洗浄液100の量の管理は、配管に流量計を設けてその積算流量を測定することで管理するようにしてもよい。   In the present embodiment, a weight detector 40 such as a load cell is provided in the decomposition tank 1 so that the weight of the plastic, the cleaning liquid 100 and the solvent supplied to the decomposition tank 1 can be detected and weight management can be performed. . For example, a predetermined amount of the cleaning liquid 100 is supplied to clean the inside of the decomposition tank 1, and the amount of the cleaning liquid 100 is detected by the weight of the cleaning liquid 100 supplied into the decomposition tank 1, and the supply is performed when the predetermined weight is reached. I try to stop. The amount of the cleaning liquid 100 may be managed by providing a flow meter in the pipe and measuring the integrated flow rate.

以上の構成を備えた分解装置では次のようにして洗浄処理を行う。なお、この洗浄処理は、分解槽1内でプラスチックの分解処理が終了し、分解液が分解槽1から排出された状態で行うものとする。   In the disassembling apparatus having the above configuration, the cleaning process is performed as follows. In addition, this washing process shall be performed in a state where the plastic decomposition process is completed in the decomposition tank 1 and the decomposition solution is discharged from the decomposition tank 1.

まず、排出用開閉弁31を閉止し、洗浄液供給弁51、供給弁21及び安全弁301を開放して、洗浄液100を洗浄液供給口5から分解槽1に供給する。洗浄液100を分解槽1に供給することによって、原料供給管路2の内部及び分解槽1の内部を洗浄する。分解槽1に供給された洗浄液100の重量を重量検出器40で検出し、所定量に達したら洗浄液供給弁51を閉止して洗浄液100の供給を停止する。分解槽1に供給した洗浄液100を攪拌装置20によって攪拌して分解槽1の内壁に付着した固形分を除去するが、その際には洗浄によって剥離した固形分が分解槽1の底部に沈降しないように攪拌する。次いで、安全弁301を閉止し、空気供給弁61を開放して空気供給口6から空気を供給して分解槽1の内圧を高める。分解槽1の内圧を圧力検出手段10で検出して、所定の圧力に達したら、空気供給弁61を閉止して空気の供給を停止する。次いで、排出用開閉弁31を開放し、分解槽1の内圧によって加圧された洗浄液100を分解槽1から排出管路3を通じて外部に排出する。これによって、排出管路3の内部に付着した固形分を洗浄除去する。   First, the discharge on-off valve 31 is closed, the cleaning liquid supply valve 51, the supply valve 21 and the safety valve 301 are opened, and the cleaning liquid 100 is supplied from the cleaning liquid supply port 5 to the decomposition tank 1. By supplying the cleaning liquid 100 to the decomposition tank 1, the inside of the raw material supply pipe 2 and the inside of the decomposition tank 1 are cleaned. The weight of the cleaning liquid 100 supplied to the decomposition tank 1 is detected by the weight detector 40. When a predetermined amount is reached, the cleaning liquid supply valve 51 is closed to stop the supply of the cleaning liquid 100. The cleaning liquid 100 supplied to the decomposition tank 1 is stirred by the stirring device 20 to remove the solid content adhering to the inner wall of the decomposition tank 1, but at this time, the solid content separated by the cleaning does not settle to the bottom of the decomposition tank 1. To stir. Next, the safety valve 301 is closed, the air supply valve 61 is opened, and air is supplied from the air supply port 6 to increase the internal pressure of the decomposition tank 1. When the internal pressure of the decomposition tank 1 is detected by the pressure detection means 10 and reaches a predetermined pressure, the air supply valve 61 is closed to stop the supply of air. Next, the discharge on-off valve 31 is opened, and the cleaning liquid 100 pressurized by the internal pressure of the decomposition tank 1 is discharged from the decomposition tank 1 through the discharge pipe 3 to the outside. As a result, the solid content adhering to the inside of the discharge pipe 3 is removed by washing.

このように本実施形態では、分解槽1内部及び排出管路3の内部の洗浄とともに原料供給管路2の洗浄も行っている。   As described above, in this embodiment, the raw material supply pipe 2 is cleaned together with the inside of the decomposition tank 1 and the inside of the discharge pipe 3.

以上の実施形態では、洗浄液供給口5と溶媒供給口72が別々に設けられているが、例えば洗浄液100を溶媒と同種のものを用いる場合、洗浄液供給口5から溶媒を分解槽1に供給してプラスチックの分解処理を行うようにしてもよい。この場合、溶媒供給口72を有する溶媒供給管路7を洗浄液供給口5と別体として設ける必要がなく、構造がより簡素化されて小型化が図られ、低コストで分解装置を作製できる利点がある。   In the above embodiment, the cleaning liquid supply port 5 and the solvent supply port 72 are provided separately. For example, when the same type of cleaning liquid 100 is used as the solvent, the solvent is supplied from the cleaning liquid supply port 5 to the decomposition tank 1. The plastic may be decomposed. In this case, there is no need to provide the solvent supply line 7 having the solvent supply port 72 as a separate body from the cleaning liquid supply port 5, and the structure can be simplified and reduced in size, and the decomposition apparatus can be manufactured at low cost. There is.

また、本実施形態では、原料供給管路2を通じてプラスチックを分解槽1に供給し、溶媒供給管路7を通じて溶媒を分解槽1内に供給しているが、プラスチックと溶媒を共に原料供給管路2を通じて分解槽1に供給するようにしてもよい。この場合についても、溶媒供給管路7を別体として設ける必要がなく、構造がより簡素化されて小型化が図られ、低コストで分解装置を作製できる利点がある。   In this embodiment, the plastic is supplied to the decomposition tank 1 through the raw material supply line 2 and the solvent is supplied into the decomposition tank 1 through the solvent supply line 7. However, both the plastic and the solvent are supplied to the raw material supply line. 2 may be supplied to the decomposition tank 1. Also in this case, there is no need to provide the solvent supply pipe 7 as a separate body, and there is an advantage that the structure can be simplified and the size can be reduced, and the decomposition apparatus can be manufactured at low cost.

