Process for conversion of light aliphatic hydrocarbons to aromatics

Claim 2

In a hydrocarbon conversion process wherein a vapor phase feedstream comprising a C 2 -C 5 aliphatic hydrocarbon is passed into a catalytic reaction zone containing a solid catalyst and converted into aromatic hydrocarbons comprising benzene, toluene and xylenes which are recovered from a reaction zone effluent stream; the improvement which comprises charging benzene and/or toluene into the reaction zone to increase the relative production of xylenes.

Claim 3

The improvement of claim 1 further characterized in that the aromatics charged to the reaction zone are recovered from an effluent stream emanating from the reaction zone.

Claim 4

The process of claim 1 further characterized in that the feed stream is rich in C 3 hydrocarbons.

Claim 5

The process of claim 1 further characterized in that the feed stream is rich in C 4 hydrocarbons.

Claim 6

In a dehydrocyclodimerization process wherein a vapor phase feedstream comprising propane or butane is passed into a reaction zone maintained at dehydrocyclodimerization conditions and a reaction zone effluent stream comprising benzene, toluene, xylenes and propane or butane is passed into a product recovery zone, and xylene is recovered as a product; the improvement which comprises recovering benzene from the reaction zone effluent stream and recycling benzene to the reaction zone.

Claim 7

In a dehydrocyclodimerization process wherein a vapor phase feedstream comprising propane or butane is passed into a reaction zone maintained at dehydrocyclodimerization conditions and a reaction zone effluent stream comprising benzene, toluene, xylenes and propane or butane is passed into a product recovery zone, and xylene is recovered as a product; the improvement which comprises recovering benzene from the reaction zone effluent stream and recycling benzene to the reaction zone.

Claim 8

The process of claim 5 further characterized in that a solid catalyst comprising a zeolite is employed within the reaction zone.

Claim 9

The process of claim 6 further characterized in that the catalyst comprises gallium.

Claim 10

The process of claim 7 further characterized in that the concentration of benzene in the hydrocarbons entering the reaction zone is from about 2.5 to about 8.0 mole percent.

Claim 11

A process for the production of aromatic hydrocarbons which comprises the steps of: (a) passing a first process stream comprising benzene and a feedstream comprising a C 2 -C 5 aliphatic feed hydrocarbon into a reaction zone maintained at dehydrocyclodimerization conditions and containing a solid catalyst and producing a reaction zone effluent stream which comprises the feed hydrocarbon, benzene, toluene and xylenes; and, (b) separating the reaction zone effluent stream in a separation zone and producing a product stream comprising xylenes.

Claim 12

A process for the production of aromatic hydrocarbons which comprises the steps of: (a) passing a first process stream comprising benzene and a feedstream comprising a C 2 -C 5 aliphatic feed hydrocarbon into a reaction zone maintained at dehydrocyclodimerization conditions and containing a solid catalyst and producing a reaction zone effluent stream which comprises the feed hydrocarbon, benzene, toluene and xylenes; and, (b) separating the reaction zone effluent stream in a separation zone and producing a product stream comprising xylenes.

Claim 13

The process of claim 9 further characterized in that the feedstream is rich in C 3 hydrocarbons.

Claim 14

The process of claim 9 further characterized in that the feedstream is rich in C 4 hydrocarbons.

Claim 15

The process of claim 9 further characterized in that the catalyst comprises a zeolite.

Claim 16

The process of claim 12 further characterized in that the catalyst comprises gallium.

Claim 17

The process of claim 9 further characterized in that the separation zone effluent stream is separated by a series of steps which comprise fractional distillation and a benzene-rich second process stream is also produced, and in that at least a portion of the second process stream is passed into the reaction zone as the previously referred to first process stream.

Claim 18

The process of claim 14 further characterized in that the benzene-rich second process stream comprises toluene.

Claim 19

A dehydrocyclodimerization process which comprises the steps of: (a) passing a feedstream which comprises a C 3 or C 4 aliphatic hydrocarbon and a first process stream which comprises benzene into a dehydrocyclodimerization reaction zone maintained at dehydrocyclodimerization conditions and containing a solid catalyst comprising a zeolite and producing a reaction zone effluent stream comprising benzene, toluene and xylenes; (b) separating the reaction zone effluent stream by a series of steps comprising partial condensation and fractional distillation and producing a product stream comprising xylenes and a second process stream comprising benzene; and, (c) recycling at least a portion of the second process stream to the reaction zone as the previously referred to first process stream.

Claim 20

A dehydrocyclodimerization process which comprises the steps of: (a) passing a feedstream which comprises a C 3 or C 4 aliphatic hydrocarbon and a first process stream which comprises benzene into a dehydrocyclodimerization reaction zone maintained at dehydrocyclodimerization conditions and containing a solid catalyst comprising a zeolite and producing a reaction zone effluent stream comprising benzene, toluene and xylenes; (b) separating the reaction zone effluent stream by a series of steps comprising partial condensation and fractional distillation and producing a product stream comprising xylenes and a second process stream comprising benzene; and, (c) recycling at least a portion of the second process stream to the reaction zone as the previously referred to first process stream.

Claim 21

The process of claim 16 further characterized in that the catalyst comprises gallium.

Claim 22

The process of claim 17 further characterized in that the feedstream is rich in butanes.

Claim 23

The process of claim 16 further characterized in that the concentration of benzene in the hydrocarbons entering the dehydrocyclodimerization reaction zone is from about 2.5 to about 8.0 mole percent.