JPH05178977A - Method for treating molded polymer article - Google Patents
Method for treating molded polymer articleInfo
- Publication number
- JPH05178977A JPH05178977A JP36158091A JP36158091A JPH05178977A JP H05178977 A JPH05178977 A JP H05178977A JP 36158091 A JP36158091 A JP 36158091A JP 36158091 A JP36158091 A JP 36158091A JP H05178977 A JPH05178977 A JP H05178977A
- Authority
- JP
- Japan
- Prior art keywords
- lactic acid
- polymer
- molded article
- acid polymer
- molecular weight
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J11/00—Recovery or working-up of waste materials
- C08J11/04—Recovery or working-up of waste materials of polymers
- C08J11/10—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation
- C08J11/14—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by treatment with steam or water
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2367/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
- C08J2367/04—Polyesters derived from hydroxy carboxylic acids, e.g. lactones
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、廃棄物となるポリマー
成形品の処理方法に関する。更に詳しくは、ポリマー成
形品の分子量を低下させ、同時に形態を崩壊させること
により、ポリマー成形品の廃棄処理または再利用を便な
らしめるポリマー成形品の処理方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating a polymer molded article which is a waste. More specifically, the present invention relates to a method for treating a polymer molded article, which reduces the molecular weight of the polymer molded article and at the same time disintegrates the morphology, thereby facilitating disposal or reuse of the polymer molded article.
【0002】[0002]
【従来の技術】従来、主として乳酸ポリマーからなる成
形品について、廃棄処理または再利用を容易ならしめる
ような該成形品の簡易な処理方法は提案されていなかっ
た。ポリエステル化合物の処理法として、リパーゼによ
る加水分解法が提案されていたが、リパーゼのような酵
素剤は高価であると同時に反応時間が長く、また分解さ
れないポリエステルも多く存在し、このためポリエステ
ル成形品の廃棄処理、または再利用のための処理方法と
しては満足できるものではなかった。2. Description of the Related Art Heretofore, no simple treatment method has been proposed for a molded article mainly made of lactic acid polymer, which facilitates disposal or reuse of the molded article. As a method for treating a polyester compound, a hydrolysis method using lipase has been proposed, but an enzymatic agent such as lipase is expensive, has a long reaction time, and there are many polyesters which are not decomposed. Was not satisfactory as a disposal method for waste disposal or reuse.
【0003】またポリマー成形品を強熱下に熱分解する
処理方法は多数提案されてきたが、いずれも大がかりな
装置を必要とし、ポリマー成形品の処理方法としては不
十分なものであった。Although many treatment methods for thermally decomposing polymer molded articles under strong heat have been proposed, all of them require a large-scale apparatus and are insufficient as a method for treating polymer molded articles.
【0004】[0004]
【発明が解決しようとする課題】ポリマー成形品は、通
常容器等の内部に空間を有する形状に成形されているた
め、大きな容積を占め、使用後においても保管および輸
送の効率が悪かった。これを解決するため、機械的な力
によってポリマー成形品を破砕し、小さな空間に縮小す
る方法も提案されているが、簡便にポリマー成形品を粉
砕する装置がないため、現実には効率の悪い保管、輸送
を実施せざるを得なかった。Since a polymer molded article is usually molded into a shape having a space inside a container or the like, it occupies a large volume and is inefficient in storage and transportation even after use. In order to solve this, a method of crushing the polymer molded product by mechanical force and reducing it to a small space has also been proposed, but in reality there is no device for crushing the polymer molded product, so it is actually inefficient. I had no choice but to carry out storage and transportation.
【0005】主として乳酸ポリマーからなるプラスチッ
クスは、生分解性のあることが知られている。このた
め、これらのポリマーを埋め立て用に使用すると、微生
物によって分解され、消滅する場合がある。しかし多く
の場合、そのままでは分解せず、分解する場合でも、分
解消滅には長い年月を必要とするため、膨大な面積の埋
め立て地が必要である。It is known that plastics mainly composed of lactic acid polymer are biodegradable. Therefore, when these polymers are used for landfill, they may be decomposed by microorganisms and disappear. However, in many cases, it does not decompose as it is, and even if it decomposes, it takes a long time to decompose and disappear, so a huge landfill is required.
