JP2002128950A - Process for decomposition treatment of article containing thermosetting resin cured product - Google Patents

Process for decomposition treatment of article containing thermosetting resin cured product

Info

Publication number
JP2002128950A
JP2002128950A JP2000328560A JP2000328560A JP2002128950A JP 2002128950 A JP2002128950 A JP 2002128950A JP 2000328560 A JP2000328560 A JP 2000328560A JP 2000328560 A JP2000328560 A JP 2000328560A JP 2002128950 A JP2002128950 A JP 2002128950A
Authority
JP
Japan
Prior art keywords
decomposition
thermosetting resin
water
product
resin
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2000328560A
Other languages
Japanese (ja)
Inventor
Takayoshi Ueno
貴由 上野
Tetsuji Kawakami
哲司 川上
Takahiko Terada
貴彦 寺田
Keizo Nakajima
啓造 中島
Hiroshi Onishi
宏 大西
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP2000328560A priority Critical patent/JP2002128950A/en
Publication of JP2002128950A publication Critical patent/JP2002128950A/en
Pending 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
    • 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

Landscapes

  • Drying Of Gases (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a simple process for the decomposition treatment of an article containing a thermosetting resin cured product by suppressing the rise in the pressure of a decomposition vessel on the decomposition reaction in order to reutilize thermosetting resins and other constituting elements and make them into resources again. SOLUTION: The process for the decomposition treatment of an article containing a thermosetting resin cured product comprises a decomposition step of bringing the article 1 containing a thermosetting resin cured product into contact with a decomposer material 2 which decomposes the thermosetting resin cured product in a decomposition vessel 3 at a temperature of >=200 deg.C to decompose the thermosetting resin cured product, and conducts a water distilling step of distilling water by heating the article 1 prior to the decomposition step.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、強度および耐熱性
に優れ、工業材料に広く利用されている熱硬化性組成物
を結合剤として用いた製品の分解処理方法に関するもの
である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for decomposing a product using, as a binder, a thermosetting composition which is excellent in strength and heat resistance and widely used for industrial materials.

【0002】[0002]

【従来の技術】従来から、不飽和ポリエステル樹脂、エ
ポキシ樹脂およびフェノール樹脂などの熱硬化性樹脂
は、無機物質などの充填材や添加剤の配合、繊維による
強化が容易なことから、成形材料、積層板、接着剤およ
び塗料などに応用されている。この熱硬化性樹脂は、硬
化反応により架橋して三次元化し、一般的には不溶不融
の固体となる。このため、熱硬化性樹脂硬化物の分解処
理は困難であり、再生処理および再使用には不適なもの
として廃棄されていた。
2. Description of the Related Art Conventionally, thermosetting resins such as unsaturated polyester resins, epoxy resins and phenolic resins are easy to mix with fillers and additives such as inorganic substances, and are easily reinforced by fibers. It is applied to laminates, adhesives and paints. This thermosetting resin is cross-linked into a three-dimensional shape by a curing reaction, and generally becomes an insoluble and infusible solid. For this reason, it is difficult to decompose the cured thermosetting resin, and it has been discarded as unsuitable for regeneration treatment and reuse.

【0003】ところが、近年廃棄物問題が注目されるに
つれて、熱硬化性樹脂硬化物の再利用および再資源化の
ための技術開発が必要とされ、熱分解による原料化など
が検討され始めた。例えば、繊維強化不飽和ポリエステ
ル樹脂などは、漁船、タンクおよび住宅用機材などの大
型製品の製造に多用されているため、廃棄物問題は深刻
である。しかし、熱硬化性樹脂硬化物の硬さ、強度、耐
熱性、難燃性および耐薬品性などの利点が、廃棄物処理
を技術的な面から困難にしているという問題があった。
However, as the problem of waste has been attracting attention in recent years, it has become necessary to develop a technique for recycling and recycling thermoset resin cured products, and the use of raw materials by thermal decomposition has begun to be studied. For example, fiber-reinforced unsaturated polyester resins and the like are frequently used in the production of large products such as fishing boats, tanks, and housing equipment, and the waste problem is serious. However, there has been a problem that advantages such as hardness, strength, heat resistance, flame retardancy and chemical resistance of the cured thermosetting resin have made the disposal of waste difficult from a technical point of view.

【0004】また、熱硬化性樹脂は高強度的であること
から構造材として使われることが多いが、さらに金属な
どの材料を包含している場合も多々見受けられる。この
金属などは、熱硬化性樹脂よりも高価であるため、その
再生および再利用の重要性が大きいといえる。しかし、
エポキシ樹脂およびフェノール樹脂などを結合材とする
銅張積層板およびIC(集積回路)モールドは、小型で
あるにも関わらず、紙、繊維などの他、銅、金および銀
などの貴金属を含んでいる。すなわち、熱硬化性樹脂の
分解処理とともに金属の分離が求められている。
[0004] Further, thermosetting resins are often used as structural materials because of their high strength, but are often found to further include materials such as metals. Since such metals and the like are more expensive than thermosetting resins, it can be said that their importance in recycling and reuse is great. But,
Despite their small size, copper-clad laminates and IC (integrated circuit) molds using epoxy resin and phenolic resin as binders contain noble metals such as copper, gold and silver, in addition to paper and fibers. I have. That is, separation of metal is required together with decomposition treatment of the thermosetting resin.

【0005】このような状況に対して、特開2000−
198877号公報では熱硬化性樹脂を含む製品を分解
槽内において熱硬化性樹脂を分解し得る溶剤を含む分解
液に接触させる工程、前記分解液を250℃以上でかつ
前記溶剤の臨界温度未満の温度に加熱する工程を含む分
解処理方法が開示されている。この技術は、熱硬化性樹
脂硬化物を含む製品を前記溶剤を含む分解液に接触させ
ることによって、熱硬化性樹脂硬化物の主鎖および/ま
たは三次元架橋鎖を切断する。熱硬化性樹脂硬化物が分
解されることによって熱硬化性樹脂の結合材としての機
能は低下して崩壊する。すなわち、熱硬化性樹脂硬化物
は、硬化により束縛していた充填材、基材、添加剤など
を保持できなくなり、熱硬化性樹脂成分と、その他の成
分との分離が容易となる。この技術によって、製品の減
容化を行ったり金属を分離回収したりすることが可能に
なる。
In such a situation, Japanese Patent Laid-Open No. 2000-2000
In 198877, a step of contacting a product containing a thermosetting resin with a decomposition solution containing a solvent capable of decomposing the thermosetting resin in a decomposition tank, wherein the decomposition solution is at least 250 ° C. and less than the critical temperature of the solvent. A decomposition treatment method including a step of heating to a temperature is disclosed. In this technique, a main chain and / or a three-dimensional crosslinked chain of a cured thermosetting resin is cut by bringing a product containing the cured thermosetting resin into contact with a decomposition solution containing the solvent. When the cured thermosetting resin is decomposed, the function of the thermosetting resin as a binder decreases and collapses. That is, the cured thermosetting resin cannot retain the filler, the base material, the additives, and the like bound by the curing, and the separation of the thermosetting resin component from other components becomes easy. This technology makes it possible to reduce the volume of products and to separate and recover metals.

