GB2161812A - Particulate cross-linked polymer mixtures - Google Patents
Particulate cross-linked polymer mixtures Download PDFInfo
- Publication number
- GB2161812A GB2161812A GB8516830A GB8516830A GB2161812A GB 2161812 A GB2161812 A GB 2161812A GB 8516830 A GB8516830 A GB 8516830A GB 8516830 A GB8516830 A GB 8516830A GB 2161812 A GB2161812 A GB 2161812A
- Authority
- GB
- United Kingdom
- Prior art keywords
- cross
- linked
- sheet
- uncross
- polymeric material
- 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.)
- Withdrawn
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
-
- 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
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/24—Crosslinking, e.g. vulcanising, of macromolecules
-
- 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
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/0061—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof characterized by the use of several polymeric components
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
A particulate, cross-linked polymeric material, e.g. polyethylene, is mixed with a compatible particulate, uncross-linked polymeric material, preferably in a weight ratio from 1:2 to 1:5, by means of a thermoplastic process e.g. extrusion, moulding or calendering process. A cross-linking agent may be added and the resulting mixture may be expanded by means of a blowing agent at a temperature in the range 190 DEG C to 210 DEG C. The starting cross-linked polymeric material may be derived from waste material.
Description
SPECIFICATION
Method of manufacture of polymeric materials
This invention relates to a method of manufacture of polymeric materials.
Cross-linked polymeric foams are generally much stronger than uncross-linked foams, and are suitable in applications as diverse as building materials, packaging materials, heat insulators and shock and sound absorbing materials. They are particularly useful as linings in automobile applications, for example, as covers for wheel arches. A known process for the production of a foamed, cross-linked polymer sheet, consists of the thermoplastic extrusion and chemical cross-linking of a previously uncross-linked polymer, to produce a cross-linked polymer sheet, followed by the expansion of the sheet by means of a blowing agent at a high temperature. The process can include the use of additives such as anti-oxidants and lubricants in the extrusion process.One example of a blowing agent is an azo compound which, at a temperature of around 200"C and in the presence of air, causes the polymeric sheet to expand into a foam.
Where shaped products are produced by cutting parts from a sheet material of a cross-linked polymeric foam, there is generally a large amount of waste material, typically 30% or more. This not only represents uneconomical use of the sheet material, but creates the problem of waste disposal.
Both burning the waste and burying it are expensive methods, and unacceptable for environmental reasons.
According to the present invention, there is provided a method of producing a polymeric material comprising: mixing a particulate, cross-linked, polymeric-material with a compatible particulate, uncross-linked, polymeric material by means of a thermoplastic production process.
This method allows for the recycling of waste cross- linked polymeric material such as foam.
It has been found that the resulting product has a higher degree of cross-linking, and thus greater strength, than has been obtained with conventionally produced cross-linked polymeric foams. This is because the cross-linking agent is able not only to cross-link the previously uncross-linked polymer, but also to form links between the previously uncross- linked polymer and the cross-linked polymer.
In order that the invention may be better understood, a preferred embodiment will now be described by way of example.
A low density polyethylene polymer compound (formulation A) containing a peroxide cross-linking agent and an azodicarbonamide blowing agent is extruded into sheet form using a conventional thermoplastic extrusion process at a temperature below 1300C. This sheet is then chemically crosslinked and expanded at a temperature of between 190 and 210 C in an air oven, using a conventional process. The resulting sheet is then cut into the required shapes for a production process.
Any wastage from the cutting of this sheet is then either granulated and pelletized using suitable extrusion compounding equipment or else ground to a powder, for example by cryogenic milling. The result is a particulate, cross-linked, polymeric material (formulation B).
One part of formulation B is then mixed with 2 to 5, preferably 2, parts of a second batch of formulation A. This mixture, together with a chemical cross-linking agent, is extruded into sheet form at a temperature of less than 1300C.
