Process for separating alkanols from aqueous calcium chloride

Claim 2

A process which comprises adding a C 4 or C 5 hydrocarbon feed comprising an isoolefin to an aqueous solution of a calcium chloride-alkanol complex wherein the alkanol is methanol or ethanol at a temperature of about 80°-120° C. and a pressure of about 20-180 psig to provide an upper phase comprising the hydrocarbon feed and alkanol and a lower phase comprising aqueous calcium chloride.

Claim 3

The process of claim 1 wherein the hydrocarbon feed is substantially pure isobutylene.

Claim 4

The process of claim 1 wherein the hydrocarbon feed is a C 4 hydrocarbon stream containing isobutylene.

Claim 5

The process of claim 1 wherein the alkanol is methanol.

Claim 6

The process of claim 1 wherein the weight of hydrocarbon feed added to the aqueous solution is at least about 1.3 times the weight of alkanol in the calcium chloride-alkanol complex.

Claim 7

The process of claim 1 wherein the hydrocarbon feed is added until at least about 50% of the alkanol has been recovered from the aqueous solution.

Claim 8

The process of claim 6 wherein the hydrocarbon feed is added until at least about 80% of the alkanol has been recovered from the aqueous solution.

Claim 9

The process of claim 6 wherein the hydrocarbon feed is added until at least about 90% of the alkanol has been recovered from the aqueous solution.

Claim 10

A process which comprises (1) adding at least about 1.3 parts by weight of a C 4 hydrocarbon stream containing isobutylene to an amount of an aqueous solution of a calcium chloride-methanol complex containing one part by weight of complexed methanol at a temperature of about 80°-120° C. and a pressure of about 20-180 psig to provide an upper phase comprising the hydrocarbon feed and at least about 90% of the methanol and a lower phase comprising aqueous calcium chloride and up to about 10% of the methanol and (2) separating the upper phase from the lower phase.

Claim 11

A process which comprises (1) adding at least about 1.3 parts by weight of a C 4 hydrocarbon stream containing isobutylene to an amount of an aqueous solution of a calcium chloride-methanol complex containing one part by weight of complexed methanol at a temperature of about 80°-120° C. and a pressure of about 20-180 psig to provide an upper phase comprising the hydrocarbon feed and at least about 90% of the methanol and a lower phase comprising aqueous calcium chloride and up to about 10% of the methanol and (2) separating the upper phase from the lower phase.

Claim 12

In a process for preparing an ether by: (A) reacting an excess of a C 1 -C 2 alkanol with an isoolefin containing 4 or 5 carbon atoms to form a crude reaction product comprising a mixture of (1) an ether corresponding to the formula R-O-R', wherein R is a methyl or ethyl group and R' is a t-butyl or t-amyl group, (2) unreacted alkanol, and (3) unreacted hydrocarbon, (B) charging the crude reaction product to a separator, (C) intimately mixing the crude reaction product in the separator with an aqueous solution containing at least 0.25 mol of calcium chloride per mol of unreacted alkanol to form a calcium chloride-alkanol complex and provide a two-phase mixture consisting of an upper layer comprising the ether and unreacted hydrocarbon and a lower layer comprising the aqueous calcium chloride-alkanol complex, (D) withdrawing the ether and unreacted hydrocarbon from the separator as overhead, (E) withdrawing the aqueous calcium chloride-alkanol complex from the separator as bottoms, (F) separating the alkanol from the aqueous calcium chloride, (G) recycling the separated alkanol to the reactor, and (H) recycling the separated aqueous calcium chloride to the separator, the improvement which comprises: (a) separating the alkanol from the aqueous calcium chloride by adding a C 4 or C 5 hydrocarbon feed comprising an isoolefin to the bottoms of step E at a temperature of about 80°-120° C. and a pressure of about 20-180 psig to provide an upper phase comprising the hydrocarbon feed and alkanol and a lower phase comprising aqueous calcium chloride and (b) recycling the entire upper phase containing the separated alkanol to the reactor.

Claim 13

In a process for preparing an ether by: (A) reacting an excess of a C 1 -C 2 alkanol with an isoolefin containing 4 or 5 carbon atoms to form a crude reaction product comprising a mixture of (1) an ether corresponding to the formula R-O-R', wherein R is a methyl or ethyl group and R' is a t-butyl or t-amyl group, (2) unreacted alkanol, and (3) unreacted hydrocarbon, (B) charging the crude reaction product to a separator, (C) intimately mixing the crude reaction product in the separator with an aqueous solution containing at least 0.25 mol of calcium chloride per mol of unreacted alkanol to form a calcium chloride-alkanol complex and provide a two-phase mixture consisting of an upper layer comprising the ether and unreacted hydrocarbon and a lower layer comprising the aqueous calcium chloride-alkanol complex, (D) withdrawing the ether and unreacted hydrocarbon from the separator as overhead, (E) withdrawing the aqueous calcium chloride-alkanol complex from the separator as bottoms, (F) separating the alkanol from the aqueous calcium chloride, (G) recycling the separated alkanol to the reactor, and (H) recycling the separated aqueous calcium chloride to the separator, the improvement which comprises: (a) separating the alkanol from the aqueous calcium chloride by adding a C 4 or C 5 hydrocarbon feed comprising an isoolefin to the bottoms of step E at a temperature of about 80°-120° C. and a pressure of about 20-180 psig to provide an upper phase comprising the hydrocarbon feed and alkanol and a lower phase comprising aqueous calcium chloride and (b) recycling the entire upper phase containing the separated alkanol to the reactor.

Claim 14

The process of claim 10 wherein (1) the crude reaction product is the product obtained by reacting an excess of methanol with a C 4 hydrocarbon stream containing isobutylene and (2) the hydrocarbon feed is a C 4 hydrocarbon stream containing isobutylene.

Claim 15

The process of claim 11 wherein the hydrocarbon feed comprises the unreacted hydrocarbon portion of the overhead of step D.