【0006】[0006]

【発明が解決しようとする課題】しかし、使用済み製品
や工程で不良品として発生した製品であるため、回収さ
れる過程で製品に水分を含んでしまう場合も多く、ま
た、製品にフェノール樹脂など熱分解の過程で水を生成
する場合もある。このような場合、特開2000−19
8877号公報で開示されている方法では分解液を25
0℃以上で加熱する工程を含むため、生成した水によっ
て分解槽内の圧力が急激に上昇してその取扱いが困難に
なる課題があった。
However, since these products are used products or products generated as defective products in the process, they often contain water in the process of being recovered, and the products often contain phenolic resin or the like. In some cases, water is produced during the pyrolysis process. In such a case, JP-A-2000-19
In the method disclosed in Japanese Patent No. 8877, 25
Since the method includes a step of heating at 0 ° C. or higher, there is a problem that the pressure in the decomposition tank rapidly increases due to the generated water, and the handling becomes difficult.

【0007】以上のような事実に鑑み、本発明は、熱硬
化性樹脂硬化物を含む製品から、熱硬化性樹脂およびそ
の他の構成要素を再利用および再資源化するために、分
解反応時の分解槽の圧力上昇を抑えることで熱硬化性樹
脂硬化物を含む製品の簡易な分解処理方法を提供するこ
とを目的とする。
[0007] In view of the above facts, the present invention provides a method for reusing and recycling thermosetting resin and other components from a product containing a cured thermosetting resin. An object of the present invention is to provide a simple decomposition treatment method for a product containing a cured thermosetting resin by suppressing a pressure increase in a decomposition tank.

【0008】[0008]

【課題を解決するための手段】本発明は、熱硬化性樹脂
硬化物を含む製品と前記熱硬化性樹脂硬化物を分解する
分解材料とを分解槽内で200℃以上の温度で接触させ
て前記熱硬化性樹脂硬化物を分解する分解工程を含む分
解処理方法であって、前記製品を100℃以上に加熱し
て水分を留去する水分留去工程を前記分解工程の前に行
うことを特徴とする熱硬化性樹脂硬化物を含む製品の分
解処理方法によって上記目的を達成した。
According to the present invention, a product containing a cured thermosetting resin is brought into contact with a decomposition material for decomposing the cured thermosetting resin at a temperature of 200 ° C. or more in a decomposition tank. A decomposition treatment method comprising a decomposition step of decomposing the cured thermosetting resin, wherein a water distillation step of distilling water by heating the product to 100 ° C. or higher is performed before the decomposition step. The above object has been achieved by a method for decomposing a product containing a cured thermosetting resin.

【0009】また、本発明は、熱硬化性樹脂硬化物を含
む製品と前記熱硬化性樹脂硬化物を分解する分解材料と
を分解槽内で200℃以上の温度で接触させて前記熱硬
化性樹脂硬化物を分解する分解工程を含む分解処理方法
であって、前記分解槽内に水との共沸混合物形成物質を
添加して前記分解槽内で発生した水分を留去することを
特徴とする熱硬化性樹脂硬化物を含む製品の分解処理方
法によって上記目的を達成した。
Further, the present invention relates to a thermosetting resin, wherein a product containing a cured thermosetting resin is brought into contact with a decomposition material for decomposing the thermosetting resin at a temperature of 200 ° C. or more in a decomposition tank. A decomposition treatment method including a decomposition step of decomposing a resin cured product, characterized in that an azeotropic mixture-forming substance with water is added to the decomposition tank and water generated in the decomposition tank is distilled off. The object has been achieved by a method for decomposing a product containing a cured thermosetting resin.

【0010】また、本発明は、熱硬化性樹脂硬化物を含
む製品と前記熱硬化性樹脂硬化物を分解する分解材料と
を分解槽内で200℃以上の温度で接触させて前記熱硬
化性樹脂硬化物を分解する分解工程を含む分解処理方法
であって、水分吸収剤によって前記分解槽内で発生した
水分を吸収除去することを特徴とする熱硬化性樹脂硬化
物を含む製品の分解処理方法によって上記目的を達成し
た。
[0010] The present invention also relates to a thermosetting resin, wherein a product containing a cured thermosetting resin is brought into contact with a decomposition material for decomposing the cured thermosetting resin at a temperature of 200 ° C or higher in a decomposition tank. A decomposition treatment method including a decomposition step of decomposing a resin cured product, wherein a moisture absorbent absorbs and removes moisture generated in the decomposition tank, wherein the product contains a thermosetting resin cured product. The above object was achieved by the method.

【0011】[0011]

【発明の実施の形態】まず、本発明の対象である熱硬化
性樹脂硬化物を含む製品について説明する。本発明の分
解処理方法に供される熱硬化性樹脂硬化物を含む製品
は、熱硬化性樹脂を結合材としている。すなわち、熱硬
化性樹脂を充填材、基材および添加物などと複合化し、
熱硬化性樹脂の硬化反応により硬化したものである。
DESCRIPTION OF THE PREFERRED EMBODIMENTS First, a product containing a cured thermosetting resin which is an object of the present invention will be described. The product containing the cured thermosetting resin to be subjected to the decomposition treatment method of the present invention uses the thermosetting resin as a binder. That is, the thermosetting resin is compounded with the filler, the base material and the additives,
It is cured by a curing reaction of a thermosetting resin.

【0012】このような熱硬化性樹脂としては、例えば
不飽和ポリエステル樹脂、フェノール樹脂、エポキシ樹
脂、ポリウレタン樹脂、メラミン樹脂、ユリア樹脂など
があげられる。これらの熱硬化性樹脂の製造方法および
条件には特に制限はない。例えば、モノマー成分の重合
比なども任意である。
Examples of such a thermosetting resin include unsaturated polyester resin, phenol resin, epoxy resin, polyurethane resin, melamine resin, urea resin and the like. The production method and conditions for these thermosetting resins are not particularly limited. For example, the polymerization ratio of the monomer components is also arbitrary.

【0013】不飽和ポリエステル樹脂を結合材として用
いる製品の例としては、充填材、増粘剤、離型剤、ワッ
クス、着色剤などを加えたBMC(bulk Molding Compo
und)、SMC(Sheet Molding Compound)などの成形
品、ガラスなどのフレークや繊維などを加えたライニン
グ材、ワックスなどを加えた塗料、充填材などを加えた
パテ、骨材、充填材などを加えたレジンコンクリート、
充填材、顔料などを加えた人工大理石、発泡剤などを加
えた発泡体、硬化促進剤、安定剤などを加えた接着剤な
どがあげられる。また、熱硬化性樹脂はバルク状の成形
材料として用いられていてもよく、シート状のSMC、
または粒状のPMC(Pelletized typeMolding Compoun
d)であってもよい。
[0013] Examples of products using an unsaturated polyester resin as a binder include BMC (bulk molding compo- tor) containing a filler, a thickener, a release agent, a wax, a coloring agent, and the like.
und), molding products such as SMC (Sheet Molding Compound), lining materials including glass and other flakes and fibers, paints including wax, putty including fillers, aggregates, fillers, etc. Resin concrete,
Examples include artificial marble to which fillers and pigments are added, foams to which foaming agents are added, and adhesives to which curing accelerators, stabilizers and the like are added. Further, the thermosetting resin may be used as a bulk molding material, and a sheet-like SMC,
Or granular PMC (Pelletized typeMolding Compoun
d).