The resulting sheet contains cross-links not only between the molecules of formulation A, but also between the molecules of formulation B and formulation A. The sheet is then expanded into a foam using a blowing agent such as azodicarbonide, at a temperature of between 190 and 210"C, in the presence of air. The resulting expanded material may have at least equal physical characteristics to sheets produced exclusively from uncross-linked materials, due to the higher degree of chemical cross-linking. The presence in the sheet, before blowing, of a pre-cross-linked material may have the benefits of reducing the time taken to achieve the required blowing and of increasing the toughness of the final product.
It will be appreciated that particulate, crosslinked, polymeric material of any of the kinds referred to above can be incorporated in any suitable uncross-linked and/or uncross-linkable polymeric material without subsequent cross-linking. It has been found that the presence, in such composite materials, of the particulate, cross-linked, polymeric material provides satisfactory properties in comparison with the uncross-linked/uncross-linkable polymeric material. The incorporation may be by any of the methods referred to above.
1. A method of producing a polymeric material comprising: mixing a particulate, cross-linked, polymeric material with a compatible particulate, uncross-linked, polymeric material by means of a thermoplastic production process.
2. A method according to claim 1, wherein the uncross-linked polymeric material is cross-linkable, the method further comprising the inclusion of a cross-linking agent in the mix, performing the thermoplastic production process at a temperature below 1300C and then cross-linking the resulting mixture by means of a blowing agent at a temperature in the range of 1900C to 210 C.
3. A method according to claim 1 or claim 1, wherein the thermoplastic production process is an extrusion or calendering process, or a moulding process such as injection-, compression-, blow-, and press-moulding.
4. A method according to any one of claims 1 to 3, wherein the ratio of cross-linked to uncrosslinked material is between 1:2 and 1:5.
5. A method according to claim 4, wherein the ratio is substantially 1 to 2.
6. A method according to any one of claims 1 to 5, wherein the particulate, cross-linked polymeric starting material is prepared by the granula
**WARNING** end of DESC field may overlap start of CLMS **.
Claims (9)
1. A method of producing a polymeric material comprising: mixing a particulate, cross-linked, polymeric material with a compatible particulate, uncross-linked, polymeric material by means of a thermoplastic production process.
2. A method according to claim 1, wherein the uncross-linked polymeric material is cross-linkable, the method further comprising the inclusion of a cross-linking agent in the mix, performing the thermoplastic production process at a temperature below 1300C and then cross-linking the resulting mixture by means of a blowing agent at a temperature in the range of 1900C to 210 C.
3. A method according to claim 1 or claim 1, wherein the thermoplastic production process is an extrusion or calendering process, or a moulding process such as injection-, compression-, blow-, and press-moulding.
4. A method according to any one of claims 1 to 3, wherein the ratio of cross-linked to uncrosslinked material is between 1:2 and 1:5.
5. A method according to claim 4, wherein the ratio is substantially 1 to 2.
6. A method according to any one of claims 1 to 5, wherein the particulate, cross-linked polymeric starting material is prepared by the granula tion and subsequent pelletisation of an extruded cross-linked polymeric foam in sheet form.
7. A method according to any one of claims 1 to 6, wherein the polymeric material is polyethylene or a polyolefin copolymer.