図2は、本発明に係るプラスチックの分解装置の別の一実施形態を示した概要構成図である。なお、図1に示した部分と同一の部分については同じ符号を付し、説明を省略する。   FIG. 2 is a schematic configuration diagram showing another embodiment of the plastic disassembling apparatus according to the present invention. In addition, the same code | symbol is attached | subjected about the part same as the part shown in FIG. 1, and description is abbreviate | omitted.

分解槽1でのプラスチックの分解処理時、分解液の飛沫によって安全弁管路30の内部に固形分が付着する場合がある。本実施形態では、安全弁管路30の内部に付着した固形分を洗浄除去するものである。具体的には、安全弁管路30における安全弁301の2次側に洗浄液供給口5を有する配管が接続されている。このような分解装置においては、洗浄液供給口5から洗浄液100を供給すると、安全弁301の2次側から安全弁管路30を通じて分解槽1に至るので、安全弁301を含む安全弁管路30の内部を洗浄することができ、これによって安全弁管路30の閉塞を防止し、安全性を確保することができる。   During the plastic decomposition process in the decomposition tank 1, solid content may adhere to the inside of the safety valve line 30 due to the spray of the decomposition liquid. In this embodiment, the solid content adhering to the inside of the safety valve conduit 30 is washed away. Specifically, a pipe having the cleaning liquid supply port 5 is connected to the secondary side of the safety valve 301 in the safety valve line 30. In such a decomposition apparatus, when the cleaning liquid 100 is supplied from the cleaning liquid supply port 5, it reaches the decomposition tank 1 from the secondary side of the safety valve 301 through the safety valve line 30, so that the inside of the safety valve line 30 including the safety valve 301 is cleaned. Thus, the safety valve line 30 can be prevented from being blocked and safety can be ensured.

なお、図2の分解装置は、図1の分解装置と同様に空気供給口6が原料供給管路2に設けられているが、安全弁301の2次側に洗浄液供給口5とあわせて空気供給口6を設けるようにしてもよい。   2, the air supply port 6 is provided in the raw material supply pipe 2 in the same manner as the decomposition device in FIG. 1, but air is supplied to the secondary side of the safety valve 301 together with the cleaning liquid supply port 5. A mouth 6 may be provided.

図3は、本発明に係るプラスチックの分解装置のさらに別の一実施形態を示した概要構成図である。なお、図1に示した部分と同一の部分については同じ符号を付し、説明を省略する。   FIG. 3 is a schematic configuration diagram showing still another embodiment of the plastic disassembling apparatus according to the present invention. In addition, the same code | symbol is attached | subjected about the part same as the part shown in FIG. 1, and description is abbreviate | omitted.

本実施形態では、洗浄液供給口5を有する配管が2つに分岐して分解槽1内に延び、各々の先端に噴射ノズル52が設けられている。噴射ノズル52は、例えば、スプレーノズルやシャワー状に噴射するノズルであり、流量、噴射圧力、噴射形態等を変えて、分解槽1内部の特定部位を洗浄し、付着した固形分を剥ぎ取る効果を奏する。分解槽1内の分解液の喫水面には無機物を主成分とする固形分が特に付着しやすくなっており、付着の程度にもよるが、場合によっては分解槽1の加熱性能が低下しこれに伴い分解効率も低下する。本実施形態の分解装置は、このような部位に付着した固形分の除去に有効であり、分解槽1の分解効率を維持することができる。   In the present embodiment, the pipe having the cleaning liquid supply port 5 branches into two and extends into the decomposition tank 1, and an injection nozzle 52 is provided at each tip. The spray nozzle 52 is, for example, a spray nozzle or a nozzle that sprays in the form of a shower, and changes the flow rate, spray pressure, spray form, and the like to clean a specific part inside the decomposition tank 1 and strip off the attached solid content. Play. Solid content mainly composed of inorganic substances easily adheres to the draft surface of the decomposition solution in the decomposition tank 1, and depending on the degree of adhesion, depending on the case, the heating performance of the decomposition tank 1 may decrease. As a result, the decomposition efficiency also decreases. The decomposition apparatus of the present embodiment is effective for removing the solid content attached to such a part, and can maintain the decomposition efficiency of the decomposition tank 1.

図4は、本発明に係るプラスチックの分解装置のさらに別の一実施形態を示した概要構成図である。なお、図1に示した部分と同一の部分については同じ符号を付し、説明を省略する。   FIG. 4 is a schematic configuration diagram showing still another embodiment of the plastic disassembling apparatus according to the present invention. In addition, the same code | symbol is attached | subjected about the part same as the part shown in FIG. 1, and description is abbreviate | omitted.

分解槽1でプラスチックの分解処理が終了すると、図4に示すように、その分解液は排出用開閉弁31を開放することによって分解槽1の底部から排出管路3を通じて分解液貯槽50に回収される。本実施形態では、分解液の分解液貯槽50とは別に、分解槽1から排出された洗浄液100を貯留するための排液貯槽60が排出管路3の出口側に設けられている。分解液貯槽50は排液貯槽60の上流側に設けられているが、分解液貯槽50が排液貯槽60の下流側に設けられていてもよく、その位置関係は特に問わない。分解液貯槽50と排液貯槽60には各々、分解液開閉弁501と排液開閉弁601がその入口側に設けられている。これを開放することにより分解液、洗浄液100がそれぞれ分解液貯槽50と排液貯槽60に回収される。例えば、プラスチックの分解処理が終了して分解槽1から分解液を排出した時は、排液開閉弁601を閉止し、分解液開閉弁501を開放して分解液を分解液貯槽50に回収するようにし、分解槽1の内部の洗浄が終了して分解槽1から洗浄液100を排出した時には、逆に分解液開閉弁501を閉止し、排液開閉弁601を開放して洗浄液100を排液貯槽60に回収するようにする。   When the plastic decomposition process is completed in the decomposition tank 1, the decomposition liquid is recovered from the bottom of the decomposition tank 1 to the decomposition liquid storage tank 50 through the discharge pipe 3 by opening the discharge on-off valve 31, as shown in FIG. Is done. In the present embodiment, a waste liquid storage tank 60 for storing the cleaning liquid 100 discharged from the decomposition tank 1 is provided on the outlet side of the discharge pipe 3 separately from the decomposition liquid storage tank 50 of the decomposition liquid. Although the decomposition liquid storage tank 50 is provided on the upstream side of the drainage liquid storage tank 60, the decomposition liquid storage tank 50 may be provided on the downstream side of the drainage liquid storage tank 60, and the positional relationship is not particularly limited. The decomposition liquid storage tank 50 and the drainage liquid storage tank 60 are respectively provided with a decomposition liquid opening / closing valve 501 and a drainage opening / closing valve 601 on the inlet side thereof. By opening this, the decomposition solution and the cleaning solution 100 are collected in the decomposition solution storage tank 50 and the drainage storage tank 60, respectively. For example, when the plastic decomposition process is completed and the decomposition liquid is discharged from the decomposition tank 1, the drainage on-off valve 601 is closed, the decomposition liquid on-off valve 501 is opened, and the decomposition liquid is collected in the decomposition liquid storage tank 50. Thus, when cleaning of the inside of the decomposition tank 1 is completed and the cleaning liquid 100 is discharged from the decomposition tank 1, conversely, the decomposition liquid on-off valve 501 is closed and the drain on-off valve 601 is opened to discharge the cleaning liquid 100. It collects in the storage tank 60.

