GB1310430A - Process for producing a synthetic resin sheet - Google Patents
Process for producing a synthetic resin sheetInfo
- Publication number
- GB1310430A GB1310430A GB1310430DA GB1310430A GB 1310430 A GB1310430 A GB 1310430A GB 1310430D A GB1310430D A GB 1310430DA GB 1310430 A GB1310430 A GB 1310430A
- Authority
- GB
- United Kingdom
- Prior art keywords
- sheets
- resin
- copolymer
- temperature
- styrene
- 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.)
- Expired
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C55/00—Shaping by stretching, e.g. drawing through a die; Apparatus therefor
- B29C55/02—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Laminated Bodies (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
Abstract
1310430 Heat-stretched polyolefin sheets SEKISUI KAGAKU KOGYO KK 29 Dec 1970 [26 Dec 1969 (2) 29 Dec 1969 12 Jan 1970 (3) 16 Jan 1970 (2)] 61634/70 Headings B5A and B5B [Also in Division C3] Porous or void-containing synthetic resin sheets suitable for use as synthetic paper are prepared by a process which comprises uniaxially or biaxially stretching an unstretched sheet of an olefinic resin at a temperature below its melting point, the temperature of both surface layers of the sheet being at least 10‹ C. higher than that of the inner layer. The olefinic resin, which is preferably a C 2 -C 4 α-olefin polymer or copolymer having a melt index of from 0À01 to 5, may be blended with up to 50 wt. per cent of a resin having poor compatibility with the olefin polymer or copolymer, e.g. a styrene polymer, polyamide, polyacetal, polyacrylate, vinyl chloride, vinyl acetate, phenoxy or high molecular weight elastomer resin and the blend may also contain up to 75% (based on the weight of the composition) of a powdered inorganic filler material, e.g. talc, mica, zeolite, asbestos, lithopone, clay, kaolin, diatomaceous earth, silica, alumina, CaCO 3 , MgCO 3 , CaSO 4 , BaSO 4 , ZnS, TiO 2 or ZnO. To further improve the weight and surface characteristics of the sheets they may be uni- or bi-axially after-stretched at a temperature which is below the melting temperature of the resin and may be either below or above the temperature of the surface layers of the sheet during the primary stretching process. In examples olefinic resins comprising low pressure polyethylene (Examples 1 and 7); high density polyethylene (6); and low pressure polyethylene blended with inorganic filler materials and polystyrene and an ethylene/vinylacetate copolymer (2); high pressure polyethylene, styrene/vinyl acetate copolymer and a phenoxy resin (3); ethylene/vinyl acetate copolymer, polystyrene, and a styrene/butadiene copolymer (4); and styrene/vinyl acetate copolymer, polybutadiene, and polystyrene (5) are kneaded with a roller at 150-160‹ C., converted into sheets by hot pressing or calendering, cooled to 80‹ C. and passed between rollers maintained at 100-124‹ C. and stretched biaxially to 2À5 x their original length and width. The sheets so produced were white and opaque, had densities in the range 0À580-0À665 g./cm.<SP>3</SP>, both the surface and inner layers of the sheets having a porous structure with the void size of the surface layers being smaller than those of the inner layers and the void size distribution being symmetrical with respect to the centre line of a section of the sheets. In further examples the sheets obtained above are further biaxially stretched at 120‹ C., the sheets of Examples 1, 6 and 7 also being heated to 120‹ C. and allowed to shrink 5% (Example 8) and supercalendered in three stages at a pressure of 50 kg./cm.<SP>3</SP> (Example 9).
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB6163470 | 1970-12-29 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1310430A true GB1310430A (en) | 1973-03-21 |
Family
ID=10487253
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1310430D Expired GB1310430A (en) | 1970-12-29 | 1970-12-29 | Process for producing a synthetic resin sheet |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB1310430A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2556648A1 (en) * | 1983-12-16 | 1985-06-21 | Mitsui Toatsu Chemicals | PROCESS FOR PRODUCING POROUS FILMS, FILMS OBTAINED AND THEIR USE |
US9725566B2 (en) | 2004-12-07 | 2017-08-08 | Daramic, Llc | Microporous material and a method of making same |
-
1970
- 1970-12-29 GB GB1310430D patent/GB1310430A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2556648A1 (en) * | 1983-12-16 | 1985-06-21 | Mitsui Toatsu Chemicals | PROCESS FOR PRODUCING POROUS FILMS, FILMS OBTAINED AND THEIR USE |
US9725566B2 (en) | 2004-12-07 | 2017-08-08 | Daramic, Llc | Microporous material and a method of making same |
US10249863B2 (en) | 2004-12-07 | 2019-04-02 | Daramic, Llc | Microporous material and a method of making same |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3758661A (en) | Process for producing a synthetic paper | |
US3790435A (en) | Synthetic papers and method of making | |
SU570329A3 (en) | Synthetic paper | |
US3773608A (en) | Paper-like polymeric films and production thereof | |
US5397635A (en) | Multi-layer high opacity film structure of improved whiteness and machinability | |
GB1268823A (en) | Synthetic papers and method of making the same | |
US4176148A (en) | Method of manufacturing microporous paper-like butene-1 polymer sheets | |
GB1316671A (en) | Porous thermoplastic synthetic polymer sheets and films | |
US3765999A (en) | Synthetic paper | |
CA1170159A (en) | Laminate film | |
US5264277A (en) | Multi-layer opaque film structures of reduced surface friction and process for producing same | |
EP0044544A1 (en) | Adhesive tape | |
US3993718A (en) | Method of manufacturing an artificial paper | |
US3234313A (en) | Thermoplastic films and process for preparing same | |
KR19980703334A (en) | Shrinking film made of polyethylene resin and styrene-butadiene copolymer | |
GB2150881A (en) | Decorative packaging films | |
GB1090059A (en) | Polymeric film-forming compositions and films of said compositions | |
CA2156896C (en) | Composite plastics film or sheet | |
KR910009977A (en) | Method of flash spinning polyolefin | |
US4359497A (en) | Paper-like butene-1 polymer compositions | |
KR850004599A (en) | Manufacturing method of porous film | |
WO1994006849A1 (en) | Paper-like film and method and compositions for making it | |
US3741841A (en) | Production of synthetic papers | |
GB1386544A (en) | Process for extruding composition of thermoplastic resin containing high content of inorganic filler | |
KR890701323A (en) | Linear low density polyethylene casting film |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PCNP | Patent ceased through non-payment of renewal fee |