Process for preparing polybutenes having enhanced reactivity using boron trifluoride catalysts (PT-647)

Claim 2

A process for the preparation of a polybutene having a number average molecular weight (M n ) of from about 500 to about 5,000 and a total terminal double bond content of at least 40%, based on the total theoretical unsaturation of the polybutene, said polybutene containing at least 50% by weight isobutylene units based on the polybutene M n which comprises: (1) contacting a feed comprising at least 10% by weight isobutylene, based on the weight of the feed, with a BF 3 catalyst in a manner and under conditions su fficient to cationically polymerize said feed in the liquid phase to form said polybutene, said polymerization being conducted in the presence of a catalyst promoter (a) at an average polymerization time of from 12 to about 40 minutes, (b) at a ratio of millimoles of BF 3 to moles of isobutylene in the feed of from about 0.1:1 to about 5:1, and (c) to an isobutylene conversion of at least about 70%; and (2) immediately quenching the polybutene product with a quench medium sufficient to deactivate said BF 3 catalyst.

Claim 3

The process of claim 1 wherein the isobutylene conversion is from about 75 to 99%.

Claim 4

The process of claims 1 or 2 wherein the average polymerization time is from about 15 to about 30 minutes.

Claim 5

The process of claims 1 or 2 wherein immediate quench is conducted on the polybutene product what is at the polymerization temperature.

Claim 6

The process of claims 1 or 2 wherein said catalyst promoter comprises at least one member selected from the group consisting of water, alcohol, carboxylic acid, acid anhydride, HF, ether and mixtures thereof.

Claim 7

The process of claims 1 or 2 wherein the feed comprises between about 10 and 40% butene-1, between about 10 and 40% butene-2, between about 40 and 60% isobutane, between about 4 and 10% n-butane, and up to about 0.5% butadiene, said percentages being by weight, based on the weight of the feed.

Claim 8

The process of claims 1 or 2 wherein the polymerization reaction is conducted in the presence of a catalyst promoter added separately from the polymerization catalyst to the polymerization zone in which the polymerization reaction is conducted.

Claim 9

The process of claims 1 or 2 wherein the ratio of mmoles of BF 3 to moles of isobutylene in the feed is from about 0.3:1 to about 4:1.

Claim 10

The process of claims 1 or 2 wherein the polymerization reaction is conducted to achieve an a isobutylene conversion of from about 80 to about 98%.

Claim 11

The process of claims or 2 wherein the polymerization reaction is conducted to achieve a polybutene having a terminal disubstituted double bond content of at least 18%, and a total terminal double bond content of at least about 45%.

Claim 12

The process of claims 1 or 2 wherein the feed consists essentially of olefin monomers containing 4 carbon atoms.

Claim 13

The process of claims 1 or 2 wherein the polymerization reaction is conducted at a temperature of from about -20° to about +25° C.

Claim 14

The process of claims 1 or 2 wherein the molecular weight distribution of the polybutene is controlled to be from about 1.5 to about 2.5.

Claim 15

The process of claims 1 or 2 wherein the average polymerization time is from about 15 to about 30 minutes.

Claim 16

The process of claims 1 or 2 wherein the average polymerization time is from about 20 to about 30 minutes.

Claim 17

The process of claims 1 or 2 wherein said immediate quench is conducted on polybutene which has not been suojected to isomerization suppression temperatures of less than -25° C.

Claim 18

A process for the preparation of a polybutene having a number average molecular weight (M n ) of from about 500 to about 5,000 and a total terminal double bond content of at least 40%, based on the total theoretical unsaturation of the polybutene, said polybutene containing at least 50% by weight isobutylene units based on the polybutene M n which comprises; (1) contacting a feed comprising at least 10% by weight isobutylene, based on the weight of the feed, with a BF 3 catalyst in a manner and under conditions sufficient to cationically polymerize said feed in the liquid phase to form said polybutene, said polymerization being conducted in the presence of a catalyst promoter (a) at an average polymerization time of from 12 to about 40 minutes, (b) at a ratio of millimoles of BF 3 to moles of isobutylene in the feed of from about 0.1:1 to about 5:1, (c) at a polymerization temperature of from about -20° to about +25° C., and (d) to an isobutylene conversion of at least about 70%; and (2) immediately quenching the polybutene product before the temperature of said product exceeds by about 2° C. the highest polymerization temperature employed with a quench medium sufficient to deactivate said BF 3 catalyst.

Claim 19

A process for the preparation of a polybutene having a number average molecular weight (M n ) of from about 500 to about 5,000 and a total terminal double bond content of at least 40%, based on the total theoretical unsaturation of the polybutene, said polybutene containing at least 50% by weight isobutylene units based on the polybutene M n which comprises; (1) contacting a feed comprising at least 10% by weight isobutylene, based on the weight of the feed, with a BF 3 catalyst in a manner and under conditions sufficient to cationically polymerize said feed in the liquid phase to form said polybutene, said polymerization being conducted in the presence of a catalyst promoter (a) at an average polymerization time of from 12 to about 40 minutes, (b) at a ratio of millimoles of BF 3 to moles of isobutylene in the feed of from about 0.1:1 to about 5:1, (c) at a polymerization temperature of from about -20° to about +25° C., and (d) to an isobutylene conversion of at least about 70%; and (2) immediately quenching the polybutene product before the temperature of said product exceeds by about 2° C. the highest polymerization temperature employed with a quench medium sufficient to deactivate said BF 3 catalyst.

Claim 20

The process of claim 17 wherein the isobutylene conversion is from about 75 to 99%.

Claim 21

The process of claim 18 wherein the average polymerization time is from about 15 to about 30 minutes.

Claim 22

The process of claim 17 wherein said catalyst promoter comprises at least one member selected from the group consisting of water, alcohol, carboxylic acid, acid anhydride, HF, ether and mixtures thereof.

Claim 23

The process of claim 17 wherein the feed comprises between about 10 and 40% butene-1, between about 10 and 40% butene-2, between about 40 and 60% isobutane, between about 4 and 10% n-butane, and up to about 0.5% butadiene, said percentages being by weight, based on the weight of the feed.

Claim 24

The process of claim 17 wherein the polymerization reaction is conducted in the presence of a catalyst promoter added separately from the polymerization catalyst to the polymerization zone in which the polymerization reaction is conducted.

Claim 25

The process of claim 17 wherein the ratio of moles of BF 3 to moles of isobutylene in the feed is from about 0.3:1 to about 4:1.

Claim 26

The process of claim 17 wherein the polymerization reaction is conducted to achieve an isobutylene conversion of from about 80 to about 98%.

Claim 27

The process of claim 17 wherein the polymerization reaction is conducted to achieve a polybutene having a terminal disubstituted double bond content of at least 18%, and a total terminal double bond content of at least about 45%.

Claim 28

The process of claim 17 wherein the feed consists essentially of olefin monomers containing 4 carbon atoms.

Claim 29

The process of claim 17 wherein the molecular weight distribution of the polybutene is controlled to be from about 1.5 to about 2.5.

Claim 30

The process of claim 17 wherein the average polymerization time is from about 15 to about 30 minutes.

Claim 31

The process of claim 28 wherein the average polymerization time is from about 20 to about 30 minutes.

Claim 32

The process of claim 17 wherein said immediate quench is conducted on polybutene which has not been subjected to isomerization suppression temperatures of less than -25° C.