このように本実施形態では、分解液と洗浄液100をそれぞれ別々に回収しているので、各々再利用することが可能になっている。例えば、回収した洗浄液100は、再度、洗浄液100やプラスチックを分解するための溶媒として利用することができる。   Thus, in this embodiment, since the decomposition liquid and the cleaning liquid 100 are collected separately, each can be reused. For example, the recovered cleaning liquid 100 can be used again as a solvent for decomposing the cleaning liquid 100 and plastic.

図5は、本発明に係るプラスチックの分解装置のさらに別の一実施形態を示した概要構成図である。なお、図1および図4に示した部分と同一の部分については同じ符号を付し、説明を省略する。   FIG. 5 is a schematic configuration diagram showing still another embodiment of the plastic disassembling apparatus according to the present invention. In addition, the same code | symbol is attached | subjected about the part same as the part shown in FIG. 1 and FIG. 4, and description is abbreviate | omitted.

本実施形態では、分解液貯槽50及び排液貯槽60の出口側に濾過等の固形分分離装置70を有している。例えば、排液貯槽60に貯留されている洗浄液100には、原料供給管路2、分解槽1、安全弁管路30、排出管路3等の洗浄で除去された固形分が含まれている。このような固形分を含む洗浄液100を前記固形分分離装置70に通すことによって洗浄液100から固形分を分離して濾液を回収することができる。分解液も未分解や未溶解の固形分が含まれているので、分解液を前記固形分分離装置70に通すことによって分解液から固形分を分離して濾液を回収することができる。   In the present embodiment, a solid content separation device 70 such as filtration is provided on the outlet side of the decomposition liquid storage tank 50 and the drainage liquid storage tank 60. For example, the cleaning liquid 100 stored in the drainage storage tank 60 contains solids removed by cleaning of the raw material supply pipe 2, the decomposition tank 1, the safety valve pipe 30, the discharge pipe 3, and the like. By passing the cleaning liquid 100 containing such a solid content through the solid content separation device 70, the solid content can be separated from the cleaning liquid 100 and the filtrate can be recovered. Since the decomposed liquid also contains undecomposed or undissolved solid content, the filtrate can be collected by separating the solid content from the decomposed liquid by passing the decomposed liquid through the solid content separation device 70.

固形分分離装置70には、分解液貯槽50に貯留された分解液の濾液を回収する分解液濾液貯槽80と、排液貯槽60に貯留された洗浄液100の濾液を回収する排液濾液貯槽90と、に通じる配管が接続されている。分解液濾液貯槽80と排液濾液貯槽90には各々、分解液濾液開閉弁801と排液濾液開閉弁901がその入口側に設けられている。これを開放することにより分解液濾液、洗浄液濾液がそれぞれ分解液濾液貯槽80と排液濾液貯槽90に回収される。例えば、分解液貯槽50から分解液を排出した時は、排液濾液開閉弁901を閉止し、分解液濾液開閉弁801を開放して分解液濾液を分解液濾液貯槽80に回収するようにし、排液貯槽60から洗浄液100を排出した時には、逆に分解液濾液開閉弁801を閉止し、排液濾液開閉弁901を開放して洗浄液濾液を排液濾液貯槽90に回収するようにする。   The solid content separator 70 includes a decomposition liquid filtrate storage tank 80 that collects the filtrate of the decomposition liquid stored in the decomposition liquid storage tank 50, and a drainage filtrate storage tank 90 that collects the filtrate of the cleaning liquid 100 stored in the drainage storage tank 60. And pipes leading to are connected. The cracked filtrate storage tank 80 and the drained filtrate storage tank 90 are respectively provided with a cracked filtrate on-off valve 801 and a drained filtrate on-off valve 901 on the inlet side. By opening this, the decomposed filtrate and the washing filtrate are recovered in the decomposed filtrate storage tank 80 and the drained filtrate storage tank 90, respectively. For example, when the decomposition liquid is discharged from the decomposition liquid storage tank 50, the drainage filtrate on-off valve 901 is closed, the decomposition liquid filtrate on-off valve 801 is opened, and the decomposition liquid filtrate is recovered in the decomposition liquid filtrate storage tank 80. When the cleaning liquid 100 is discharged from the drainage storage tank 60, the decomposition liquid filtrate on / off valve 801 is closed, and the drainage filtrate on / off valve 901 is opened to collect the cleaning liquid filtrate in the drainage filtrate storage tank 90.

このように本実施形態では、分解液濾液と洗浄液濾液をそれぞれ別々に回収しているので、各々再利用することが可能になっている。例えば、回収した洗浄液濾液は、再度、洗浄液100やプラスチックを分解するための溶媒として利用することができる。   As described above, in the present embodiment, since the decomposition solution filtrate and the washing solution filtrate are separately collected, each can be reused. For example, the collected washing liquid filtrate can be used again as a solvent for decomposing the washing liquid 100 and plastic.

