GB942297A - Poly(4-methyl-pentene-1) and articles produced therefrom - Google Patents
Poly(4-methyl-pentene-1) and articles produced therefromInfo
- Publication number
- GB942297A GB942297A GB2269561A GB2269561A GB942297A GB 942297 A GB942297 A GB 942297A GB 2269561 A GB2269561 A GB 2269561A GB 2269561 A GB2269561 A GB 2269561A GB 942297 A GB942297 A GB 942297A
- Authority
- GB
- United Kingdom
- Prior art keywords
- polymer
- ashing
- slurry
- medium
- liquid
- 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
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
Abstract
A polymer of 4-methyl-pentene-1 is prepared by polymerizing the monomer under air and moisture-free conditions in the presence of a stereospecific catalyst, and as diluent an inert hydrocarbon liquid, excess of the monomer itself or a chlorinated aromatic hydrocarbon, whereby a separable slurry of poly-4-methyl-pentene-1 is diluent is obtained and then de-ashing the polymer under water-free conditions so that the ash content does not exceed 0.1% by weight of the polymer and the transition metal content of the polymer is below 50 p.p.m. In the de-ashing operation, the slurry or its dispersed polymer content is treated with sufficient of an effective reagent to react with all of the catalyst residues to convert them to products soluble in the liquid medium, then the polymer is washed at least until all visible colour has been removed and finally the polymer is separated from the residual wash liquid. The polymer obtained has a melting point of 243 DEG C., a melt flow index between 0.01 and 1000, a density of 0.82 to 0.86 g/cc. and can be melt shaped into shaped articles having in 1/8 inch section a clarity of grade 1 and a haze of group 1. Suitable liquid media for the de-ashing step include (a) the dispersion phase of the slurry (including any unreacted reagent plus any other organic solvent which may be added), (b) if the dispersed polymer has previously been separated from the dispersion phase of the slurry, the liquid media may be any unreacted reagent plus any other organic solvent which might have been added to the polymer and any of the dispersion phase of the slurry occluded with the dispersed polymer. If the medium is primarily hydrocarbon, the higher alcohols, higher acids and higher amines (e.g. carbon chain of at least 8 carbon atoms) may be employed as the de-ashing reagents. e.g. 3,5,5-trimethylhexanol dodecanol, n-nonoic acid and 3,5,5-trimethylhexylamine may be used. Mixtures of acetyl acetone and isopropylalcohol may also be used. If the medium is primarily a polar one, lower alcohols may be used both as the reagent and as the medium. Numerous examples are given in which the stereospecific catalysts are selected from TiCl3 with AL(C2H5)2 Cl, LiC4H9, Zn(C4H9)2, AL(C2H5)3, AL(iso-C4H9)3, lithium aluminium butyl triethyl or with aluminium ethyl sesquichloride. The de-ashing agents are selected from acetylacetone with n-butanol or isopropyl alcohol; n-butanol; isopropanol; nonanol; ethanol; methanol; n-dodecanol; n-nonoic acid; 3,5,5 trimethylhexylamine; 3,5,5 trimethylhexanol and acetyl acetone. The washing medium is preferably a water-free organic liquid. In some examples, alcohols e.g. methanol, ethanol, isopropanol, butanol and nonanol, are used both as the de-ashing reagent and as the washing agent. Shaped articles may be produced from the polymers by the usual processes. Specifications 789,781, 808,144, 821,634, 877,050 and 940,145 are referred to.
Priority Applications (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BE619296D BE619296A (en) | 1961-06-22 | ||
NL280043D NL280043A (en) | 1961-06-22 | ||
NL133100D NL133100C (en) | 1961-06-22 | ||
GB2269561A GB942297A (en) | 1961-06-22 | 1961-06-22 | Poly(4-methyl-pentene-1) and articles produced therefrom |
DE1962J0021965 DE1520101B2 (en) | 1961-06-22 | 1962-06-20 | PROCESS FOR MANUFACTURING CLEAR, CRYSTALLINE POLY-4-METHYLPENTENE |
FR901697A FR1331635A (en) | 1961-06-22 | 1962-06-22 | Production and applications of new crystalline polymers of 4-methyl-pentene-1 |
JP2557962A JPS5270B1 (en) | 1961-06-22 | 1962-06-22 | |
DK280362A DK109758C (en) | 1961-06-22 | 1962-06-22 | Process for the preparation of a polymer of 4-methylpentene-1, which can be formed by melting into objects with high transparency. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2269561A GB942297A (en) | 1961-06-22 | 1961-06-22 | Poly(4-methyl-pentene-1) and articles produced therefrom |
GB4303461 | 1961-12-01 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB942297A true GB942297A (en) | 1963-11-20 |
Family
ID=26256068
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2269561A Expired GB942297A (en) | 1961-06-22 | 1961-06-22 | Poly(4-methyl-pentene-1) and articles produced therefrom |
Country Status (6)
Country | Link |
---|---|
JP (1) | JPS5270B1 (en) |
BE (1) | BE619296A (en) |
DE (1) | DE1520101B2 (en) |
DK (1) | DK109758C (en) |
GB (1) | GB942297A (en) |
NL (2) | NL133100C (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3327050A (en) * | 1964-07-29 | 1967-06-20 | Ici Ltd | Cables with 4-methyl pentene-1 primary insulation |
CN115612005A (en) * | 2022-11-09 | 2023-01-17 | 山东京博石油化工有限公司 | Efficient solvent deashing treatment method for polypropylene resin |
-
0
- NL NL280043D patent/NL280043A/xx unknown
- NL NL133100D patent/NL133100C/xx active
- BE BE619296D patent/BE619296A/xx unknown
-
1961
- 1961-06-22 GB GB2269561A patent/GB942297A/en not_active Expired
-
1962
- 1962-06-20 DE DE1962J0021965 patent/DE1520101B2/en active Granted
- 1962-06-22 JP JP2557962A patent/JPS5270B1/ja active Pending
- 1962-06-22 DK DK280362A patent/DK109758C/en active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3327050A (en) * | 1964-07-29 | 1967-06-20 | Ici Ltd | Cables with 4-methyl pentene-1 primary insulation |
CN115612005A (en) * | 2022-11-09 | 2023-01-17 | 山东京博石油化工有限公司 | Efficient solvent deashing treatment method for polypropylene resin |
Also Published As
Publication number | Publication date |
---|---|
NL280043A (en) | |
NL133100C (en) | |
DE1520101A1 (en) | 1970-03-19 |
DK109758C (en) | 1968-06-24 |
JPS5270B1 (en) | 1977-01-05 |
BE619296A (en) | |
DE1520101B2 (en) | 1976-11-04 |
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