【0014】ユリア樹脂、メラミン樹脂、ポリウレタン
樹脂を結合材として用いた製品としても、不飽和ポリエ
ステル樹脂と同様に充填材、基材、添加物などが加えら
れた成型品、接着剤、塗料などがあげられる。
Products using a urea resin, a melamine resin, or a polyurethane resin as a binder include moldings, adhesives, paints, etc. to which fillers, base materials, additives, etc. are added in the same manner as the unsaturated polyester resin. can give.

【0015】また、フェノール樹脂、エポキシ樹脂、不
飽和ポリエステル樹脂およびポリイミドなどの熱硬化性
樹脂を結合材とする製品の例としては、上記結合材とす
る樹脂硬化物と同様の製品以外に、ガラス繊維、ポリア
ミド繊維、アラミド繊維、アクリル繊維もしくはポリエ
ステル繊維の織布または不織布、綿布、アスベストなど
を基材とし、それに各樹脂成分を含浸させて得られたプ
リプレグを積層成形した樹脂積層品などがあげられる。
この樹脂積層品は、さらに接着剤を塗布した銅箔を乗せ
て積層成形すれば銅張積層板となる場合もある。また、
導体パターンを形成したプリント配線板や、さらにプリ
ント配線板に電子部品を装着したプリント回路板であっ
てもよい(本発明では、銅張積層板、プリント配線板、
プリント回路板を含めてプリント基板という表現を用い
る)。これらの場合、本発明の分解処理方法により、積
層板部分の熱硬化性樹脂のみならず、レジスト部分や部
品に使用されている熱硬化性樹脂についても同様に分解
される。
Examples of products using a thermosetting resin such as a phenol resin, an epoxy resin, an unsaturated polyester resin, and polyimide as a binder include, in addition to the same products as the above-mentioned cured resin used as a binder, glass products. Resin laminates obtained by laminating prepregs obtained by impregnating each resin component with woven or non-woven fabric, cotton cloth, asbestos, etc. of fibers, polyamide fibers, aramid fibers, acrylic fibers or polyester fibers Can be
This resin laminate may be a copper-clad laminate if further laminated with a copper foil coated with an adhesive. Also,
It may be a printed wiring board on which a conductor pattern is formed, or a printed circuit board further mounted with electronic components on the printed wiring board (in the present invention, a copper-clad laminate, a printed wiring board,
The expression printed circuit board is used, including printed circuit boards.) In these cases, according to the decomposition treatment method of the present invention, not only the thermosetting resin in the laminated board portion but also the thermosetting resin used in the resist portion and components are similarly decomposed.

【0016】本発明の分解処理の対象となる製品として
は、例えば浴槽、便槽、貯水槽および洗面台などの建設
資材、椅子、机および家具などの家庭用品、タイル、人
工大理石およびパイプなどの土木資材、船舶、自動車、
鉄道および航空機などの輸送機器のボディや部品、住宅
機器、化粧板ならびに装飾品などがあげられる。また、
これらの製品における熱硬化性樹脂の形態および形状な
どにも制限はなく、塗料、パテおよび接着剤などとして
用いられていてもよい。また、テレビ、ステレオ、電子
レンジ、ファクシミリなどの使用済みの家電製品や、部
品としてはプリント基板、銅および鉄からなる巻線およ
び芯材などの金属部材を含むモールドモータ、モールド
トランス、半導体素子やリードフレームなどが熱硬化性
樹脂で封止されたIC部品などのモールド電子部品など
幅広く適用できる。特に、プリント基板には多種類の部
品が実装されて多種類の金属成分や樹脂成分を含み、ま
た、環境負荷物質である鉛などの重金属を含有するた
め、金属材料を効率的に分離できる本発明の適用が有効
である。この場合、プリント基板を含んだ機器や、機器
から抜き取られたプリント基板、製造工程で発生するプ
リント基板などが対象となる。樹脂積層板に銅箔が張ら
れた銅張積層板、銅張積層板にプリント配線が施された
プリント配線板、およびプリント配線板に部品が実装さ
れたプリント回路板のいずれもが本発明の対象である。
The products to be subjected to the decomposition treatment of the present invention include, for example, construction materials such as bathtubs, toilet tubs, water tanks and wash basins, household goods such as chairs, desks and furniture, tiles, artificial marbles and pipes. Civil engineering materials, ships, automobiles,
Examples include bodies and parts of transportation equipment such as railways and aircraft, housing equipment, decorative boards, and decorative articles. Also,
The form and shape of the thermosetting resin in these products are not limited, and may be used as paints, putties, adhesives and the like. In addition, used home appliances such as televisions, stereos, microwave ovens, and facsimile machines, and parts include printed circuit boards, molded motors including metal members such as windings and cores made of copper and iron, molded transformers, semiconductor elements, The present invention can be widely applied to molded electronic components such as IC components in which a lead frame or the like is sealed with a thermosetting resin. In particular, since various types of components are mounted on the printed circuit board and contain various types of metal components and resin components, and also contain heavy metals such as lead, which is an environmentally harmful substance, it is possible to efficiently separate metal materials. The application of the invention is effective. In this case, a target includes a device including a printed circuit board, a printed circuit board extracted from the device, a printed circuit board generated in a manufacturing process, and the like. The copper clad laminate in which copper foil is clad in a resin laminate, a printed wiring board in which printed wiring is applied to a copper clad laminate, and a printed circuit board in which components are mounted on a printed wiring board are all of the present invention. The subject.

【0017】分解材料には、熱硬化性樹脂を分解する材
料ならば特に限定はないが、Fedorsによって示さ
れている溶解パラメータ(Polymer Engen
eering Science 14巻 147頁 1
974年)の値が18(MJ/m31/2以上である溶剤
を含んでいれば、熱硬化性樹脂を分解する効果が大きく
好ましい。例えば、炭化水素、アルコール類、ケトン
類、エーテル類、エステル類、カーボネート類、フェノ
ール類、有機酸類、あるいは酸無水物類などが用いられ
る。使用後の分解材料の廃棄方法として焼却処理を考え
た場合、分解材料は炭素、水素、酸素のみから構成され
ていることが焼却処理における排ガス処理の負担を軽減
できる点から好ましい。また、分解工程における分解材
料の蒸気圧を上昇することを考慮して、分解材料の沸点
は140℃以上の蒸気圧の低い材料が好ましい。
The decomposition material is not particularly limited as long as it is a material that decomposes the thermosetting resin, and the decomposition parameter (Polymer Engen) indicated by Fedors is used.
eering Science Vol.14 p.147 p.1
(974) is not less than 18 (MJ / m 3 ) 1/2, which is preferable because the effect of decomposing the thermosetting resin is large. For example, hydrocarbons, alcohols, ketones, ethers, esters, carbonates, phenols, organic acids, or acid anhydrides are used. When incineration is considered as a method of disposing of the decomposed material after use, it is preferable that the decomposed material is composed of only carbon, hydrogen, and oxygen from the viewpoint of reducing the burden of exhaust gas treatment in the incineration process. Further, in consideration of increasing the vapor pressure of the decomposition material in the decomposition step, a material having a low vapor pressure of 140 ° C. or higher is preferable.