図6は、本発明に係るプラスチックの分解装置のさらに別の一実施形態を示した概要構成図である。なお、図1および図4に示した部分と同一の部分については同じ符号を付し、説明を省略する。   FIG. 6 is a schematic configuration diagram showing still another embodiment of the plastic disassembling apparatus according to the present invention. In addition, the same code | symbol is attached | subjected about the part same as the part shown in FIG. 1 and FIG. 4, and description is abbreviate | omitted.

分解槽1からプラスチックの分解液の排出時、高圧排出でスラリ状の分解液を圧送して排出して排出管路3の詰まりを抑制しているが、排出終了段階で繊維等の固形分が一部抜けきらずに排出管路3中に残り、排出管路3の壁面に付着する場合がある。この状態で排出用開閉弁31を開放して分解槽1から洗浄液100を排出すると、排出管路3内を洗浄液100のみが勢いよく通過し、排出管路3の壁面の付着物(固形分)がそのまま残留した状態になる場合がある。   When the plastic decomposition liquid is discharged from the decomposition tank 1, the clogging of the discharge pipe 3 is suppressed by pumping and discharging the slurry-like decomposition liquid by high pressure discharge. There is a case where a part of the discharge pipe 3 remains without being completely removed and adheres to the wall surface of the discharge pipe 3. When the discharge on-off valve 31 is opened in this state and the cleaning liquid 100 is discharged from the decomposition tank 1, only the cleaning liquid 100 passes through the discharge pipe 3 vigorously, and the deposits (solid content) on the wall surface of the discharge pipe 3. May remain as it is.

そこで、本実施形態では、排出管路3に洗浄液供給口5’を設けている。具体的には、洗浄液供給口5’を有する配管が排出管路3を構成する配管に接続されており、その接続位置は排出用開閉弁31の下流側、分解液貯槽50の分解液開閉弁501及び排液貯槽60の排液開閉弁601の上流側である。洗浄液供給口5’を有する配管には洗浄液供給弁51’が設けられており、これを開放して洗浄液供給口5’から高圧ポンプ等により洗浄液100が排出管路3に導入されるようになっている。   Therefore, in the present embodiment, the cleaning liquid supply port 5 ′ is provided in the discharge pipe 3. Specifically, a pipe having a cleaning liquid supply port 5 ′ is connected to a pipe constituting the discharge pipe 3, and the connection position is downstream of the discharge on-off valve 31 and the decomposition liquid on-off valve of the decomposition liquid storage tank 50. 501 and upstream side of the drainage on-off valve 601 of the drainage storage tank 60. The pipe having the cleaning liquid supply port 5 ′ is provided with a cleaning liquid supply valve 51 ′, which is opened and the cleaning liquid 100 is introduced into the discharge pipe 3 from the cleaning liquid supply port 5 ′ by a high-pressure pump or the like. ing.

本実施形態のプラスチックの分解装置で洗浄処理を行うにあたっては、まず、排出用開閉弁31、分解液開閉弁501及び排液開閉弁601を閉止し、洗浄液供給弁51、供給弁21及び安全弁301を開放して、洗浄液供給口5から洗浄液100を分解槽1に供給する。分解槽1内の洗浄液100が所定量に達したら洗浄液供給弁51を閉止して洗浄液100の供給を停止し、分解槽1内の洗浄液100を攪拌装置20によって攪拌して分解槽1の内壁に付着した固形分を除去する。次いで安全弁301を閉止し、空気供給弁61を開放して空気供給口6から空気を供給して分解槽1の内圧を所定の圧力まで高めた後、空気供給弁61を閉止して空気の供給を停止する。その間、洗浄液供給弁51’を開放して洗浄液供給口5’から洗浄液100をタイマ又は積算流量計等によって排出管路3に所定量供給する。このとき排出用開閉弁31、分解液開閉弁501及び排液開閉弁601を閉止しているので、洗浄液供給口5’から排出管路3に供給した洗浄液100は排出用開閉弁31と分解液開閉弁501及び排液開閉弁601との間に溜まる。ここで排出管路3内を洗浄液100で完全に満たす必要はなく、例えば、その容積の7割程度満たしておけばよい。排出管路3内に洗浄液100を貯留した後は、洗浄液供給弁51’を閉止して洗浄液100の供給を停止する。次に、排出用開閉弁31及び排液開閉弁601を開放し、分解槽1の内圧によって加圧された洗浄液100を分解槽1から排出管路3を通じて排出することによって排出管路3内に貯留した洗浄液100を押し出し、その押し出し流れで排出管路3内の壁面の付着物を除去して排出する。これによって排出管路3の清掃が確実なものになる。しかもこの実施形態では、分解槽1内に多量に洗浄液100を供給しなくても排出管路3の壁面の付着物を効果的に除去することができるので、分解槽1及び排出管路3に供給した洗浄液100全体の供給量及び排出量を抑えることができる。   In performing the cleaning process with the plastic decomposing apparatus of the present embodiment, first, the discharge on-off valve 31, the decomposition liquid on-off valve 501, and the drainage on-off valve 601 are closed, and the cleaning liquid supply valve 51, the supply valve 21, and the safety valve 301 are closed. And the cleaning liquid 100 is supplied to the decomposition tank 1 from the cleaning liquid supply port 5. When the cleaning liquid 100 in the decomposition tank 1 reaches a predetermined amount, the cleaning liquid supply valve 51 is closed to stop the supply of the cleaning liquid 100, and the cleaning liquid 100 in the decomposition tank 1 is stirred by the stirring device 20 to the inner wall of the decomposition tank 1. Remove attached solids. Next, the safety valve 301 is closed, the air supply valve 61 is opened, air is supplied from the air supply port 6 to increase the internal pressure of the decomposition tank 1 to a predetermined pressure, and then the air supply valve 61 is closed to supply air. To stop. Meanwhile, the cleaning liquid supply valve 51 'is opened, and a predetermined amount of the cleaning liquid 100 is supplied from the cleaning liquid supply port 5' to the discharge pipe 3 by a timer or an integrated flow meter. At this time, since the discharge on-off valve 31, the decomposition liquid on-off valve 501 and the drainage on-off valve 601 are closed, the cleaning liquid 100 supplied to the discharge pipe 3 from the cleaning liquid supply port 5 ′ is separated from the discharge on-off valve 31 and the decomposition liquid. It collects between the on-off valve 501 and the drainage on-off valve 601. Here, it is not necessary to completely fill the inside of the discharge pipe 3 with the cleaning liquid 100. For example, it may be about 70% of its volume. After the cleaning liquid 100 is stored in the discharge pipe 3, the cleaning liquid supply valve 51 'is closed to stop the supply of the cleaning liquid 100. Next, the discharge on / off valve 31 and the drain on / off valve 601 are opened, and the cleaning liquid 100 pressurized by the internal pressure of the decomposition tank 1 is discharged from the decomposition tank 1 through the discharge pipe 3 into the discharge pipe 3. The stored cleaning liquid 100 is extruded, and the adhered flow on the wall surface in the discharge pipe 3 is removed and discharged by the extrusion flow. This ensures the cleaning of the discharge line 3. Moreover, in this embodiment, the deposits on the wall surface of the discharge pipe 3 can be effectively removed without supplying a large amount of the cleaning liquid 100 into the decomposition tank 1. The supply amount and discharge amount of the supplied cleaning liquid 100 as a whole can be suppressed.

