WO2002048244A1 - Verfahren zum aufbereiten eines kunststoffgemisches - Google Patents
Verfahren zum aufbereiten eines kunststoffgemisches Download PDFInfo
- Publication number
- WO2002048244A1 WO2002048244A1 PCT/DE2001/004704 DE0104704W WO0248244A1 WO 2002048244 A1 WO2002048244 A1 WO 2002048244A1 DE 0104704 W DE0104704 W DE 0104704W WO 0248244 A1 WO0248244 A1 WO 0248244A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- solvent
- plastic mixture
- molecular weight
- polymers
- separation
- Prior art date
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
- C08J11/06—Recovery or working-up of waste materials of polymers without chemical reactions
- C08J11/08—Recovery or working-up of waste materials of polymers without chemical reactions using selective solvents for polymer components
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/02—Separating plastics from other materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/02—Separating plastics from other materials
- B29B2017/0203—Separating plastics from plastics
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/02—Separating plastics from other materials
- B29B2017/0213—Specific separating techniques
- B29B2017/0293—Dissolving the materials in gases or liquids
-
- 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
Definitions
- the invention relates to a method for processing a plastic mixture consisting of high molecular weight polymers which is contaminated with low molecular weight polymers and other foreign substances.
- High molecular weight polymers are those with a molecular weight above about 10,000, for example polyvinyl chloride, polystyrene, polyethylene terephthalate, polypropylene and polyethylenes, such as e.g. LDPE (low density polyethylene), LLDPE (linear low density polyethylene), MDPE (medium density polyethylene), HDPE (high density polyethylene), UHDPE (ultra high density polyethylene), with appropriate degree of polymerization.
- LDPE low density polyethylene
- LLDPE linear low density polyethylene
- MDPE medium density polyethylene
- HDPE high density polyethylene
- UHDPE ultra high density polyethylene
- low molecular weight polymers are those with a molecular weight of up to approximately 5000, for example waxes or degraded high molecular weight polymers.
- the plastic mixture can also contain polyester.
- a content of waxes, additives, degradation products and other impurities has been found to be disruptive for further utilization, especially if these polyolefins are to be used like new goods.
- From DE 41 22 277 AI it is known to subject shredded films of polyethylene in a solvent bath containing an organic solvent to intensive frictional surface cleaning and extraction in which ingredients and polyethylene waxes are removed from the chips without the plastic itself is dissolved, and inks are also removed by the frictive surface cleaning.
- Low-boiling acetic acid esters such as methyl, ethyl or isopropyl acetate or also low-boiling alcohols such as ethyl alcohol are mentioned as suitable solvents, the acetic acid esters being particularly suitable.
- a disadvantage of this process is the high need for solvents in the surface cleaning steps and extraction.
- foils Due to the special properties of the foils with their high surface-to-volume ratio, cleaning is easy. However, foils are no longer contained to a large extent in the mixed plastics from the collection of the dual system.
- the plastic mixture is introduced into an organic solvent in which at least one of the high molecular weight polymers is soluble at a specific temperature.
- the specific temperature can be defined as the dissolving temperature at which at least one of the polymers contained in the plastic mixture is present in dissolved form in the presence of the organic solvent used in more than 10-50% by weight.
- the solvent is kept at normal pressure at a working temperature at which none of the high molecular weight polymers is dissolved, a certain weight ratio of the plastic mixture to the solvent being set.
- the low molecular weight constituents are then extracted during a certain dwell time, and the plastic mixture is then optionally removed from the solvent.
- Granules are to be understood as meaning granules or agglomerates which can be obtained with the aid of the dry and wet processing methods mentioned above.
- Granules and especially agglomerates are characterized by a high porosity or surface fissuring, so that surprisingly it is possible to extract low molecular weight kular polymers and other foreign substances with a satisfactory degree of purity.
- Dissolving and phase separation ie taking advantage of the occurrence of at least two liquid phases, for separation in fractions of different polymer compositions.