【0006】上記ポリマー成形品は、使用後の廃棄物を
焼却処分しようとすると、固形成形品のままでは局部的
に大量の酸素を必要とする。このため、通常の焼却炉で
固形成形品を燃焼させると、不完全燃焼となり、すすや
固まりで残ってしまう場合が多い。The above-mentioned polymer molded product locally requires a large amount of oxygen when the waste product after use is to be incinerated and disposed of as a solid molded product. For this reason, when a solid molded product is burned in an ordinary incinerator, incomplete combustion often occurs, and soot and solid residue often remain.
【0007】また主として乳酸ポリマーからなる成形品
は、加熱融解した場合、一部酸化分解するためそのまま
新たな成形品の原料として回収使用することは困難であ
る。しかしこれに対し酸化を防止しながら分子量を低下
させ、粉末または液状とすれば新たに合成原料とするこ
とができ、再び資源として回収利用することもできる。
即ち本発明は、上記ポリマー成形品を、簡便な方法で回
収使用できる方法の提供を目的とする。A molded product mainly composed of a lactic acid polymer is partially oxidized and decomposed when heated and melted, so that it is difficult to recover and use it as a raw material for a new molded product as it is. However, by reducing the molecular weight while preventing oxidation and making it into powder or liquid, it can be newly used as a synthetic raw material and can be recovered and used again as a resource.
That is, an object of the present invention is to provide a method for recovering and using the above-mentioned polymer molded product by a simple method.
【0008】[0008]
【課題を解決するための手段】本発明は、主として乳酸
ポリマーからなる成形品を、水分の存在下で100℃以
上、1気圧以上、好ましくは120℃以上、2気圧以上
に加熱加圧して該成形品を加水分解させることを特徴と
するポリマー成形品の処理方法を提供する。According to the present invention, a molded article mainly composed of a lactic acid polymer is heated and pressurized to 100 ° C or higher and 1 atm or higher, preferably 120 ° C or higher and 2 atm or higher in the presence of water. Provided is a method for treating a polymer molded article, which comprises hydrolyzing the molded article.
【0009】即ち本発明は、上記ポリマー成形品を、好
ましくは空気接触による酸化を防止できる密閉容器中
で、高温、高圧の水蒸気と接触させると、上記ポリマー
は加水分解し、低分子量化してペースト状あるいは粉末
状となることを見いだして完成された。That is, according to the present invention, when the above-mentioned polymer molded product is brought into contact with steam at high temperature and high pressure, preferably in a closed container capable of preventing oxidation by air contact, the polymer is hydrolyzed to have a low molecular weight and paste. It was completed by discovering that it will be in the form of powder or powder.
【0010】本発明において、主として乳酸ポリマーか
らなる成形品とは、乳酸ポリマー単独あるいは、乳酸ポ
リマーとポリグリコール酸との共重合体であるポリラク
チド類を主たるポリマー成分として有する成形品を意味
する。In the present invention, the term "molded product mainly composed of a lactic acid polymer" means a molded product having a polylactide which is a lactic acid polymer alone or a copolymer of a lactic acid polymer and polyglycolic acid as a main polymer component.
【0011】以下本発明を実施例に基づきより詳細に説
明する。 実施例1〜2、比較例1 試料1(実施例1): 直径4mm、長さ3mmのペレ
ット状に成形したL/D比95/5、重量平均分子量約
23万のポリ乳酸、 試料2(実施例2): 直径3mm、長さ4mmのペレ
ット状に成形したL/D比85/15、重量平均分子量
約20万のポリ乳酸、 試料3(比較例1): 厚さ1mmのシート状ポリプロ
ピレン、The present invention will be described in more detail based on the following examples. Examples 1 and 2, Comparative Example 1 Sample 1 (Example 1): Polylactic acid having an L / D ratio of 95/5 and a weight average molecular weight of about 230,000, which was molded into pellets having a diameter of 4 mm and a length of 3 mm, Sample 2 ( Example 2): Polylactic acid having an L / D ratio of 85/15 and a weight average molecular weight of about 200,000 formed into a pellet having a diameter of 3 mm and a length of 4 mm. Sample 3 (Comparative Example 1): 1 mm thick sheet-shaped polypropylene ,
【0012】試料1〜3をそれぞれ試験管に入れ、滅菌
用オートクレーブにて120℃、2気圧の水蒸気と1時
間接触させた。その結果、試料1および試料2のポリ乳
酸は、形状がかなり崩壊し、指でつまむだけで容易に粉
末になった。試料3のポリプロピレンは、形態の変化が
全く認められなかった。Each of Samples 1 to 3 was placed in a test tube and brought into contact with steam at 120 ° C. and 2 atm for 1 hour in a sterilizing autoclave. As a result, the polylactic acid of Sample 1 and Sample 2 had their shapes considerably disintegrated, and easily powdered by pinching them with fingers. No morphological change was observed in the polypropylene of Sample 3.