上記実施形態では、排出用開閉弁31、分解液開閉弁501及び排液開閉弁601を閉止して洗浄液供給口5’から洗浄液100を排出管路3に所定量供給していたが、洗浄液供給口5’から洗浄液100を排出管路3に供給するにあたり分解液開閉弁501及び排液開閉弁601を閉止し排出用開閉弁31を開放して分解液の排出方法とは逆の方向に洗浄液100を排出管路3に流すようにしてもよい。この場合、洗浄液100による排出管路3内の洗浄の範囲をより広くするために、洗浄液供給口5’を有する配管と排出管路3を構成する配管との接続位置をより分解液開閉弁501側や排液開閉弁601側に設定することが望ましい。一般的に排出管路3を構成する配管にはバルブや曲がり部等があって閉塞が一番懸念される部分であるため、分解液の排出方法とは逆方向に洗浄液100を流すことによって排出管路3内を効果的に清掃することができる。洗浄液供給口5’から洗浄液100を排出管路3に供給して分解槽1に洗浄液100を溜めた後、洗浄液供給弁51’を閉止して洗浄液100の供給を停止する。次に、洗浄液供給弁51を開放して洗浄液供給口5から洗浄液100を供給して分解槽1にさらに洗浄液100を溜めた後、上記実施形態と同様の方法で空気供給口6から空気を供給して分解槽1の内圧を所定の圧力まで高めて洗浄液100を分解槽1から排出管路3を通じて排出する。ここで、洗浄液供給口5’から供給された分解槽1内の洗浄液100の量や原料供給管路2の内部の汚れの程度によっては、洗浄液供給口5から洗浄液100の供給を行わずに分解槽1の内圧を所定の圧力まで高めて分解槽1から洗浄液100を排出管路3を通じて排出するようにしてもよい。   In the above embodiment, the discharge on / off valve 31, the decomposition liquid on / off valve 501 and the drain on / off valve 601 are closed and the cleaning liquid 100 is supplied to the discharge pipe 3 from the cleaning liquid supply port 5 ′. When supplying the cleaning liquid 100 from the port 5 ′ to the discharge pipe 3, the decomposition liquid on / off valve 501 and the drain liquid on / off valve 601 are closed and the discharge on / off valve 31 is opened to clean the cleaning liquid in the direction opposite to the method of discharging the decomposition liquid. 100 may flow through the discharge line 3. In this case, in order to broaden the range of cleaning in the discharge pipe 3 by the cleaning liquid 100, the connection position of the pipe having the cleaning liquid supply port 5 ′ and the pipe constituting the discharge pipe 3 is further set to the decomposition liquid on-off valve 501. It is desirable to set to the side or the drainage on-off valve 601 side. In general, since the piping constituting the discharge pipe 3 has a valve, a bent portion, and the like and is the portion most likely to be clogged, it is discharged by flowing the cleaning liquid 100 in the direction opposite to the method of discharging the decomposition liquid. The inside of the pipe line 3 can be effectively cleaned. After supplying the cleaning liquid 100 from the cleaning liquid supply port 5 ′ to the discharge pipe 3 and storing the cleaning liquid 100 in the decomposition tank 1, the cleaning liquid supply valve 51 ′ is closed to stop the supply of the cleaning liquid 100. Next, the cleaning liquid supply valve 51 is opened, the cleaning liquid 100 is supplied from the cleaning liquid supply port 5 and the cleaning liquid 100 is further stored in the decomposition tank 1, and then air is supplied from the air supply port 6 in the same manner as in the above embodiment. Then, the internal pressure of the decomposition tank 1 is increased to a predetermined pressure, and the cleaning liquid 100 is discharged from the decomposition tank 1 through the discharge pipe 3. Here, depending on the amount of the cleaning liquid 100 in the decomposition tank 1 supplied from the cleaning liquid supply port 5 ′ and the degree of contamination inside the raw material supply pipe 2, the decomposition is performed without supplying the cleaning liquid 100 from the cleaning liquid supply port 5. The internal pressure of the tank 1 may be increased to a predetermined pressure and the cleaning liquid 100 may be discharged from the decomposition tank 1 through the discharge pipe 3.

図7は、本発明に係るプラスチックの分解装置のさらに別の一実施形態を示した概要構成図である。なお、図1、図4および図6に示した部分と同一の部分については同じ符号を付し、説明を省略する。   FIG. 7 is a schematic configuration diagram showing still another embodiment of the plastic disassembling apparatus according to the present invention. In addition, the same code | symbol is attached | subjected about the part same as the part shown in FIG.1, FIG4 and FIG.6, and description is abbreviate | omitted.