【0018】また、分解材料には、上記材料の他に、分
解材料および前記製品が含有する金属などの酸化劣化を
より確実に防ぐために、酸化防止剤または還元剤を含む
のが好ましい。このような酸化防止剤または還元剤とし
ては、分解材料に対する溶解性が良好であり、分解材料
および金属の酸化(劣化)を防止する防止の効果が高い
という理由から、例えばヒドロキノン、メトキノン、ベ
ンゾキノン、ナフトキノン、ブチルカテコール、ブチル
ヒドロキノン、次亜リン酸ナトリウム、チオ硫酸ナトリ
ウムおよびアスコルビン酸よりなる群から選択される少
なくとも1種があげられる。また、これらのなかでも、
酸化防止能に優れるという点から、ヒドロキノン、メト
キノンが好ましい。これら酸化防止剤または還元剤は、
酸化防止機能および還元機能を発揮するという点から、
分解材料中の溶剤100重量部に対して0.2〜10重
量部であればよいが、さらに、分解材料の溶解安定性と
いう点から、1〜5重量部であるのが好ましい。
The decomposed material preferably contains an antioxidant or a reducing agent, in addition to the above-mentioned materials, in order to more reliably prevent the oxidative deterioration of the decomposed material and the metal contained in the product. As such an antioxidant or a reducing agent, for example, hydroquinone, methoquinone, benzoquinone, and the like are preferable because they have good solubility in decomposed materials and a high effect of preventing oxidation (deterioration) of decomposed materials and metals. Examples include at least one selected from the group consisting of naphthoquinone, butylcatechol, butylhydroquinone, sodium hypophosphite, sodium thiosulfate, and ascorbic acid. Also, among these,
Hydroquinone and methoquinone are preferred because of their excellent antioxidant ability. These antioxidants or reducing agents are
In terms of exhibiting antioxidant and reducing functions,
The amount may be 0.2 to 10 parts by weight with respect to 100 parts by weight of the solvent in the decomposed material, but is preferably 1 to 5 parts by weight from the viewpoint of the dissolution stability of the decomposed material.

【0019】本発明では、熱硬化性樹脂硬化物を含む製
品と分解材料とを接触は200℃以上の温度で行う。接
触時の温度は高い方が大きな分解反応速度を得るが、温
度が高すぎると、圧力が高くなりすぎて分解槽に高耐圧
性が必要となること、分解によって発生するガス量が多
くなってその回収が困難になること、および分解材料の
分解も起こりうることから、分解材料の温度は分解材料
の臨界温度未満であるのが好ましい。
In the present invention, the contact between the product containing the cured thermosetting resin and the decomposed material is performed at a temperature of 200 ° C. or higher. The higher the temperature at the time of contact, the higher the decomposition reaction rate is obtained, but if the temperature is too high, the pressure will be too high and a high pressure resistance is required for the decomposition tank, and the amount of gas generated by decomposition will increase. The temperature of the decomposed material is preferably lower than the critical temperature of the decomposed material because its recovery becomes difficult and decomposition of the decomposed material can occur.

【0020】熱硬化性樹脂硬化物を含む製品と分解材料
とを接触には、分解材料が液相の状態で接触させる場
合、および気相の状態で接触させる場合のいずれの状態
でも構わない。液相状態で接触させる場合には、分解材
料の液相中に直接製品を浸漬したり、あるいは分解材料
の液を製品に吹き付けたりする。一方、気相状態で接触
させる場合には、製品と分解材料の液相部分と離して配
置して分解材料の蒸気を含む雰囲気下に製品をさらした
り、あるいは分解材料の蒸気を製品に吹き付けたりす
る。
The product containing the cured thermosetting resin and the decomposed material may be brought into contact with each other in either a case where the decomposed material is brought into contact in a liquid phase or a case where the decomposed material is brought into contact in a gas phase. When the contact is made in the liquid phase, the product is directly immersed in the liquid phase of the decomposition material, or a liquid of the decomposition material is sprayed on the product. On the other hand, when contacting in the gaseous phase, the product is separated from the liquid phase of the decomposition material and the product is exposed to an atmosphere containing the decomposition material vapor, or the decomposition material vapor is sprayed on the product. I do.

【0021】本発明の分解材料は、高温での安定性が高
く、また自らの分解により酸素を発生させることや、樹
脂硬化物が含有する金属類などの酸化を誘発することが
まれであるので、酸素排除などの前処理工程を必ずしも
必要としない。しかし、樹脂硬化物に含有される金属な
どのわずかな酸化が問題となる場合や、分解材料の寿命
をより長くするためには、酸素排除などの前処理工程を
設けることもできる。すなわち、熱硬化性樹脂硬化物を
含む製品と分解材料とを接触させる前に、分解槽内の酸
素を排除するのが好ましい。この工程は常法により実施
できるが、例えば前記製品および分解材料を仕込んだ分
解槽にガス導入管および排気バルブを設け、窒素ガスボ
ンベから直接送気すればよい。また、減圧して分解槽内
の気体を排気してもよい。減圧するには、例えば前記製
品および分解液を仕込んだ分解槽に排気バルブを設け、
真空ポンプを配管して行えばよい。このときの減圧の程
度はできるだけ真空に近いほうが良い。好ましくは0.
001MPa以下である。さらに、いずれの方法におい
ても、分解材料を攪拌したり、適度に加温したりするこ
とによって酸素排除の効率を上げることができる。好ま
しくは、これらの方法を両方とも採用し、前記分解槽内
の酸素を排気できればどのような方法で行っても構わな
いが、例えば前記分解槽内の気体を窒素ガスで置換し、
ついで窒素ガスを排気して前記分解槽内を減圧するのが
よい。このように、酸素排除の前処理の後に分解処理を
行うことにより、高温反応処理時の主な分解液劣化原因
である酸化を防ぎ、分解液の寿命を延ばし、繰り返し使
用性を向上させる。さらに前記製品に含まれる金属類な
どの酸化劣化なども防止し、分離回収される材料の品質
も向上させることができる。
The decomposition material of the present invention has high stability at high temperatures and rarely generates oxygen by its own decomposition and induces oxidation of metals and the like contained in the cured resin. However, a pretreatment step such as oxygen elimination is not necessarily required. However, in cases where slight oxidation of metals or the like contained in the cured resin becomes a problem, or in order to prolong the life of the decomposed material, a pretreatment step such as oxygen exclusion may be provided. That is, it is preferable to eliminate oxygen in the decomposition tank before bringing the product containing the cured thermosetting resin into contact with the decomposition material. This step can be performed by a conventional method. For example, a gas introduction pipe and an exhaust valve may be provided in a decomposition tank charged with the product and the decomposition material, and the gas may be directly supplied from a nitrogen gas cylinder. Further, the gas in the decomposition tank may be exhausted by reducing the pressure. To reduce the pressure, for example, an exhaust valve is provided in a decomposition tank charged with the product and the decomposition solution,
What is necessary is just to pipe | connect a vacuum pump. The degree of pressure reduction at this time is preferably as close to vacuum as possible. Preferably 0.
001 MPa or less. Furthermore, in any of the methods, the efficiency of oxygen exclusion can be increased by stirring the decomposition material or heating it appropriately. Preferably, both of these methods are employed, and any method may be used as long as oxygen in the decomposition tank can be exhausted.For example, the gas in the decomposition tank is replaced with nitrogen gas.
Next, the inside of the decomposition tank is preferably depressurized by exhausting nitrogen gas. As described above, by performing the decomposition treatment after the pretreatment for removing oxygen, oxidation, which is the main cause of degradation of the decomposition liquid during the high-temperature reaction treatment, is prevented, the life of the decomposition liquid is extended, and the reusability is improved. Further, it is possible to prevent the deterioration of metals contained in the product by oxidation and the like, and to improve the quality of materials separated and recovered.