【0013】実施例3 試料として直径3mm、長さ4mmのペレット状に成形
した、L/D比85/15、重量平均分子量約20万の
ポリ乳酸を用い、温度の相違による水蒸気加水分解の程
度を調べた。Example 3 Polylactic acid having a L / D ratio of 85/15 and a weight average molecular weight of about 200,000, which was formed into a pellet having a diameter of 3 mm and a length of 4 mm, was used as a sample. I checked.
【0014】試料を4本の試験管に入れ、その内4本を
反応用オートクレーブに入れ、それぞれ120℃、2気
圧、140℃、3気圧、160℃、6気圧および180
℃、11気圧の水蒸気と1時間接触させた。処理後各試
料の形状を観察すると共に、テトラヒドロフラン(TH
F)に溶解してゲルパーミエイションクロマトグラフィ
ー(GPC)により平均分子量を調べた。Samples were placed in four test tubes, four of which were placed in a reaction autoclave, and each was placed at 120 ° C., 2 atm, 140 ° C., 3 atm, 160 ° C., 6 atm and 180 atm.
It was contacted with water vapor at 11 ° C. for 1 hour. After the treatment, the shape of each sample is observed, and tetrahydrofuran (TH
It melt | dissolved in F) and the average molecular weight was investigated by the gel permeation chromatography (GPC).
【0015】水蒸気処理した試料は、いずれも形状が崩
壊していた。160℃、180℃で処理した試料は指で
押すと容易に粉末となった。120℃、140℃で処理
した試料は、160℃、180℃で処理したものよりも
若干の強い力はいるものの指で押すと粉末になった。図
1にポリ乳酸の重量平均分子量の測定結果を示す。温度
が高い程重量平均分子量は低くなっている。The shape of all the steam-treated samples had collapsed. The samples treated at 160 ° C. and 180 ° C. easily became powders when pressed with a finger. The samples treated at 120 ° C. and 140 ° C. became powdery when pressed with a finger, although they had a slightly stronger force than those treated at 160 ° C. and 180 ° C. FIG. 1 shows the measurement results of the weight average molecular weight of polylactic acid. The higher the temperature, the lower the weight average molecular weight.
【0016】実施例4 試料として直径3mm、長さ4mmのペレット状に成形
した、L/D比85/15、重量平均分子量約20万の
ポリ乳酸を用い、処理時間の相違による水蒸気加水分解
の程度を調べた。試料をそれぞれ8本の試験管に入れ、
その内4本を120℃、水蒸気2気圧のオートクレーブ
で、他の4本を140℃、水蒸気3気圧のオートクレー
ブでそれぞれ15分間、30分間、60分間、90分間
水蒸気と接触させた。処理後各試料をTHFに溶解し、
GPCにより平均分子量を測定した。測定結果を図2に
示す。接触時間が長い程平均分子量は低下している。Example 4 Polylactic acid having a L / D ratio of 85/15 and a weight average molecular weight of about 200,000, which was formed into a pellet having a diameter of 3 mm and a length of 4 mm, was used as a sample, and was subjected to steam hydrolysis due to a difference in treatment time. I checked the degree. Put each sample into 8 test tubes,
Four of them were contacted with steam in an autoclave at 120 ° C. and 2 atm of steam, and the other four were contacted with steam at 140 ° C. and 3 atm of steam for 15 minutes, 30 minutes, 60 minutes, and 90 minutes, respectively. After treatment, dissolve each sample in THF,
The average molecular weight was measured by GPC. The measurement results are shown in FIG. The longer the contact time, the lower the average molecular weight.
