Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
263 words
A combination xylene separation and a toluene transalkylation process, for producing benzene and orthoxylene comprising the steps of: a. transalkylating a mixture of toluene and C 9 alkylbenzene in a transalkylation zone at transalkylation conditions to produce a transalkylation zone effluent comprising benzene, toluene, C 8 alkylbenzenes, C 9 alkylbenzenes, and C 10 alkylbenzenes; b. fractionating at least a portion of said transalkylation zone effluent in a distillation column wherein benzene and toluene are recovered as an overhead fraction and materials heavier than toluene are recovered as a bottoms fraction; c. fractionating said benzene and toluene fraction in a fractionation column to produce a benzene product and to recover a toluene-rich stream which comprises at least a portion of the charge to the transalkylation zone; d. passing at least a portion of said bottoms fraction, comprising material heavier than toluene, into a xylene fractionator, and recovering overhead a stream comprising orthoxylene and recovering as a bottoms fraction a stream comprising C 9 and C 10 alkylbenzenes; e. passing the C 9 and C 10 alkylbenzene bottoms fraction to a fractionation zone to recover overhead a stream comprising C 9 alkylbenzenes, at least a portion of which C 9 alkylbenzenes stream is charged to the transalkylation zone; f. reboiling the column producing benzene product by indirect heat exchange with vapors from the column producing C 9 alkylbenzenes as an overhead fraction; and, g. reboiling the column producing benzene and toluene as an overhead fraction by indirect heat exchange with a stream comprising orthoxylene vapors obtained as an overhead vapor fraction from the xylene fractionator.
Claim 2
Dependent Claim
263 words
A combination xylene separation and a toluene transalkylation process, for producing benzene and orthoxylene comprising the steps of: a. transalkylating a mixture of toluene and C 9 alkylbenzene in a transalkylation zone at transalkylation conditions to produce a transalkylation zone effluent comprising benzene, toluene, C 8 alkylbenzenes, C 9 alkylbenzenes, and C 10 alkylbenzenes; b. fractionating at least a portion of said transalkylation zone effluent in a distillation column wherein benzene and toluene are recovered as an overhead fraction and materials heavier than toluene are recovered as a bottoms fraction; c. fractionating said benzene and toluene fraction in a fractionation column to produce a benzene product and to recover a toluene-rich stream which comprises at least a portion of the charge to the transalkylation zone; d. passing at least a portion of said bottoms fraction, comprising material heavier than toluene, into a xylene fractionator, and recovering overhead a stream comprising orthoxylene and recovering as a bottoms fraction a stream comprising C 9 and C 10 alkylbenzenes; e. passing the C 9 and C 10 alkylbenzene bottoms fraction to a fractionation zone to recover overhead a stream comprising C 9 alkylbenzenes, at least a portion of which C 9 alkylbenzenes stream is charged to the transalkylation zone; f. reboiling the column producing benzene product by indirect heat exchange with vapors from the column producing C 9 alkylbenzenes as an overhead fraction; and, g. reboiling the column producing benzene and toluene as an overhead fraction by indirect heat exchange with a stream comprising orthoxylene vapors obtained as an overhead vapor fraction from the xylene fractionator.
Claim 3
Dependent Claim
37 words
Process of claim 1 wherein the xylene fractionator is a single fractionator, wherein C 8 alkylbenzenes, including orthoxylene, are recovered as an overhead vapor fraction and C 9 and heavier alkylbenzenes are recovered as a bottoms fraction.
Claim 4
Dependent Claim
62 words
Process of claim 1 wherein the xylene fractionator comprises two fractionators, a xylene splitter wherein meta- and para-xylene are recovered as an overhead fraction and orthoxylene and heavier alkylbenzenes recovered as a bottoms fraction are charged to an orthoxylene column wherein orthoxylene is recovered overhead as an overhead vapor fraction and C 9 and heavier alkylbenzenes are recovered as a bottoms fraction.
Claim 5
Dependent Claim
33 words
Process of claim 3 wherein the meta- and para-xylene overhead fraction is charged to an isomerization zone and at least a portion of the isomerization zone effluent is charged to the xylene splitter.
Claim 6
Dependent Claim
49 words
Process of claim 1 wherein the transalkylation zone effluent also contains alkylbenzenes heavier than C 10 and wherein the fractionator in step (e) recovers overhead a stream comprising C 9 and C 10 alkylbenzenes and recovers as a bottoms fraction a stream comprising alkylaromatics heavier than C 10 .