【0022】(実施の形態1)本発明の実施の形態1に
ついて説明する。
(Embodiment 1) Embodiment 1 of the present invention will be described.

【0023】本発明の実施の形態1は、対象とする製品
の回収過程などで製品に水分を含んだり、熱分解過程で
脱水反応によって水を生成する材料(フェノール樹脂な
ど)を製品に含んだりする場合に特に効果がある。分解
工程は200℃以上の温度で行われるため水分の蒸気圧
はかなり高くなり、分解槽として密閉容器を用いた場合
には200℃以上の温度で行う分解工程で分解槽内の圧
力は急激に上昇するため取扱い上好ましくなかった。ま
た、分解槽に還流塔を設けることで、水分は還流塔で還
流され分解槽内の圧力上昇は抑えられるが、水の沸点が
100℃と分解工程が温度200℃に対して充分に低い
ため、還流塔で凝縮落下した水は加熱された分解槽内で
局所的に急激に気化して分解槽内の状態が不安定になり
好ましくなかった。
In the first embodiment of the present invention, the product contains moisture in the recovery process of the target product or the like, or contains a material (such as a phenol resin) that generates water by a dehydration reaction in the pyrolysis process. It is especially effective when you do. Since the decomposition step is performed at a temperature of 200 ° C. or higher, the vapor pressure of water becomes considerably high. When a closed vessel is used as the decomposition tank, the pressure in the decomposition tank is rapidly increased in the decomposition step performed at a temperature of 200 ° C. or higher. Because of the rise, it was not preferable in handling. In addition, by providing a reflux tower in the decomposition tank, the water is refluxed in the reflux tower and the pressure rise in the decomposition tank is suppressed, but the boiling point of water is 100 ° C. and the decomposition step is sufficiently lower than the temperature of 200 ° C. However, water condensed and dropped in the reflux tower evaporates locally in the heated decomposition tank, and the state in the decomposition tank becomes unstable, which is not preferable.

【0024】本発明の実施の形態1の構成では、製品に
含まる水分は100℃以上から短時間で蒸発し、一方、
熱分解で生成する水も300℃までに短時間に発生する
ことに着眼して、前記製品を100℃以上に加熱して水
分を留去する水分留去工程を前記分解工程の前に行う。
分解槽を100℃以上に加熱しながら、水分を凝縮させ
ずに大気へ排出させて水分留去工程を行う。水分留去工
程での水分が排出される温度が分解材料の沸点よりも低
い場合には、分解槽内に製品と共に分解材料を投入して
水分留去工程を行える。一方、水分留去工程で水分が排
出される温度が分解材料の沸点よりも高い場合には、分
解槽内に製品のみを投入して水分留去工程を行い、その
後分解材料を投入して分解工程を行うことが望ましい。
In the configuration of the first embodiment of the present invention, the moisture contained in the product evaporates in a short time from 100 ° C. or higher, while
In view of the fact that water generated by thermal decomposition is also generated up to 300 ° C. in a short time, a water distilling step of heating the product to 100 ° C. or more to distill water is performed before the decomposing step.
While the decomposition tank is heated to 100 ° C. or higher, the water is discharged to the atmosphere without condensing the water to perform a water distillation step. When the temperature at which water is discharged in the water removal step is lower than the boiling point of the decomposition material, the decomposition material can be charged together with the product into the decomposition tank to perform the water removal step. On the other hand, if the temperature at which water is discharged in the water distillation step is higher than the boiling point of the decomposition material, only the product is put into the decomposition tank to perform the water distillation step, and then the decomposition material is charged to decompose. It is desirable to perform a step.

【0025】なお、図1ではバルブ9を閉じることで分
解槽3は密閉容器となるが、還流塔を分解槽3に設ける
構成でも適用可能である。
In FIG. 1, the decomposition tank 3 becomes a closed vessel by closing the valve 9. However, a configuration in which a reflux tower is provided in the decomposition tank 3 is also applicable.

【0026】実施例を図1に示すような構成で行った。
熱硬化性樹脂硬化物を含む製品1として、紙を基材とし
てフェノール樹脂および銅箔を積層硬化させ、導体パタ
ーンを形成したプリント配線板に電子部品が実装された
プリント回路板を用いた。分解材料2としてトリエチル
ビフェニル(沸点340℃)を用いた。水分除去工程と
して、製品1のみを分解槽3へ投入して加熱手段4で製
品1の温度が280℃に加熱しながら10分間保持し
た。この時、バルブ6は開放しており、フェノール樹脂
から熱分解で生成した水分を分解槽3から系外へ排出さ
せることができた。水分除去工程が終了すると分解槽3
へ分解材料2を供給した。その後、バルブ6を閉じて分
解材料2の温度が300℃になるように加熱手段4で加
熱し1時間その温度を保持して分解工程を行った。分解
工程中は分解による水の生成がないため、分解槽3内の
圧力が急激に上昇することもなかった。その後、分解槽
を冷却して、処理されたプリント配線板を取り出したと
ころ、フェノール樹脂の大半はプリント回路板から分解
され、配線銅と電子部品を回収できた。
The embodiment was performed with the configuration as shown in FIG.
As a product 1 containing a cured thermosetting resin, a printed circuit board in which electronic components were mounted on a printed wiring board on which a conductive pattern was formed by laminating and curing a phenol resin and a copper foil using paper as a base material was used. As the decomposition material 2, triethylbiphenyl (boiling point: 340 ° C.) was used. In the water removing step, only the product 1 was put into the decomposition tank 3, and the temperature of the product 1 was kept at 280 ° C. by the heating means 4 for 10 minutes. At this time, the valve 6 was opened, and the water generated by thermal decomposition from the phenol resin could be discharged from the decomposition tank 3 to the outside of the system. When the water removal process is completed, the decomposition tank 3
The decomposition material 2 was supplied. Thereafter, the valve 6 was closed, the decomposition material 2 was heated by the heating means 4 so that the temperature of the decomposition material 2 became 300 ° C., and the temperature was maintained for 1 hour to perform the decomposition step. During the decomposition process, there was no generation of water due to the decomposition, so that the pressure in the decomposition tank 3 did not rise rapidly. After that, the decomposition tank was cooled and the treated printed wiring board was taken out. As a result, most of the phenol resin was decomposed from the printed circuit board, and the wiring copper and electronic components could be recovered.