本実施形態は、図6に示したプラスチックの分解装置と同様に排出管路3に洗浄液供給口5’を設けており、洗浄液供給口5’を有する配管を排出管路3を構成する配管に接続しているが、その接続位置は分解槽1により近い箇所、例えば、排出用開閉弁31の上流側としている。   In the present embodiment, the cleaning liquid supply port 5 ′ is provided in the discharge pipe 3 in the same manner as the plastic decomposing apparatus shown in FIG. 6, and the pipe having the cleaning liquid supply port 5 ′ is used as the pipe constituting the discharge pipe 3. Although connected, the connection position is closer to the decomposition tank 1, for example, upstream of the discharge on-off valve 31.

本実施形態のプラスチックの分解装置においても図6のプラスチックの分解装置と同様に洗浄液供給口5’から洗浄液100を排出管路3に導入して排出管路3内を洗浄液100で満たすようにするが、排出管路3全体に渡ってその管路内を満たす必要はなく、例えば、垂直配管の下部や絞り部等、固形物が多く残留していることが予想される箇所が含まれるようにすればよい。そのため、洗浄液供給口5’から排出管路3への洗浄液100の導入にあたっては、排出用開閉弁31を閉止してその排出用開閉弁31よりも上流側の排出管路3内に洗浄液100を満たすようにしたり、もしくは、排出用開閉弁31を開放し分解液開閉弁501及び排液開閉弁601を閉止して分解液開閉弁501及び排液開閉弁601よりも上流側の排出管路3に洗浄液100を満たすようにする等、排出管路3の途中に設けられている開閉弁を適宜開閉して排出管路3内を洗浄液100で満たすようにすればよい。また排出管路3内を洗浄液100で満たす際にはできるだけ気相をなくし、満液の状態にしておくことが望ましい。   Also in the plastic decomposing apparatus of the present embodiment, the cleaning liquid 100 is introduced into the discharge pipe 3 from the cleaning liquid supply port 5 ′ in the same manner as the plastic decomposing apparatus in FIG. 6 so that the discharge pipe 3 is filled with the cleaning liquid 100. However, it is not necessary to fill the entire discharge pipe 3, and for example, a part where a large amount of solid matter is expected to remain, such as a lower part of a vertical pipe or a throttle part, is included. do it. Therefore, when introducing the cleaning liquid 100 from the cleaning liquid supply port 5 ′ into the discharge pipe 3, the discharge on-off valve 31 is closed and the cleaning liquid 100 is poured into the discharge pipe 3 upstream of the discharge on-off valve 31. Alternatively, the discharge on-off valve 31 is opened and the decomposition liquid on-off valve 501 and the drain on-off valve 601 are closed, and the discharge pipe 3 on the upstream side of the decomposition liquid on-off valve 501 and the drain on-off valve 601 The opening and closing valve provided in the middle of the discharge pipe 3 may be appropriately opened and closed so that the inside of the discharge pipe 3 is filled with the cleaning liquid 100. Further, when the inside of the discharge pipe 3 is filled with the cleaning liquid 100, it is desirable to eliminate the gas phase as much as possible and to keep it full.

排出管路3内に洗浄液100を導入する際には、洗浄液供給口5’から導入される洗浄液100の液流れによって排出管路3内に残留した固形物が移動してその固形物同士が折り重なって排出管路3が閉塞をおこしてしまうおそれがあるので、固形物が移動しないように洗浄液供給口5’からの洗浄液100の供給流量を調整することが望ましい。具体的には、固形物が一片10mm程度のFRP片である場合、固形物の沈降速度は0.1m/s程度であるため、その沈降速度よりも小さい速度、例えば固形物の沈降速度の1/10程度の流速、つまり、0.01m/s程度の流速で洗浄液供給口5’から洗浄液100を導入すれば、固形物の移動はほとんど見られない。   When the cleaning liquid 100 is introduced into the discharge pipe 3, the solid matter remaining in the discharge pipe 3 is moved by the liquid flow of the cleaning liquid 100 introduced from the cleaning liquid supply port 5 ′, and the solids are folded over. Therefore, it is desirable to adjust the supply flow rate of the cleaning liquid 100 from the cleaning liquid supply port 5 ′ so that the solid matter does not move. Specifically, when the solid is an FRP piece having a piece of about 10 mm, the settling speed of the solid is about 0.1 m / s, and therefore a speed lower than the settling speed, for example, 1 of the settling speed of the solid. If the cleaning liquid 100 is introduced from the cleaning liquid supply port 5 ′ at a flow rate of about / 10, that is, a flow rate of about 0.01 m / s, the movement of the solid matter is hardly observed.

洗浄処理を行うにあたっては、以上のようにして排出管路3内に洗浄液100を導入した後、図6のプラスチックの分解装置の実施形態と同様にして分解槽1から洗浄液100を圧送して排出管路3内を満たした洗浄液100を押し出して排出する。これによって、排出管路3内の固形物同士が折り重なることなく排出されるため、排出管路3内での閉塞を防止することができる。   In performing the cleaning process, after the cleaning liquid 100 is introduced into the discharge pipe 3 as described above, the cleaning liquid 100 is pumped and discharged from the decomposition tank 1 in the same manner as in the plastic decomposition apparatus of FIG. The cleaning liquid 100 filling the pipeline 3 is pushed out and discharged. As a result, since solids in the discharge pipe 3 are discharged without being folded, blockage in the discharge pipe 3 can be prevented.