8. A method of producing a polymeric material substantially as herein described.
9. A polymeric material when made by the method of any one of claims 1 to 8.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB8417412A GB8417412D0 (en) | 1984-07-07 | 1984-07-07 | Manufacture of polymeric materials |
Publications (2)
Publication Number | Publication Date |
---|---|
GB8516830D0 GB8516830D0 (en) | 1985-08-07 |
GB2161812A true GB2161812A (en) | 1986-01-22 |
Family
ID=10563599
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB8417412A Pending GB8417412D0 (en) | 1984-07-07 | 1984-07-07 | Manufacture of polymeric materials |
GB8516830A Withdrawn GB2161812A (en) | 1984-07-07 | 1985-07-03 | Particulate cross-linked polymer mixtures |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB8417412A Pending GB8417412D0 (en) | 1984-07-07 | 1984-07-07 | Manufacture of polymeric materials |
Country Status (1)
Country | Link |
---|---|
GB (2) | GB8417412D0 (en) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB904985A (en) * | 1960-04-26 | 1962-09-05 | Grace W R & Co | Polyethylene blends |
GB1117906A (en) * | 1966-05-26 | 1968-06-26 | Grace W R & Co | Polyolefin blends |
GB1424204A (en) * | 1972-05-04 | 1976-02-11 | British Industrial Plastics | Filled aminoplast moulding materials |
GB1594350A (en) * | 1976-11-30 | 1981-07-30 | Dunlop Ltd | Flexible sheet material |
-
1984
- 1984-07-07 GB GB8417412A patent/GB8417412D0/en active Pending
-
1985
- 1985-07-03 GB GB8516830A patent/GB2161812A/en not_active Withdrawn
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB904985A (en) * | 1960-04-26 | 1962-09-05 | Grace W R & Co | Polyethylene blends |
GB1117906A (en) * | 1966-05-26 | 1968-06-26 | Grace W R & Co | Polyolefin blends |
GB1424204A (en) * | 1972-05-04 | 1976-02-11 | British Industrial Plastics | Filled aminoplast moulding materials |
GB1594350A (en) * | 1976-11-30 | 1981-07-30 | Dunlop Ltd | Flexible sheet material |
Also Published As
Publication number | Publication date |
---|---|
GB8516830D0 (en) | 1985-08-07 |
GB8417412D0 (en) | 1984-08-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA1297629C (en) | Moldable silane-crosslinked polyolefin foam beads | |
US4452751A (en) | Styrena polymer foam made with α-polyolefin additives | |
US5605937A (en) | Moldable thermoplastic polymer foam beads | |
US4870111A (en) | Moldable silane-crosslinked polyolefin foam beads | |
US5026736A (en) | Moldable shrunken thermoplastic polymer foam beads | |
US5589519A (en) | Process of extruding lightly crosslinked polyolefin foam | |
EP0036562B1 (en) | Foamable olefin polymer compositions stabilized with certain higher ethers, esters or anhydrides, foaming process using them and foam article produced | |
US4255372A (en) | Process for the production of foam materials on polyolefin basis | |
US4246211A (en) | Process for the production of foam materials on polyolefin basis | |
EP0036561B1 (en) | Foamable olefin polymer compositions stabilized with certain naphthyl amine compounds, foaming process using them and foam article produced | |
CA1111999A (en) | Stabilized polystyrene compositions | |
US5631304A (en) | Method of manufacturing rigid foamed product | |
EP0166252B1 (en) | Production process of pre-foamed particles | |
GB2161812A (en) | Particulate cross-linked polymer mixtures | |
EP0280993B1 (en) | Moldable silane-crosslinked polyolefin foam beads | |
US3010916A (en) | Composition comprising isoolefin-diolefin copolymer and preparation of closed cell prduct therefrom | |
GB2113228A (en) | Foamable vinyl chloride resin compositions | |
JPH07330935A (en) | Crystalline polyolefin foam | |
KR102434208B1 (en) | Method for manufacturing highly flame resistant and eco-friendly rubber-based nanocomposite foam using waste rubber foam powder | |
JP2675240B2 (en) | Rigid polyvinyl chloride foam material | |
CA1038577A (en) | Rotational molding of chemically cross-linked polyethylene foam | |
JPH05214143A (en) | Polypropylene-based resin crosslinked foam | |
CA1230200A (en) | STYRENE POLYMER FOAM MADE WITH .alpha.-POLYOLEFIN ADDITIVES | |
DE69030972T2 (en) | Process for the production of moldable shrinked thermoplastic foam beads | |
JPH06170963A (en) | Polyolefinic resin foam and production thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
WAP | Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1) |