【0027】(実施の形態2)本発明の実施の形態2に
ついて説明する。
(Embodiment 2) Embodiment 2 of the present invention will be described.

【0028】本実施の形態2は、実施の形態1と同様
に、対象とする製品の回収過程などで製品に水分を含ん
だり、熱分解過程で脱水反応によって水を生成する材料
(フェノール樹脂など)を製品に含んだりする場合に特
に効果がある。そこで、本実施の形態1では、熱硬化性
樹脂硬化物を含む製品と熱硬化性樹脂硬化物を分解する
分解材料とを分解槽内で200℃以上の温度で接触させ
て熱硬化性樹脂硬化物を分解する分解工程を含む分解処
理方法であって、分解槽内に水との共沸混合物形成物質
を添加して前記分解槽内で発生した水分を留去すること
を特徴とする製品の分解処理方法によって、発生する水
分を効率的に除去できる。
In the second embodiment, as in the first embodiment, a material containing water in a product recovery process or the like, or a material (such as a phenol resin) that generates water by a dehydration reaction in a thermal decomposition process, as in the first embodiment. ) Is particularly effective when included in products. Therefore, in the first embodiment, a product containing a cured thermosetting resin and a decomposition material that decomposes the cured thermosetting resin are brought into contact in a decomposition tank at a temperature of 200 ° C. or more to cure the thermosetting resin. A decomposition treatment method comprising a decomposition step of decomposing a substance, wherein an azeotropic mixture-forming substance with water is added to the decomposition tank to distill off water generated in the decomposition tank. The generated water can be efficiently removed by the decomposition method.

【0029】分解槽内に水との共沸混合物形成物質を添
加して、前記分解槽内で発生した水の沸点を下げて留去
する方法によって、発生した水分を除去することでき望
ましい。水との共沸混合物形成物質としては特に限定は
ないが、例えば、エタノール、メチルエチルケトン、酢
酸酸エチル、1,4−ジオキサン、2、5−ジメチルフラ
ン、トルエン、ヘキサン、ベンゼンなどが挙挙げられ
る。
It is desirable to add a substance forming an azeotrope with water into the decomposition tank and reduce the boiling point of the water generated in the decomposition tank to distill off the generated water. The substance forming an azeotrope with water is not particularly limited, and examples thereof include ethanol, methyl ethyl ketone, ethyl acetate, 1,4-dioxane, 2,5-dimethylfuran, toluene, hexane, and benzene.

【0030】実施例を図2示すような構成で行った。製
品1として、紙を基材としてフェノール樹脂および銅箔
を積層硬化させ、導体パターンを形成したプリント配線
板に電子部品が実装されたプリント回路板を用いた。分
解材料2としてエチルビフェニル(沸点286℃)を用
いた。製品1および分解材料2を分解槽3へ投入して加
熱手段4で製品1の温度が300℃に加熱しながら1時
間保持した。この間、製品1中のフェノール樹脂の分解
によって生成した水が還流管5で冷却凝縮して再び高温
の分解槽3へ戻る際に急激に凝縮した水が気化して分解
槽3内は不安定な状態が続いていた。そこで、水との共
沸混合物形成物質としてトルエンを共沸混合物形成物質
供給手段7より供給することで、水はトルエンと共に留
去されて分解槽3内の状態は安定した。その後、分解槽
を冷却して、処理されたプリント配線板を取り出したと
ころ、フェノール樹脂の大半はプリント回路板から分解
除去され、配線銅と電子部品を回収できた。
The embodiment was performed with the configuration as shown in FIG. As the product 1, a printed circuit board having electronic components mounted on a printed wiring board on which a conductive pattern was formed by laminating and curing a phenol resin and a copper foil using paper as a base material was used. Ethyl biphenyl (boiling point 286 ° C.) was used as decomposition material 2. The product 1 and the decomposition material 2 were put into the decomposition tank 3 and maintained for 1 hour while the temperature of the product 1 was heated to 300 ° C. by the heating means 4. During this time, when the water generated by the decomposition of the phenolic resin in the product 1 is cooled and condensed in the reflux pipe 5 and returns to the high-temperature decomposition tank 3 again, the rapidly condensed water vaporizes and the inside of the decomposition tank 3 becomes unstable. The situation had continued. Then, by supplying toluene as an azeotrope-forming substance with water from the azeotrope-forming substance supply means 7, the water was distilled off together with the toluene, and the state in the decomposition tank 3 was stabilized. Thereafter, the decomposition bath was cooled and the treated printed wiring board was taken out. As a result, most of the phenolic resin was decomposed and removed from the printed circuit board, and the wiring copper and electronic components could be recovered.

【0031】(実施の形態3)本発明の実施の形態3に
ついて説明する。
(Embodiment 3) Embodiment 3 of the present invention will be described.

【0032】本実施の形態3は、実施の形態2と同様
に、対象とする製品の回収過程などで製品に水分を含ん
だり、熱分解過程で脱水反応によって水を生成する材料
(フェノール樹脂など)を製品に含んだりする場合に特
に効果がある。そこで、本実施の形態3では、熱硬化性
樹脂硬化物を含む製品と前記熱硬化性樹脂硬化物を分解
する分解材料とを分解槽内で200℃以上の温度で接触
させて前記熱硬化性樹脂硬化物を分解する分解工程を含
む分解処理方法であって、水分吸収剤によって前記分解
槽内で発生した水分を吸収除去することを特徴とする製
品の分解処理方法によって、発生する水分を効率的に除
去できる。
In the third embodiment, similarly to the second embodiment, a material (such as phenolic resin) that contains water in a product in a recovery process of a target product or generates water by a dehydration reaction in a pyrolysis process. ) Is particularly effective when included in products. Therefore, in the third embodiment, a product containing a cured thermosetting resin and a decomposition material that decomposes the cured thermosetting resin are brought into contact with each other at a temperature of 200 ° C. or more in a decomposition tank to form the thermosetting resin. A decomposition treatment method including a decomposition step of decomposing a cured resin, wherein the water generated in the decomposition tank is absorbed and removed by a water absorbent, whereby the generated water is efficiently removed. Can be removed.

