Low-fluoride, reactive polyisobutylene
View Patent ↗A method of making a low-fluoride reactive PIB composition includes in one embodiment: a) providing an isobutylene-enriched C4 feedstock by way of blending a first mixed C4 feedstock with a second feedstock having a lower LB/IsoB index; (b) feeding the isobutylene-enriched C4 feedstock to a polymerization reactor with a catalyst complex comprising BF 3 and a modifier selected from alcohols, ethers and mixtures thereof; (c) polymerizing the isobutylene-enriched C4 feedstock in the reactor while maintaining the reactor at a temperature above −40° C. and most preferably above −15° C. and utilizing a residence time less than 45 minutes to produce a crude PIB composition in a polymerization mixture; and (d) recovering a purified PIB composition from the polymerization mixture having a molecular weight, Mn, from 250 to 5000 Daltons and an alpha vinylidene content of at least 50 mol %. The crude PIB composition suitably has a fluoride content of less than 100 ppm and the purified PIB composition has a fluoride content of less than 20 ppm. In another aspect, ammonium salts are used to neutralize the catalyst and fluoride salts are sublimed from the product at elevated temperatures.
1. A method of making a low-fluoride reactive PIB composition comprising:
(a) providing an isobutylene-enriched C4 feedstock by way of blending a first mixed C4 feedstock having an LB/IsoB index of greater than 3% with a second feedstock having a lower LB/IsoB index, thereby upgrading the feed to the reactor to higher isobutylene content through blending;
(b) feeding the isobutylene-enriched C4 feedstock to a polymerization reactor with a catalyst complex comprising BF 3 and a modifier selected from alcohols, ethers and mixtures thereof;
(c) polymerizing the isobutylene-enriched C4 feedstock in the reactor while maintaining the reactor at a temperature above −40° C. and utilizing a residence time less than 45 minutes to produce a crude PIB composition in a polymerization mixture; and
(d) recovering a purified PIB composition from the polymerization mixture having a molecular weight, Mn, from 250 to 5000 Daltons, and an alpha vinylidene content of at least 50 mol %.
2. The method according to claim 1 , wherein the residual fluoride content of the purified PIB composition is less than 20 ppm.
3. The method according to claim 2 , wherein the residual fluoride content of the purified PIB composition is less than 5 ppm.
4. The method according to claim 2 , wherein the residual organic fluoride content of the purified PIB composition is less than 3 ppm.
5. The method according to claim 1 , wherein the first mixed C4 feedstock has an LB/IsoB index of greater than 25% and wherein the second feedstock has an LB/IsoB index of less than 3%.
6. The method according to claim 1 , wherein the first mixed C4 feedstock comprises raffinate or dehydro effluent.
7. The method according to claim 1 , wherein the second feedstock comprises isobutylene concentrate or highly purified isobutylene.
8. The method according to claim 1 , wherein the reactor is maintained at a temperature of −25° C. or above.
9. The method according to claim 1 , wherein the reactor is maintained at a temperature of −15° C. or above.
10. The method according to claim 1 , wherein the reactor is maintained at a temperature above 0° C.
11. The method according to claim 1 , wherein the residence time is 20 minutes or less.
12. The method according to claim 11 , wherein the residence time is 7.5 minutes or less.
13. The method according to claim 1 , wherein the catalyst complex comprises a modifier selected from methanol, ethanol, tertiary butanol, isopropyl ether, diethyl ether and mixtures thereof.
14. The method according to claim 1 , wherein the molar ratio of modifier to BF 3 is in the range of 1:1 to 1.8:1.
15. The method according to claim 1 , wherein the molecular weight, Mn, of the purified PIB composition is from 300 to 5000 Daltons.
16. A method of making a low-fluoride reactive PIB composition comprising:
(a) providing an isobutylene-containing feedstock;
(b) feeding the isobutylene-containing feedstock to a polymerization reactor with a catalyst complex comprising BF 3 and a modifier selected from alcohols, ethers and mixtures thereof;
(c) polymerizing the isobutylene-enriched C4 feedstock in the reactor while maintaining the reactor at a temperature above −40° C. and utilizing a residence time less than 45 minutes to produce a crude PIB composition in a polymerization mixture;
(d) withdrawing the crude PIB composition from the reactor;
(e) neutralizing the crude PIB composition with a quenching agent;
(f) treating the crude PIB composition at a temperature of from 150° C. to 300° C. to separate oligomers from the crude PIB composition; and
(g) recovering a purified PIB composition from the polymerization mixture having a molecular weight, Mn, from 250 to 5000 Daltons, and an alpha vinylidene content of at least 50 mol %,
further comprising washing the neutralized crude PIB composition with water and decanting the washed PIB composition to provide an aqueous phase and an organic phase containing PIB polymer and treating the organic phase containing PIB polymer at a temperature of from 150° C. to 300° C. and a pressure of from 0.25 psia to 10 psia to remove PIB oligomers from the composition.
17. The method according to claim 16 , wherein the purified PIB composition has less than 10% by weight C8 to 24 oligomers.
18. The method according to claim 16 , wherein the quenching agent is an ammonium quenching agent.
19. The method according to claim 16 , wherein the quenching agent is ammonium hydroxide.
20. In a method of making a reactive PIB composition, the improvement comprising withdrawing a crude PIB composition from a reactor; neutralizing the crude PIB composition with an ammonium quenching agent; washing the neutralized crude PIB composition with water and decanting the washed PIB composition to provide an aqueous phase and an organic phase containing PIB polymer; and treating the organic phase containing PIB polymer at a temperature of from 150° C. to 300° C. and a pressure of from 0.25 psia to 10 psia to remove PIB oligomers from the composition.
21. The improvement according to claim 20 , comprising treating the organic phase containing PIB polymer at a temperature of from 200° C. to 250° C. and a pressure of from 0.5 psia to 5 psia to remove PIB oligomers from the composition.