- the tremor steps exploit the fact that, when a plastic mixture is dissolved in an organic solvent, a mixture gap is created under certain conditions and two liquid phases are generated, which can be treated separately.
- Liquid phase can also be selective be precipitated under shear or flow or with the addition of a precipitant.
- This separation process can be carried out alone or in combination with the liquid-liquid phase separation.
- a further separation method is a selective solution, which can also be carried out alone or in combination with precipitation under shear or flow or by adding a precipitant.
- the combination of selective dissolution with the liquid-liquid phase separation can also be used alone or again in combination with the precipitation processes described above.
- the solvent is removed after the extraction step and fresh solvent, either a chemically identical or non-identical one, is used for the subsequent separation into polymer fractions.
- Suitable solvents are aliphatic, aromatic or cyclic, saturated or unsaturated hydrocarbons, alcohols, carboxylic acids, amines, esters, ketones, tetrahydrofuran, bimethylformamide, dimethyl sulfoxide, N-methylpyrrolidone or mixtures thereof.
- hexane or octane as a solvent is particularly preferred.
- the solvent is preferably circulated, and when a limit concentration of low molecular weight polymers is reached in the solvent, the latter can be drawn off and purified by distillation. Fresh solvent is then returned for extraction.
- the concentration of plastic mixture in the solvent can be about 10 to 20% by weight, depending on the composition of the plastic mixture and the type of solvent.
- the working temperature is preferably kept in the range from 60 ° C to 70 ° C.
- the dwell time should be between 60 and 90 minutes in order to clean up about 80% of the waxes.
- Figure 1 is a schematic representation of the method according to the present invention.
- Figure 2 is a plot of the wax concentration in the solvent over time.
- Figure 1 shows schematically an extraction apparatus, which can be, for example, a carousel extractor operated by a motor.
- the mixed plastic pellets for example consisting of polypropylene and polyethylene, are introduced into the solvent, for example hexane, in a certain weight ratio.
- a slight relative movement of pellets to solvent is produced by stirring.
- the solvent temperature is set to 60 to 70 ° C, preferably 65 ° C.
- the extracted mixed plastic pellets are removed and, without desolventization, dissolved in a solvent kettle, which also contains hexane, for further processing. There is no longer any need for cleaning with hot water and subsequent drying.
- the polymer fractions obtained after further separation can be readjusted by adding additives.
- the solvent is normally circulated until a limit concentration of low molecular weight polymers is reached. Then the contaminated solvent is at least partially drawn off and purified by distillation, fresh solvent, preferably originating from the distillation, is filled up.
- Figure 2 shows the increase in the wax concentration in the solvent with the passage of time. It can be seen that after about 40 minutes there is no substantial enrichment in wax, so that contaminated solvent should then be removed or fresh solvent added at the latest.
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Sustainable Development (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Environmental & Geological Engineering (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BR0116120A BR0116120A (pt) | 2000-12-15 | 2001-12-13 | Processo para o tratamento de refugo misturado de plástico |