【0033】図3に例を示すように、水分を吸収除去す
る物質を格納した水分除去手段8を設けることで、分解
槽3内で発生した水分を吸収除去きる。水分を吸収除去
する物質としては、酸化カルシウム、塩化カルシウム、
硫酸ナトリウム、硫酸マグネシウム、硫酸カルシウム、
炭酸ナトリム、活性アルミナ、シリカゲル、モレキュラ
シーブなどが例として挙がられる。なお、図3では還流
塔5を用いているが、分解槽3として還流塔5を用いな
い密閉容器を用いた場合は分解槽3内に水分除去手段8
が設けられる。
As shown in FIG. 3, by providing a water removing means 8 containing a substance for absorbing and removing moisture, moisture generated in the decomposition tank 3 can be absorbed and removed. Substances that absorb and remove water include calcium oxide, calcium chloride,
Sodium sulfate, magnesium sulfate, calcium sulfate,
Examples include sodium carbonate, activated alumina, silica gel, and molecular sieve. Although the reflux tower 5 is used in FIG. 3, when a closed vessel without the reflux tower 5 is used as the decomposition tank 3, the water removing means 8 is provided in the decomposition tank 3.
Is provided.

【0034】実施例を図3示すような構成で行った。熱
硬化性樹脂硬化物を含む製品1として、紙を基材として
フェノール樹脂および銅箔を積層硬化させ、導体パター
ンを形成したプリント配線板に電子部品が実装されたプ
リント回路板を用いた。分解材料2としてテトラリン
(沸点208℃)を用いた。また、水分除去手段8には
酸化カルシウムを充填した。製品1全体が分解材料2の
液に接触する状態で両者を分解槽3に投入した後、加熱
手段4であるヒータで分解材料2が400℃になるよう
に加熱し1時間その温度を保持して分解工程を行った。
尚、水分除去手段8内の酸化カルシウムの温度は110
℃であった。分解工程中はフェノール樹脂から熱分解で
生成した水分は水分除去手段8で吸収されて分解槽3へ
凝縮落下する水がなかったため、局所的に水が急激に気
化することもなく分解槽3内の状態は安定していた。そ
の後、分解槽を冷却して、処理されたプリント配線板を
取り出したところ、フェノール樹脂の大半はプリント回
路板から分解除去され、配線銅と電子部品を回収でき
た。
The embodiment was performed with the configuration as shown in FIG. As a product 1 containing a cured thermosetting resin, a printed circuit board in which electronic components were mounted on a printed wiring board on which a conductive pattern was formed by laminating and curing a phenol resin and a copper foil using paper as a base material was used. As the decomposition material 2, tetralin (boiling point: 208 ° C.) was used. The water removing means 8 was filled with calcium oxide. After the whole product 1 is put into the decomposition tank 3 while being in contact with the liquid of the decomposition material 2, the decomposition material 2 is heated to 400 ° C. by the heater as the heating means 4 and maintained at that temperature for 1 hour. To perform a decomposition step.
The temperature of the calcium oxide in the water removing means 8 is 110
° C. During the decomposition step, the water generated by thermal decomposition from the phenolic resin was absorbed by the water removing means 8 and no water was condensed and dropped into the decomposition tank 3, so that the water did not evaporate locally in the decomposition tank 3. The state was stable. Thereafter, the decomposition bath was cooled and the treated printed wiring board was taken out. As a result, most of the phenolic resin was decomposed and removed from the printed circuit board, and the wiring copper and electronic components could be recovered.

【0035】本発明では、還流塔を用いて分解材料を還
流する場合には、非凝縮性ガスは還流塔を通じて分解槽
から排出されるため、分解槽3内から排出される非凝縮
性ガスを浄化する排ガス浄化手段を備えることが望まし
い。
In the present invention, when the decomposed material is refluxed using the reflux tower, the non-condensable gas discharged from the decomposition tank 3 is discharged from the decomposition tank through the reflux tower. It is desirable to have exhaust gas purifying means for purifying.

【0036】排ガス処理手段としては、排ガスの成分に
応じて、適宜従来から使用されている手段が用いられ
る。噴霧液体に排ガスを吸収させるスクラバーや、活性
炭などの吸着剤にガスを吸着させる吸着槽、液体中に排
ガスを噴出して吸収させる暴気槽などがあり、これらを
重複して用いることもできる。またガスの分解反応を行
せしめる分解反応炉を用いることができ、火炎燃焼や触
媒燃焼を用いた燃焼反応炉や、分解触媒を充填して希薄
ガスも反応させる触媒反応炉などがあり、使用条件や使
い勝手に応じて任意に選択して用いることができる。
As the exhaust gas treatment means, means conventionally used as appropriate according to the components of the exhaust gas is used. There are a scrubber for absorbing the exhaust gas into the spray liquid, an adsorption tank for adsorbing the gas to an adsorbent such as activated carbon, and a violent tank for ejecting and absorbing the exhaust gas into the liquid, and these can be used repeatedly. Decomposition reactors that can perform gas decomposition reactions can be used, and there are combustion reactors that use flame combustion or catalytic combustion, and catalytic reaction furnaces that fill a decomposition catalyst and also react lean gas. It can be arbitrarily selected and used according to the convenience.

【0037】本発明では分解槽から排出される非凝縮性
ガスは製品中に含まれる熱硬化性樹脂硬化物などの分解
反応の進行に応じて発生量が変動し、また、発生量自体
も比較的少量である。このため、排ガス処理手段として
ガス燃焼反応炉を用いて、還流塔と排ガス処理手段との
間にガス吸着手段およびそれを加熱する加熱手段を備え
ることで、発生した非凝縮性ガスを一旦ガス吸着手段で
所定量の非凝縮性ガスを吸着濃縮した後、加熱手段で脱
着反応を行いまとめて排ガス処理手段で非凝縮性ガスを
燃焼浄化することで、効率的に排ガス浄化が行われる。
ガス吸着手段としては活性炭やゼオライトなどの一般的
な吸着剤が用いられる。
In the present invention, the amount of the non-condensable gas discharged from the decomposition tank varies according to the progress of the decomposition reaction of the cured thermosetting resin contained in the product, and the amount of the generated gas itself is also compared. It is a very small amount. For this reason, by using a gas combustion reactor as the exhaust gas treatment means and providing a gas adsorption means and a heating means for heating it between the reflux tower and the exhaust gas treatment means, the generated non-condensable gas is once adsorbed by the gas. After a predetermined amount of non-condensable gas is adsorbed and concentrated by the means, the desorption reaction is performed by the heating means, and the non-condensable gas is combusted and purified by the exhaust gas treatment means, thereby efficiently purifying the exhaust gas.
As the gas adsorption means, a general adsorbent such as activated carbon or zeolite is used.

【0038】[0038]

【発明の効果】以上説明したように、本発明による分解
処理方法および分解装置を用いれば、分解反応時の分解
槽の圧力上昇を抑えながら、熱硬化性樹脂硬化物を含む
製品を容易に分解できる。
As described above, by using the decomposition method and the decomposition apparatus according to the present invention, it is possible to easily decompose the product containing the cured thermosetting resin while suppressing the pressure rise in the decomposition tank during the decomposition reaction. it can.