【0017】[0017]
【発明の効果】本発明の方法によれば、主として乳酸ポ
リマーからなる成形品は粉末状となり、成形品に比して
容積が大幅に減少するので、効率的な保管、輸送が達成
される。さらに本発明の方法によれば、少ない手間とエ
ネルギーで粉末状とすることができるので、焼却処分す
る際に、一定の火力で燃焼させることができる。また埋
め立て用に使用した際にも、短い時間で埋め立て地が安
定化される。本発明の方法によれば、粉末状化したポリ
マーを、再度合成原料として利用する道が開かれる。さ
らには、病原性のある微生物、ビールス等を含む血液等
が付着するおそれのある医療廃棄物を、別途滅菌処理を
実施することなく処理できるので、廃棄物の発生源にお
ける処理が容易となる。EFFECTS OF THE INVENTION According to the method of the present invention, a molded product mainly made of lactic acid polymer is powdered, and its volume is greatly reduced as compared with the molded product, so that efficient storage and transportation can be achieved. Furthermore, according to the method of the present invention, the powder can be made into powder with a small amount of labor and energy, and therefore, it can be burned with a constant thermal power when incinerated. Also, when used for landfill, the landfill is stabilized in a short time. According to the method of the present invention, a way to reuse the powdered polymer as a synthetic raw material is opened. Furthermore, since medical wastes to which blood or the like containing pathogenic microorganisms, viruses and the like may adhere can be treated without separately performing sterilization treatment, treatment at the waste generation source becomes easy.
【図1】乳酸ポリマーの処理温度と分子量低下の関係を
示すグラフである。FIG. 1 is a graph showing the relationship between the treatment temperature of lactic acid polymer and the decrease in molecular weight.
【図2】乳酸ポリマーの処理時間と分子量低下の関係を
示すグラフである。FIG. 2 is a graph showing the relationship between the treatment time of lactic acid polymer and the decrease in molecular weight.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 岡林 淳 東京都中央区京橋2丁目3番13号 東洋イ ンキ製造株式会社内 ─────────────────────────────────────────────────── ─── Continued Front Page (72) Inventor Atsushi Okabayashi 2-33 Kyobashi, Chuo-ku, Tokyo Toyo Inki Manufacturing Co., Ltd.
Claims (1)
を、水分の存在下で100℃以上、1気圧以上に加熱加
圧して該成形品を加水分解させることを特徴とするポリ
マー成形品の処理方法。1. A method for treating a polymer molded article, which comprises subjecting a molded article mainly composed of a lactic acid polymer to heating and pressurization at 100 ° C. or higher and 1 atm or higher in the presence of water to hydrolyze the molded article.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP36158091A JPH05178977A (en) | 1991-12-27 | 1991-12-27 | Method for treating molded polymer article |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP36158091A JPH05178977A (en) | 1991-12-27 | 1991-12-27 | Method for treating molded polymer article |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH05178977A true JPH05178977A (en) | 1993-07-20 |
Family
ID=18474153
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP36158091A Pending JPH05178977A (en) | 1991-12-27 | 1991-12-27 | Method for treating molded polymer article |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH05178977A (en) |
Cited By (15)
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---|---|---|---|---|
JP2005060687A (en) * | 2003-07-29 | 2005-03-10 | Cci Corp | Method for processing polymer molded article, recycled raw material for polymer and polymer molded article using the same |
JP2005330211A (en) * | 2004-05-19 | 2005-12-02 | Toyohashi Univ Of Technology | Method for hydrolyzing biodegradable polyester into monomer, and apparatus for treating biodegradable polyester |
JP2006183277A (en) * | 2004-12-27 | 2006-07-13 | Shimizu Corp | Edge trimming method for concrete body, and edge trimming material |
JP2007002160A (en) * | 2005-06-27 | 2007-01-11 | Teijin Fibers Ltd | Depolymerization process for biodegradable polyester |
JP2007023176A (en) * | 2005-07-19 | 2007-02-01 | Teijin Fibers Ltd | Method for depolymerizing biodegradable polyester |
JP2007099663A (en) * | 2005-10-04 | 2007-04-19 | Toyohashi Univ Of Technology | Separating and recovering method of waste of polylactic acid |
