Dialkyl ether production

Claim 2

A process for producing a dialkyl ether by exothermic reaction of isoolefin and alkanol in contact with catalyst, said process comprising (a) passing a stream comprising isoolefin, alkanol and diluent sequentially through a series of zones containing said catalyst, (b) cooling the effluent of any zone prior to or during the entry thereof into the next zone, (c) adding at least one of isoolefin and alkanol to the effluent from one of said zones prior to or during the entry thereof into the next zone.

Claim 3

A process in accordance with claim 1 wherein said cooling is achieved by indirect heat exchange.

Claim 4

Process in accordance with claim 1 wherein said series of zones is a plurality of catalyst beds in one reactor and wherein said cooling is achieved by interstage cooling using indirect heat exchange means.

Claim 5

Process in accordance with claim 1 wherein said cooling is achieved by direct heat exchange.

Claim 6

Process in accordance with claim 4 wherein said direct heat exchange is carried out by adding prior to or during the entry of the effluent of one zone into the following zone fluids comprising diluent and isoolefin and/or alkanol in quantities and at temperatures to said effluent to achieve the desired temperature of the combined fluids entering said zone.

Claim 7

A process in accordance with claim 1 wherein the total quantity of isoolefin employed in the process exceeds stoichiometrically the total quantity of alkanol employed so that the effluent from the last zone is substantially free of alkanol.

Claim 8

Process in accordance with claim 6 wherein the total quantity of isoolefin employed is introduced into the first zone and wherein fractions of the total quantity of alkanol employed are introduced into the first zone and into the following zones.

Claim 9

A process in accordance with claim 1 wherein said isoolefin is isobutylene, said alkanol is methanol and said catalyst is an acidic ion exchange resin.

Claim 10

A process to convert isobutylene into two high octane gasoline blending materials comprising (A) producing MTBE by (a) passing a stream comprising isobutylene, methanol and hydrocarbon diluent containing isobutane sequentially through a series of zones containing a catalyst for converting isoolefin and alkanol to dialkyl ether, (b) cooling the effluent of any zone prior to or during the entry thereof into the next zone, (c) adding at least one of isobutylene and methanol to the effluent from one zone prior to or during the entry thereof to the next zone, with the proviso that the total quantity of isobutylene employed in the multizone process exceeds stoichiometrically the total quantity of methanol employed so that the effluent from the last zone is substantially free of methanol, (d) passing the effluent from the last zone to a fractionation zone to yield a bottom stream containing MTBE and an overhead stream containing isobutylene and isobutane, (B) producing a high octane alkylate by (a) introducing said overhead stream as at least a portion of the isoolefin feedstock to an HF alkylation zone, (b) introducing an olefin and HF alkylation catalyst to said HF alkylation zone to produce an alkylation mixture, (c) withdrawing after reaction said alkylation mixture and separating it into a catalyst phase and a hydrocarbon phase, and (d) recovering alkylate as the second product of the process from said hydrocarbon phase.

Claim 11

A process to convert isobutylene into two high octane gasoline blending materials comprising (A) producing MTBE by (a) passing a stream comprising isobutylene, methanol and hydrocarbon diluent containing isobutane sequentially through a series of zones containing a catalyst for converting isoolefin and alkanol to dialkyl ether, (b) cooling the effluent of any zone prior to or during the entry thereof into the next zone, (c) adding at least one of isobutylene and methanol to the effluent from one zone prior to or during the entry thereof to the next zone, with the proviso that the total quantity of isobutylene employed in the multizone process exceeds stoichiometrically the total quantity of methanol employed so that the effluent from the last zone is substantially free of methanol, (d) passing the effluent from the last zone to a fractionation zone to yield a bottom stream containing MTBE and an overhead stream containing isobutylene and isobutane, (B) producing a high octane alkylate by (a) introducing said overhead stream as at least a portion of the isoolefin feedstock to an HF alkylation zone, (b) introducing an olefin and HF alkylation catalyst to said HF alkylation zone to produce an alkylation mixture, (c) withdrawing after reaction said alkylation mixture and separating it into a catalyst phase and a hydrocarbon phase, and (d) recovering alkylate as the second product of the process from said hydrocarbon phase.

Claim 12

Process in accordance with claim 9 wherein said olefin is selected from the group consisting of propylene, butylene and mixtures thereof.

Claim 13

Process in accordance with claim 9 wherein said catalyst phase is recycled to said HF alkylation zone.