JP2002549770A JP2004515624A (ja) | 2000-12-15 | 2001-12-13 | 混合プラスチック廃棄物の処理方法 |
EP01995592A EP1353983A1 (de) | 2000-12-15 | 2001-12-13 | Verfahren zum aufbereiten eines kunststoffgemisches |
AU2002226290A AU2002226290A1 (en) | 2000-12-15 | 2001-12-13 | Method for recovering mixed plastic matter |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10062437.5 | 2000-12-15 | ||
DE2000162437 DE10062437A1 (de) | 2000-12-15 | 2000-12-15 | Verfahren zum Aufbereiten eines Kunststoffgemisches |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2002048244A1 true WO2002048244A1 (de) | 2002-06-20 |
Family
ID=7667208
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/DE2001/004704 WO2002048244A1 (de) | 2000-12-15 | 2001-12-13 | Verfahren zum aufbereiten eines kunststoffgemisches |
Country Status (8)
Country | Link |
---|---|
US (1) | US20030146547A1 (de) |
EP (1) | EP1353983A1 (de) |
JP (1) | JP2004515624A (de) |
CN (1) | CN1481413A (de) |
AU (1) | AU2002226290A1 (de) |
BR (1) | BR0116120A (de) |
DE (1) | DE10062437A1 (de) |
WO (1) | WO2002048244A1 (de) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2017003803A1 (en) * | 2015-06-30 | 2017-01-05 | The Procter & Gamble Company | Articles of reclaimed polyethylene compositions |
WO2017003801A1 (en) * | 2015-06-30 | 2017-01-05 | The Procter & Gamble Company | Reclaimed polyethylene composition |
EP3305839A1 (de) * | 2016-10-10 | 2018-04-11 | Fraunhofer Gesellschaft zur Förderung der Angewand | Verfahren zur wiederverwertung von polyolefinhaltigem abfallmaterial |
WO2022129309A1 (de) * | 2020-12-16 | 2022-06-23 | Alpla Werke Alwin Lehner Gmbh & Co. Kg | Recycling-verfahren für verunreinigte polyolefine |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10062710A1 (de) * | 2000-12-15 | 2002-06-20 | Dkr Deutsche Ges Fuer Kunststo | Herstellung eines Polypropylen-Blends |
US9284431B2 (en) * | 2012-02-14 | 2016-03-15 | Clariant International Ltd. | Method for recycling floor coverings |
WO2017003800A1 (en) * | 2015-06-30 | 2017-01-05 | The Procter & Gamble Company | Reclaimed polypropylene composition |
AU2017204940A1 (en) * | 2016-01-05 | 2018-08-23 | Yissum Research Development Company Of The Hebrew University Of Jerusalem Ltd. | A process for treating plastic waste |
CN105806790B (zh) * | 2016-03-15 | 2019-02-19 | 通标标准技术服务有限公司广州分公司 | 一种塑料中六价铬的测定方法 |
US10961366B2 (en) * | 2018-06-20 | 2021-03-30 | The Procter & Gamble Company | Method for purifying reclaimed polymers |
CN109880131B (zh) * | 2019-01-25 | 2020-11-17 | 华中科技大学 | 一种离子液体增塑纤维素清洁制造方法 |
WO2021211646A1 (en) * | 2020-04-15 | 2021-10-21 | The Procter & Gamble Company | Reducing surface and bulk contamination in plastic |
US11180618B1 (en) * | 2020-08-05 | 2021-11-23 | Timeplast, Llc | Process of transforming a plastic extrusion system into a dynamic depolymerization reactor |
CN114058073A (zh) * | 2020-08-07 | 2022-02-18 | Apk股份公司 | 使用滚筒对滚筒加工步骤的基于溶剂的回收利用 |
US10954354B1 (en) * | 2020-10-16 | 2021-03-23 | Timeplast, Llc | Upcycling process for unsorted waste stream |
CN114434685B (zh) * | 2020-10-30 | 2023-08-08 | 中国石油化工股份有限公司 | 浸取器及其应用、含pvc废塑料回收利用的装置及其方法 |
CN112497777A (zh) * | 2020-11-27 | 2021-03-16 | 陈辉煌 | 一种可diy香薰蜡块制作装置 |
CN112920494A (zh) * | 2021-02-05 | 2021-06-08 | 保定风帆美新蓄电池隔板制造有限公司 | 一种用铅酸蓄电池pe隔板废料制备再生物的方法 |
CN118060299B (zh) * | 2024-04-25 | 2024-06-21 | 湖南金阳石墨烯研究院有限公司 | 一种废弃电池负极石墨的回收方法 |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5278282A (en) * | 1989-09-11 | 1994-01-11 | Rensselaer Polytechnic Institute | Polymer recycling by selective dissolution |