JP2007277389A (en) * | 2006-04-06 | 2007-10-25 | Keisuke Akamatsu | Recovery process of plastic waste by type |
JP2008007611A (en) * | 2006-06-29 | 2008-01-17 | Kumamoto Technology & Industry Foundation | Method for collecting lactic acid and/or water-soluble oligomer from polylactic acid |
JP2009249508A (en) * | 2008-04-07 | 2009-10-29 | Kyushu Institute Of Technology | Method for oligomerizing polylactic acid product efficiently |
JP2012041487A (en) * | 2010-08-23 | 2012-03-01 | Kyushu Institute Of Technology | Polyester resin powder, method for producing the same, and method for producing molded body |
JP2012219210A (en) * | 2011-04-12 | 2012-11-12 | As R&D合同会社 | Method for producing low-molecular polymer, low-molecular polymer obtained by the method, and coating material, powder coating material, adhesive, fiber and nonwoven fabric using the polymer |
JP2015036393A (en) * | 2013-08-12 | 2015-02-23 | 学校法人君が淵学園 | Depolymerization method of polyester and method for recovering raw ingredient monomer of polyester by using the same depolymerization method |
JP2015036394A (en) * | 2013-08-12 | 2015-02-23 | 学校法人君が淵学園 | Depolymerization method of unsaturated polyester and method for recovering raw ingredient of unsaturated polyester by using the same depolymerization method |
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-
1991
- 1991-12-27 JP JP36158091A patent/JPH05178977A/en active Pending
Cited By (19)
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JP2005330211A (en) * | 2004-05-19 | 2005-12-02 | Toyohashi Univ Of Technology | Method for hydrolyzing biodegradable polyester into monomer, and apparatus for treating biodegradable polyester |
JP2006183277A (en) * | 2004-12-27 | 2006-07-13 | Shimizu Corp | Edge trimming method for concrete body, and edge trimming material |
JP4640670B2 (en) * | 2004-12-27 | 2011-03-02 | 清水建設株式会社 | Method and material for edging concrete body |
JP4647413B2 (en) * | 2005-06-27 | 2011-03-09 | 帝人ファイバー株式会社 | Depolymerization method of biodegradable polyester |
JP2007002160A (en) * | 2005-06-27 | 2007-01-11 | Teijin Fibers Ltd | Depolymerization process for biodegradable polyester |
JP2007023176A (en) * | 2005-07-19 | 2007-02-01 | Teijin Fibers Ltd | Method for depolymerizing biodegradable polyester |
JP2007099663A (en) * | 2005-10-04 | 2007-04-19 | Toyohashi Univ Of Technology | Separating and recovering method of waste of polylactic acid |
JP2007277389A (en) * | 2006-04-06 | 2007-10-25 | Keisuke Akamatsu | Recovery process of plastic waste by type |
JP2008007611A (en) * | 2006-06-29 | 2008-01-17 | Kumamoto Technology & Industry Foundation | Method for collecting lactic acid and/or water-soluble oligomer from polylactic acid |
JP2009249508A (en) * | 2008-04-07 | 2009-10-29 | Kyushu Institute Of Technology | Method for oligomerizing polylactic acid product efficiently |
JP2012041487A (en) * | 2010-08-23 | 2012-03-01 | Kyushu Institute Of Technology | Polyester resin powder, method for producing the same, and method for producing molded body |
JP2012219210A (en) * | 2011-04-12 | 2012-11-12 | As R&D合同会社 | Method for producing low-molecular polymer, low-molecular polymer obtained by the method, and coating material, powder coating material, adhesive, fiber and nonwoven fabric using the polymer |
JP2015036393A (en) * | 2013-08-12 | 2015-02-23 | 学校法人君が淵学園 | Depolymerization method of polyester and method for recovering raw ingredient monomer of polyester by using the same depolymerization method |
JP2015036394A (en) * | 2013-08-12 | 2015-02-23 | 学校法人君が淵学園 | Depolymerization method of unsaturated polyester and method for recovering raw ingredient of unsaturated polyester by using the same depolymerization method |
JP2015040265A (en) * | 2013-08-22 | 2015-03-02 | 国立大学法人豊橋技術科学大学 | Polylactic acid-based resin for use in anaerobic digestion process and method for producing the same |
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