US3932371A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for preparing low bulk viscosity polymers
Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1973-12-28
•
Granted: 1976-01-13
•
Expires: 1993-12-28
Abstract
Abstract Polymerization reactions may be carried out in a solvent at a temperature which is above its lower critical solution temperature thereby resulting in a two-phase system comprising a solvent phase containing dissolved therein monomers and low molecular weight fractions of polymer and dispersed fluid phase comprising a solution of solvent in the higher molecular weight fraction of polymer being formed.
Inventors
- 👤 Kenneth W. Powers
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 14:16
CPC Classifications
C; C08; C08F; C08F10/00; C08F36/00; C08F36/02; C08F36/04
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
228 words
A two phase polymerization process for preparing an LM polymer which comprises reacting at polymerization conditions a C 4 -C 6 conjugated diolefin with an isoolefin having the general formula: ##EQU2## wherein R 1 is H, a C 1 -C 12 acyclic hydrocarbyl radical or a C 1 -C 12 alicyclic hydrocarbyl radical and R 2 is a hydrocarbyl radical selected from the group consisting of phenyl, C 1 -C 12 acyclic radicals, C 1 -C 12 alicyclic radicals and mixtures thereof, in the presence of a catalyst selected from the group consisting of (1) aluminum bromide and (2) ethyl aluminum dichloride promoted with a compound selected from the group consisting of hydrogen chloride, C 3 -C 7 organic halides, and mixtures thereof, said catalyst being dissolved in a C 5 -C 9 alkane; said polymerization being carried out in a vehicle wherein said vehicle is (1) propane or (2) propane plus a C 5 -C 9 alkane, the reaction being carried out continuously with the steady-state concentration of monomers to be polymerized plus C 5 -C 9 alkane is about 4 to about 23 weight percent based on monomers plus propane, plus C 5 -C 9 alkane, the polymerization being carried out at a temperature of about -30 to about -80°C. and the polymerization being carried out at a conversion rate of about 60 to about 90%.
Claim 2
Dependent Claim
228 words
A two phase polymerization process for preparing an LM polymer which comprises reacting at polymerization conditions a C 4 -C 6 conjugated diolefin with an isoolefin having the general formula: ##EQU2## wherein R 1 is H, a C 1 -C 12 acyclic hydrocarbyl radical or a C 1 -C 12 alicyclic hydrocarbyl radical and R 2 is a hydrocarbyl radical selected from the group consisting of phenyl, C 1 -C 12 acyclic radicals, C 1 -C 12 alicyclic radicals and mixtures thereof, in the presence of a catalyst selected from the group consisting of (1) aluminum bromide and (2) ethyl aluminum dichloride promoted with a compound selected from the group consisting of hydrogen chloride, C 3 -C 7 organic halides, and mixtures thereof, said catalyst being dissolved in a C 5 -C 9 alkane; said polymerization being carried out in a vehicle wherein said vehicle is (1) propane or (2) propane plus a C 5 -C 9 alkane, the reaction being carried out continuously with the steady-state concentration of monomers to be polymerized plus C 5 -C 9 alkane is about 4 to about 23 weight percent based on monomers plus propane, plus C 5 -C 9 alkane, the polymerization being carried out at a temperature of about -30 to about -80°C. and the polymerization being carried out at a conversion rate of about 60 to about 90%.
Claim 3
Dependent Claim
39 words
The process of claim 1 wherein the propane is the sole vehicle, the concentration of monomers in the feed stream to the reactor is about 40-44 volume % based on monomers plus propane, and the catalyst solvent is hexane.
Claim 4
Dependent Claim
17 words
The process of claim 1 wherein the vehicle is propane plus a C 5 -C 9 alkane.
Claim 5
Dependent Claim
15 words
The process of claim 3 wherein the alkane is a C 6 -C 8 alkane.
Claim 6
Dependent Claim
10 words
The process of claim 4 wherein the alkane is hexane.
Claim 7
Dependent Claim
25 words
The process of claim 1 wherein R 1 is methyl and R 2 is an alkyl radical of about 1 to about 6 carbon atoms.
Claim 8
Dependent Claim
71 words
The process of claim 1 wherein: 1. the vehicle containing polymer product is allowed to stand at a temperature above the lower critical solution temperature of the solvent-polymer system for a time sufficient to cause separation into a lighter solvent rich phase and a heavier polymer rich phase; 2. the lighter solvent rich phase is recycled to the reactor; and 3. the polymer is separated from the heavier polymer rich phase.
Claim 9
Dependent Claim
25 words
The process of claim 7 wherein R 1 is methyl and R 2 is an alkyl radical having about 1 to about 6 carbon atoms.
Claim 10
Dependent Claim
29 words
The process of claim 7 wherein the isoolefin is isobutylene, the diolefin is isoprene and the catalyst is ethyl aluminum dichloride promoted with a minor amount of benzyl chloride.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-01-12 | 1979-07-14 | 1980-01-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-01-12 | 1983-07-14 | 1984-01-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-01-12 | 1987-07-14 | 1988-01-13 | $7700.00 | Window Closed / Lapsed |