Production of isobutene from methyl tertiary butyl ether

Claim 2

A process for producing high purity isobutene by the dissociation of MTBE comprising contacting a stream in vapor phase and containing MTBE with a microreticular acid cation exchange resin in a fixed bed, the inlet temperature of the vapor phase being in the range of 110° C. to 150° C. and the temperature in said fixed bed being in the range of 90° C. to 160° C., said stream having an LHSV in the range of 7 to 35, thereby dissociating a portion of said MTBE into methanol and isobutene.

Claim 3

The process according to claim 1 wherein the inlet temperature of the vapor phase is in the range of 115° C. to 145° C. and the temperature of the fixed bed being in the range of 120° C. to 150° C.

Claim 4

The process according to claim 2 wherein the LHSV is in the range of 14 to 25.

Claim 5

The process according to claim 1 wherein the MTBE comprises at least 95% wt. of said stream.

Claim 6

The process according to claim 4 wherein the MTBE comprises at least 97 wt. % of said stream.

Claim 7

The process according to claim 1 wherein said acid cation exchange resin is thermally stabilized.

Claim 8

The process according to claim 6 wherein chlorine or bromine groups are incorporated into the resin.

Claim 9

The process according to claim 7 wherein chlorine groups are incorporated into the resin.

Claim 10

The process according to claim 1 wherein said fixed bed is positioned in a tubular reactor comprising a plurality of tubes containing said acid cation exchange resin, said tubes being mounted in a shell for contact with a heat exchange medium therein.

Claim 11

The process according to claim 9 wherein the heat exchange medium supplies heat to the reactor whereby the heat supplied by said heat exchange medium and the vaporized stream containing MTBE maintain the temperature in said fixed bed.

Claim 12

The process according to claim 1, wherein there is a pressure drop through said fixed bed in the range of 0.5 to 50 psig at reaction pressure in the range of 0.5 to 4 atmospheres.

Claim 13

A process for producing high purity isobutene from a C 4 hydrocarbon stream containing isobutene comprising contacting said C 4 hydrocarbon stream and methanol in liquid phase with a macroreticular acid cation exchange resin in a first fixed bed reactor, reacting said isobutene and methanol preferentially to produce MTBE, removing a product stream containing MTBE from the reactor, recovering an MTBE stream from said product stream, feeding a portion of said MTBE stream in vapor phase at an inlet temperature in the range of 110° C. to 150° C. to a second fixed bed reactor containing a macroreticular acid cation exchange resin, the temperature in said fixed bed being in the range of 90° C. to 160° C., said MTBE stream having an LHSV in the range of 7 to 35, dissociating a portion of said MTBE into methanol and isobutene, and recyclying the undissociated MTBE to said first reactor.

Claim 14

A process for producing high purity isobutene from a C 4 hydrocarbon stream containing isobutene comprising contacting said C 4 hydrocarbon stream and methanol in liquid phase with a macroreticular acid cation exchange resin in a first fixed bed reactor, reacting said isobutene and methanol preferentially to produce MTBE, removing a product stream containing MTBE from the reactor, recovering an MTBE stream from said product stream, feeding a portion of said MTBE stream in vapor phase at an inlet temperature in the range of 110° C. to 150° C. to a second fixed bed reactor containing a macroreticular acid cation exchange resin, the temperature in said fixed bed being in the range of 90° C. to 160° C., said MTBE stream having an LHSV in the range of 7 to 35, dissociating a portion of said MTBE into methanol and isobutene, and recyclying the undissociated MTBE to said first reactor.

Claim 15

The process according to claim 12 wherein the inlet temperature of said MTBE stream is in the range of 115° C. to 145° C. and the temperature in said fixed bed is in the range of 120° C. to 150° C.

Claim 16

The process according to claim 13 wherein the LHSV is in the range of 14 to 25.

Claim 17

The process according to claim 12 wherein said second fixed bed reactor is a tubular reactor comprising a plurality of tubes containing said acid cation exchange resin and mounted in a shell and surrounded therein by a heat exchange medium for supplying heat to said fixed bed whereby said heat exchange medium and said vaporized MTBE stream maintain the temperature of said fixed bed.

Claim 18

The process according to claim 12 wherein said MTBE stream comprises at least 95 wt. % MTBE.

Claim 19

The process according to claim 16 wherein said MTBE stream comprises at least 97 wt. % MTBE.

Claim 20

The process according to claim 12 wherein said acid cation exchange resin is thermally stabilized.

Claim 21

The process according to claim 18 wherein said acid cation exchange resin has electron withdrawing groups incorporated therein.

Claim 22

The process according to claim 19 wherein chlorine or bromine groups are incorporated into the resin.

Claim 23

The process according to claim 20 wherein chlorine groups are incorporated into the resin.

Claim 24

A process for producing high purity isobutene by the dissociation of MTBE comprising contacting a stream in vapor phase and containing at least 95% wt. MTBE with a microreticular acid cation exchange resin in a fixed bed, the inlet temperature of the vapor phase being in the range of 115° C. to 145° C. and the temperature in said fixed bed being in the range of 120° C. to 150° C., said stream having an LHSV in the range of 14 to 25, thereby dissociating a portion of said MTBE into methanol and isobutene.

Claim 25

A process for producing high purity isobutene by the dissociation of MTBE comprising contacting a stream in vapor phase and containing at least 95% wt. MTBE with a microreticular acid cation exchange resin in a fixed bed, the inlet temperature of the vapor phase being in the range of 115° C. to 145° C. and the temperature in said fixed bed being in the range of 120° C. to 150° C., said stream having an LHSV in the range of 14 to 25, thereby dissociating a portion of said MTBE into methanol and isobutene.