1 分解槽
2 原料供給管路
21 供給弁
3 排出管路
31 排出用開閉弁
4 洗浄装置
5,5’ 洗浄液供給口
51,51’ 洗浄液供給弁
52 噴射ノズル
6 空気供給口
61 空気供給弁
30 安全弁管路
301 安全弁
50 分解液貯槽
501 分解液開閉弁
60 排液貯槽
601 排液開閉弁
70 固形分分離装置
80 分解液濾液貯槽
801 分解液濾液開閉弁
90 排液濾液貯槽
901 排液濾液開閉弁
100 洗浄液
DESCRIPTION OF SYMBOLS 1 Decomposition tank 2 Raw material supply line 21 Supply valve 3 Discharge line 31 Discharge on-off valve 4 Cleaning device 5, 5 'Cleaning liquid supply port 51, 51' Cleaning liquid supply valve 52 Injection nozzle 6 Air supply port 61 Air supply valve 30 Safety valve Pipe 301 Safety valve 50 Decomposition liquid storage tank 501 Decomposition liquid opening / closing valve 60 Waste liquid storage tank 601 Drainage opening / closing valve 70 Solid content separation device 80 Decomposition liquid filtrate storage tank 801 Decomposition liquid filtrate opening / closing valve 90 Drainage filtrate storage tank 901 Drainage filtrate opening / closing valve 100 Cleaning liquid

Claims (13)