EP0790277A1 (de) * | 1996-02-19 | 1997-08-20 | Fina Research S.A. | Verfahren zum Sortieren von Polymerisaten |
DE19744436A1 (de) * | 1997-10-08 | 1999-04-15 | Lindner Wolfgang | Verfahren zur Gewinnung von polyolefinischen Kunststoffen |
DE19822234A1 (de) * | 1998-05-07 | 1999-11-18 | Stefan Bosewitz | Verfahren zur Trennung von Kunststoffen und deren Mischungen durch selektives Fällen aus Lösungen |
DE19905029A1 (de) * | 1999-01-29 | 2000-11-16 | Bgb Ges Tu Berlin | Verfahren zur Trennung vermischter Polyolefine |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5554657A (en) * | 1995-05-08 | 1996-09-10 | Shell Oil Company | Process for recycling mixed polymer containing polyethylene terephthalate |
US5994417A (en) * | 1996-06-04 | 1999-11-30 | Auburn University | Process for recovering polymers from commingled materials |
-
2000
- 2000-12-15 DE DE2000162437 patent/DE10062437A1/de not_active Withdrawn
-
2001
- 2001-01-13 US US10/220,690 patent/US20030146547A1/en not_active Abandoned
- 2001-12-13 EP EP01995592A patent/EP1353983A1/de not_active Withdrawn
- 2001-12-13 JP JP2002549770A patent/JP2004515624A/ja active Pending
- 2001-12-13 BR BR0116120A patent/BR0116120A/pt not_active Application Discontinuation
- 2001-12-13 WO PCT/DE2001/004704 patent/WO2002048244A1/de active Application Filing
- 2001-12-13 CN CNA018206360A patent/CN1481413A/zh active Pending
- 2001-12-13 AU AU2002226290A patent/AU2002226290A1/en not_active Abandoned
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5278282A (en) * | 1989-09-11 | 1994-01-11 | Rensselaer Polytechnic Institute | Polymer recycling by selective dissolution |
EP0790277A1 (de) * | 1996-02-19 | 1997-08-20 | Fina Research S.A. | Verfahren zum Sortieren von Polymerisaten |
DE19744436A1 (de) * | 1997-10-08 | 1999-04-15 | Lindner Wolfgang | Verfahren zur Gewinnung von polyolefinischen Kunststoffen |
DE19822234A1 (de) * | 1998-05-07 | 1999-11-18 | Stefan Bosewitz | Verfahren zur Trennung von Kunststoffen und deren Mischungen durch selektives Fällen aus Lösungen |
DE19905029A1 (de) * | 1999-01-29 | 2000-11-16 | Bgb Ges Tu Berlin | Verfahren zur Trennung vermischter Polyolefine |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2017003803A1 (en) * | 2015-06-30 | 2017-01-05 | The Procter & Gamble Company | Articles of reclaimed polyethylene compositions |
WO2017003801A1 (en) * | 2015-06-30 | 2017-01-05 | The Procter & Gamble Company | Reclaimed polyethylene composition |
EP3305839A1 (de) * | 2016-10-10 | 2018-04-11 | Fraunhofer Gesellschaft zur Förderung der Angewand | Verfahren zur wiederverwertung von polyolefinhaltigem abfallmaterial |
WO2018068973A1 (en) * | 2016-10-10 | 2018-04-19 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Method for recycling polyolefin containing waste |
US10934410B2 (en) | 2016-10-10 | 2021-03-02 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Method for recycling polyolefin containing waste |
WO2022129309A1 (de) * | 2020-12-16 | 2022-06-23 | Alpla Werke Alwin Lehner Gmbh & Co. Kg | Recycling-verfahren für verunreinigte polyolefine |
CH718174A1 (de) * | 2020-12-16 | 2022-06-30 | Alpla Werke Alwin Lehner Gmbh & Co Kg | Recycling-Verfahren für verunreinigte Polyolefine. |
Also Published As
Publication number | Publication date |
---|---|
JP2004515624A (ja) | 2004-05-27 |
CN1481413A (zh) | 2004-03-10 |
AU2002226290A1 (en) | 2002-06-24 |
EP1353983A1 (de) | 2003-10-22 |
US20030146547A1 (en) | 2003-08-07 |
BR0116120A (pt) | 2003-12-23 |
DE10062437A1 (de) | 2002-06-20 |
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