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

【図1】本発明の熱硬化性樹脂硬化物を含む製品の分解
処理装置の構成を示す概略図
FIG. 1 is a schematic diagram showing the configuration of a device for decomposing a product containing a thermosetting resin cured product of the present invention.

【図2】本発明の熱硬化性樹脂硬化物を含む製品の分解
処理装置の別の構成を示す概略図
FIG. 2 is a schematic diagram showing another configuration of a device for decomposing a product containing a cured thermosetting resin of the present invention.

【図3】本発明の熱硬化性樹脂硬化物を含む製品の分解
処理装置の別の構成を示す概略図
FIG. 3 is a schematic view showing another configuration of a device for decomposing a product containing a cured thermosetting resin of the present invention.

【符号の説明】[Explanation of symbols]

1 製品 2 分解材料 3 分解槽 4 加熱手段 5 還流塔 6 バルブ 7 水との共沸混合物形成物質供給手段 8 水分除去手段 DESCRIPTION OF SYMBOLS 1 Product 2 Decomposition material 3 Decomposition tank 4 Heating means 5 Reflux tower 6 Valve 7 Supply means of azeotrope-forming substance with water 8 Water removal means

───────────────────────────────────────────────────── フロントページの続き (72)発明者 寺田 貴彦 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 中島 啓造 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 大西 宏 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 Fターム(参考) 4D052 AA00 CE00 HA00 HA01 HA02 HA05 HA07 HA08 HA11 HA12 4D076 AA14 AA24 BB08 BC03 EA04Z EA12Z FA03 FA12 FA15 GA01 HA03 JA02 JA03 4F301 AA22 AA23 AA24 AA25 AA29 CA09 CA23 CA41 CA52 CA61 CA72  ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Takahiko Terada 1006 Kadoma Kadoma, Osaka Pref. Matsushita Electric Industrial Co., Ltd. 72) Inventor Hiroshi Onishi 1006 Kazuma Kadoma, Kadoma City, Osaka Prefecture F-term (reference) 4D052 AA00 CE00 HA00 HA01 HA02 HA05 HA07 HA08 HA11 HA12 4D076 AA14 AA24 BB08 BC03 EA04Z EA12Z FA03 FA12 FA15 GA03 HA03 JA02 4F301 AA22 AA23 AA24 AA25 AA29 CA09 CA23 CA41 CA52 CA61 CA72

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 熱硬化性樹脂硬化物を含む製品と前記熱
硬化性樹脂硬化物を分解する分解材料とを分解槽内で2
00℃以上の温度で接触させて前記熱硬化性樹脂硬化物
を分解する分解工程を含む分解処理方法であって、前記
製品を100℃以上に加熱して水分を留去する水分留去
工程を前記分解工程の前に行うことを特徴とする熱硬化
性樹脂硬化物を含む製品の分解処理方法。
1. A product containing a cured thermosetting resin and a decomposition material for decomposing the cured thermosetting resin are separated in a decomposition tank in a decomposition tank.
A decomposition treatment method comprising a decomposition step of decomposing the cured thermosetting resin by contacting at a temperature of 00 ° C. or higher, wherein the water distilling step of distilling water by heating the product to 100 ° C. or higher. A method for decomposing a product containing a cured thermosetting resin, which is performed before the decomposing step.
【請求項2】 熱硬化性樹脂硬化物を含む製品と前記熱
硬化性樹脂硬化物を分解する分解材料とを分解槽内で2
00℃以上の温度で接触させて前記熱硬化性樹脂硬化物
を分解する分解工程を含む分解処理方法であって、前記
分解槽内に水との共沸混合物形成物質を添加して前記分
解槽内で発生した水分を留去することを特徴とする熱硬
化性樹脂硬化物を含む製品の分解処理方法。
2. A product containing a thermosetting resin cured product and a decomposition material for decomposing the thermosetting resin cured product are separated in a decomposition tank.
A decomposition treatment method comprising a decomposition step of decomposing the cured thermosetting resin by contacting at a temperature of 00 ° C. or more, wherein an azeotrope-forming substance with water is added to the decomposition tank, A method for decomposing a product containing a cured thermosetting resin, wherein water generated in the product is distilled off.
【請求項3】 熱硬化性樹脂硬化物を含む製品と前記熱
硬化性樹脂硬化物を分解する分解材料とを分解槽内で2
00℃以上の温度で接触させて前記熱硬化性樹脂硬化物
を分解する分解工程を含む分解処理方法であって、水分
吸収剤によって前記分解槽内で発生した水分を吸収除去
することを特徴とする熱硬化性樹脂硬化物を含む製品の
分解処理方法。
3. A product containing a cured thermosetting resin and a decomposition material for decomposing the cured thermosetting resin are separated into two in a decomposition tank.
A decomposition treatment method comprising a decomposition step of decomposing the cured thermosetting resin by contacting at a temperature of 00 ° C. or higher, wherein water generated in the decomposition tank is absorbed and removed by a water absorbent. Of a product containing a cured thermosetting resin.
JP2000328560A 2000-10-27 2000-10-27 Process for decomposition treatment of article containing thermosetting resin cured product Pending JP2002128950A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000328560A JP2002128950A (en) 2000-10-27 2000-10-27 Process for decomposition treatment of article containing thermosetting resin cured product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000328560A JP2002128950A (en) 2000-10-27 2000-10-27 Process for decomposition treatment of article containing thermosetting resin cured product

Publications (1)

Publication Number Publication Date
JP2002128950A true JP2002128950A (en) 2002-05-09

Family

ID=18805393

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2002128950A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003026853A (en) * 2001-07-19 2003-01-29 Hitachi Chem Co Ltd Method for dissolving thermosetting composition
JP2009019141A (en) * 2007-07-13 2009-01-29 Hitachi Industrial Equipment Systems Co Ltd Recycle of electrical equipment
JP2010132915A (en) * 2010-01-22 2010-06-17 Hitachi Chem Co Ltd Processing liquid of resin
JP2010138402A (en) * 2010-01-22 2010-06-24 Hitachi Chem Co Ltd Method of processing resin
WO2017154101A1 (en) * 2016-03-08 2017-09-14 日立化成株式会社 Method for processing thermosetting resin cured product

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003026853A (en) * 2001-07-19 2003-01-29 Hitachi Chem Co Ltd Method for dissolving thermosetting composition
JP4590797B2 (en) * 2001-07-19 2010-12-01 日立化成工業株式会社 Method for dissolving thermosetting composition
JP2009019141A (en) * 2007-07-13 2009-01-29 Hitachi Industrial Equipment Systems Co Ltd Recycle of electrical equipment
JP2010132915A (en) * 2010-01-22 2010-06-17 Hitachi Chem Co Ltd Processing liquid of resin
JP2010138402A (en) * 2010-01-22 2010-06-24 Hitachi Chem Co Ltd Method of processing resin
WO2017154101A1 (en) * 2016-03-08 2017-09-14 日立化成株式会社 Method for processing thermosetting resin cured product

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