プラスチックを超臨界又は亜臨界の状態で溶媒にて分解する分解槽を備え、この分解槽にプラスチックを供給する原料供給管路と、前記分解槽で分解されたプラスチックの分解液を取り出す排出管路と、排出管路に開閉弁が形成されている分解装置で開閉弁を閉止した状態でプラスチックを分解処理し、次いで開閉弁を開放して分解槽から分解液を取り出した後、前記分解槽に洗浄液を供給して分解槽及び排出管路を洗浄する方法であって、
分解槽から分解液を取り出した後、開閉弁を閉止状態にして分解槽に洗浄液を供給し、分解槽内に洗浄液を貯留しつつその洗浄液で分解槽内部を洗浄し、次いで、分解槽の内圧が大気圧を超える圧力になるまで分解槽に空気を供給した後、開閉弁を開き、その分解槽の内圧によって分解槽内の洗浄液を排出管路に排出して排出管路内部を洗浄することを特徴とするプラスチックの分解装置の洗浄方法。
A decomposition tank for decomposing plastic with a solvent in a supercritical or subcritical state is provided, a raw material supply line for supplying the plastic to the decomposition tank, and a discharge line for taking out the decomposition solution of the plastic decomposed in the decomposition tank And after the plastic is decomposed in a state in which the on-off valve is closed in the disassembly device in which the on-off valve is formed in the discharge pipe, the on-off valve is opened and the decomposition liquid is taken out from the decomposition tank. A method of supplying a cleaning liquid and cleaning a decomposition tank and a discharge pipe,
After removing the decomposition liquid from the decomposition tank, the cleaning valve is supplied to the decomposition tank with the on-off valve closed, and the inside of the decomposition tank is washed with the cleaning liquid while storing the cleaning liquid in the decomposition tank. After supplying air to the decomposition tank until the pressure exceeds the atmospheric pressure, open the on-off valve and discharge the cleaning liquid in the decomposition tank to the discharge line by the internal pressure of the decomposition tank to clean the inside of the discharge line A method for cleaning a plastic disassembling apparatus.
原料供給管路から洗浄液を分解槽に供給することを特徴とする請求項1に記載のプラスチックの分解装置の洗浄方法。   2. The method for cleaning a plastic decomposing apparatus according to claim 1, wherein the cleaning liquid is supplied to the decomposition tank from the raw material supply pipe. 分解槽の安全弁の2次側から洗浄液を分解槽に供給することを特徴とする請求項1に記載のプラスチックの分解装置の洗浄方法。   2. The method for cleaning a plastic decomposing apparatus according to claim 1, wherein the cleaning liquid is supplied to the decomposition tank from the secondary side of the safety valve of the decomposition tank. 分解槽の内圧によって分解槽内の洗浄液を排出管路に排出する前に、分解槽に加えてさらに排出管路にも洗浄液を供給して排出管路内に洗浄液を予め貯留しておくことを特徴とする請求項1から3のいずれか一項に記載のプラスチックの分解装置の洗浄方法。   Before discharging the cleaning liquid in the decomposition tank to the discharge pipe by the internal pressure of the decomposition tank, supply the cleaning liquid to the discharge pipe in addition to the decomposition tank and store the cleaning liquid in the discharge pipe in advance. The method for cleaning a plastic disassembling apparatus according to any one of claims 1 to 3. 排出管路の下流側から上流側に向かって洗浄液を供給して排出管路内に洗浄液を貯留することを特徴とする請求項4に記載のプラスチックの分解装置の洗浄方法。   5. The method for cleaning a plastic decomposing apparatus according to claim 4, wherein the cleaning liquid is supplied from the downstream side to the upstream side of the discharge pipe and the cleaning liquid is stored in the discharge pipe. 分解槽への空気の供給は、分解槽の内圧が150〜500kPaの範囲の圧力になるまで行われることを特徴とする請求項1から5のいずれか一項に記載のプラスチックの分解装置の洗浄方法。   The supply of air to the decomposition tank is performed until the internal pressure of the decomposition tank reaches a pressure in the range of 150 to 500 kPa, and the plastic decomposition apparatus according to any one of claims 1 to 5, Method. プラスチックを超臨界又は亜臨界の状態で溶媒にて分解する分解槽を備え、この分解槽にプラスチックを供給する原料供給管路と、前記分解槽で分解されたプラスチックの分解液を取り出す排出管路が形成されているプラスチックの分解装置において、
分解槽内部及び排出管路内部を洗浄液で洗浄する洗浄装置と、分解槽内の洗浄液量を検出する洗浄液検出手段と、分解槽内の内圧を検出する圧力検出手段と、排出管路への洗浄液の流入を制御する手段とを備え、
前記洗浄装置は、洗浄液を分解槽に供給する第1の洗浄液供給手段と空気を分解槽に供給する空気供給手段とを有し、第1の洗浄液供給手段は、洗浄液検出手段で検出される洗浄液量に基づいて所定量の洗浄液を供給するものであり、空気供給手段は、分解槽内に所定量の洗浄液が供給されている状態で、圧力検出手段で検出される分解槽内の内圧に基づいて分解槽内の内圧が大気圧を超える圧力になるように空気を供給するものであり、
排出管路への洗浄液の流入を制御する手段は、排出管路に設けられた開閉弁が、分解槽内に所定量の洗浄液が供給されている状態において分解槽内の内圧が大気圧を超える圧力になるように空気供給手段から分解槽への空気の供給中は閉状態とされ、分解槽内の内圧が大気圧を超える圧力に達した後は開状態とされて分解槽内の加圧された洗浄液が排出管路に排出されるように制御されることを特徴とするプラスチックの分解装置。
A decomposition tank for decomposing plastic with a solvent in a supercritical or subcritical state is provided, a raw material supply line for supplying the plastic to the decomposition tank, and a discharge line for taking out the decomposition solution of the plastic decomposed in the decomposition tank In the plastic decomposing apparatus in which
A cleaning device for cleaning the inside of the decomposition tank and the inside of the discharge pipe with a cleaning liquid, a cleaning liquid detection means for detecting the amount of cleaning liquid in the decomposition tank, a pressure detection means for detecting the internal pressure in the decomposition tank, and a cleaning liquid for the discharge pipe Means for controlling the inflow of
The cleaning apparatus has a first cleaning liquid supply means for supplying a cleaning liquid to the decomposition tank and an air supply means for supplying air to the decomposition tank. The first cleaning liquid supply means is a cleaning liquid detected by the cleaning liquid detection means. The air supply means supplies the predetermined amount of cleaning liquid based on the amount, and the air supply means is based on the internal pressure in the decomposition tank detected by the pressure detection means in a state where the predetermined amount of cleaning liquid is supplied in the decomposition tank. Air is supplied so that the internal pressure in the decomposition tank exceeds the atmospheric pressure ,
The means for controlling the flow of the cleaning liquid into the discharge pipe is such that the on-off valve provided in the discharge pipe has an internal pressure exceeding the atmospheric pressure in a state where a predetermined amount of the cleaning liquid is supplied into the decomposition tank. During the supply of air from the air supply means to the decomposition tank so as to become pressure , it is closed, and after the internal pressure in the decomposition tank reaches a pressure exceeding the atmospheric pressure , it is opened and pressurized in the decomposition tank The plastic disassembling apparatus is controlled so that the cleaned cleaning liquid is discharged into a discharge pipe.
洗浄装置における第1の洗浄液供給手段の洗浄液供給口が、原料供給管路に設けられていることを特徴とする請求項7に記載のプラスチックの分解装置。   8. The plastic decomposing apparatus according to claim 7, wherein the cleaning liquid supply port of the first cleaning liquid supply means in the cleaning apparatus is provided in the raw material supply pipe. 洗浄装置における第1の洗浄液供給手段の洗浄液供給口が、分解槽の安全弁の2次側に設けられていることを特徴とする請求項7に記載のプラスチックの分解装置。   8. The plastic decomposition apparatus according to claim 7, wherein the cleaning liquid supply port of the first cleaning liquid supply means in the cleaning apparatus is provided on the secondary side of the safety valve of the decomposition tank. 洗浄装置における第1の洗浄液供給手段の洗浄液供給口から分解槽内に延びる配管の先端に噴射ノズルが設けられ、分解槽内部の特定部位を洗浄液の噴射によって洗浄することを特徴とする請求項7に記載のプラスチックの分解装置。   8. A spray nozzle is provided at a tip of a pipe extending from the cleaning liquid supply port of the first cleaning liquid supply means in the cleaning apparatus into the decomposition tank, and a specific portion inside the decomposition tank is cleaned by spraying the cleaning liquid. The plastic disassembling apparatus described in 1. 排出管路の出口側に排液貯槽を有し、分解槽から排出された洗浄液を再利用可能に貯留していることを特徴とする請求項7から10のいずれか一項に記載のプラスチックの分解装置。   11. The plastic according to claim 7, further comprising a drain storage tank on an outlet side of the discharge pipe, and storing the cleaning liquid discharged from the decomposition tank in a reusable manner. Disassembly equipment. 分解槽の後段に分解液から固形分を分離する固形分分離装置を有し、排液貯槽に貯留された洗浄液を、該固形分分離装置に通水し、固形分を洗浄液中から分離し、固形分が除去された洗浄液を、溶媒や洗浄液として再利用可能にしていることを特徴とする請求項11に記載のプラスチックの分解装置。   It has a solid content separation device that separates the solid content from the decomposition solution at the subsequent stage of the decomposition tank, and the cleaning liquid stored in the drainage storage tank is passed through the solid content separation device to separate the solid content from the cleaning liquid, 12. The plastic decomposing apparatus according to claim 11, wherein the cleaning liquid from which the solid content has been removed is reusable as a solvent or a cleaning liquid. さらに、洗浄装置は、洗浄液を排出管路に供給する第2の洗浄液供給手段を備えており、
第2の洗浄液供給手段は、排出管路の容積に応じた所定量の洗浄液を供給するものであり、
前記排出管路への洗浄液の流入を制御する手段は、開閉弁が、分解槽内に所定量の洗浄液が供給されている状態において空気供給手段からの空気の供給により分解槽内の内圧が大気圧を超える圧力に達し、かつ、第2の洗浄液供給手段から排出管路に所定量の洗浄液が供給された後に開状態とされて、排出管路内の洗浄液が分解槽内の加圧された洗浄液により排出されるように制御されることを特徴とする請求項7から12のいずれか一項に記載のプラスチックの分解装置。
Furthermore, the cleaning device includes a second cleaning liquid supply unit that supplies the cleaning liquid to the discharge pipe line.
The second cleaning liquid supply means supplies a predetermined amount of cleaning liquid according to the volume of the discharge conduit,
The means for controlling the inflow of the cleaning liquid into the discharge pipe has a large internal pressure in the decomposition tank due to the supply of air from the air supply means when the open / close valve is supplied with a predetermined amount of cleaning liquid in the decomposition tank. After reaching a pressure exceeding the atmospheric pressure and a predetermined amount of cleaning liquid is supplied from the second cleaning liquid supply means to the discharge pipe, it is opened, and the cleaning liquid in the discharge pipe is pressurized in the decomposition tank. It is controlled so that it may be discharged | emitted with a washing | cleaning liquid, The plastics decomposition | disassembly apparatus as described in any one of Claim 7 to 12 characterized by the above-mentioned.
JP2009044020A 2008-02-26 2009-02-26 Plastic decomposition apparatus and cleaning method thereof Expired - Fee Related JP4434305B2 (en)

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