Production of alkyl aromatic hydrocarbons

Claim 2

An improved method for producing aromatic hydrocarbons from a hydrocarbon charge containing aromatic hydrocarbons including benzene and C 8 alkyl aromatics and aliphatic hydrocarbons which charge is rich in such aromatic hydrocarbons and lean in aliphatic hydrocarbons boiling above about 220°F. by reason of conversion under severe conditions which comprises subjecting said charge to distillation conditions of temperature and pressure such that at least a portion of the benzene content of said fraction is separated as vapor from a alkyl aromatic fraction containing aliphatic hydrocarbons and the major portion of C 8 aromatics in said charge, reacting said alkyl aromatic fraction in the presence of hydrogen in contact with a catalyst containing type ZSM-5 zeolite, Zeolite ZSM-12, zeolite ZSM-21 or zeolite beta in combination with a hydrogenation/dehydrogenation component at conversion conditions to convert aliphatic hydrocarbons to lower boiling material of five carbon atoms and lighter separable from aromatics by distillation including a temperature of about 500° to 1000°F., a pressure of about 100 to about 600 pounds, a hydrogen to hydrocarbon mol ratio of 1 to 6 and weight hourly space velocity of 0.5 to 15 and distilling the product of so reacting said fraction to separate therefrom desired aromatic hydrocarbons substantially free of aliphatics.

Claim 3

A process for manufacture of xylenes from a charge selected from the class consisting of reformate of at least 90 RON clear, pyrolysis gasoline and other hydrocarbon mixtures rich in aromatics and containing non-aromatics in an amount less than about 15 weight percent in the fraction thereof boiling above 220°F., which comprises: a. fractionating the charge to take benzene overhead and recovering a liquid fraction containing the major portion of C 8 aromatics and heavier hydrocarbons of the charge in a fraction which contains less than 15 wt.% non-aromatic hydrocarbons; b. reacting said liquid fraction in contact with a catalyst which contains a hydrogenation metal and a high silica crystalline aluminosilicate zeolite in the presence of hydrogen at conversion conditions to convert aliphatic hydrocarbons to lower boiling material of five carbon atoms and lighter separable from aromatics by distillation including a temperature of about 500° to about 1000°F., a pressure of about 100 to about 600 pounds, a hydrogen to hydrocarbon mol ratio of about 1 to about 6 and space velocity of about 0.5 to about 15 weights of hydrocarbon per weight of said zeolite per hour and distilling the product of so reacting said fraction to separate therefrom desired aromatic hydrocarbons substantially free of aliphatics.

Claim 4

A process for manufacture of xylenes from a charge selected from the class consisting of reformate of at least 90 RON clear, pyrolysis gasoline and other hydrocarbon mixtures rich in aromatics and containing non-aromatics in an amount less than about 15 weight percent in the fraction thereof boiling above 220°F., which comprises: a. fractionating the charge to take benzene overhead and recovering a liquid fraction containing the major portion of C 8 aromatics and heavier hydrocarbons of the charge in a fraction which contains less than 15 wt.% non-aromatic hydrocarbons; b. reacting said liquid fraction in contact with a catalyst which contains a hydrogenation metal and a high silica crystalline aluminosilicate zeolite in the presence of hydrogen at conversion conditions to convert aliphatic hydrocarbons to lower boiling material of five carbon atoms and lighter separable from aromatics by distillation including a temperature of about 500° to about 1000°F., a pressure of about 100 to about 600 pounds, a hydrogen to hydrocarbon mol ratio of about 1 to about 6 and space velocity of about 0.5 to about 15 weights of hydrocarbon per weight of said zeolite per hour and distilling the product of so reacting said fraction to separate therefrom desired aromatic hydrocarbons substantially free of aliphatics.

Claim 5

A process for the manufacture of a xylene isomer by supplying a feed stream containing C 8 hydrocarbons to a process loop which includes the steps of separating a desired xylene isomer, subjecting the remaining hydrocarbons lean in desired isomer to catalytic isomerization which provides additional amounts of the desired isomer together with by-product hydrocarbons of lower and higher boiling point than C 8 aromatics, fractionating the isomerization effluent to remove said by-products of higher and lower boiling point and returning to said separation step the fraction of isomerization effluent from which by-products have been removed; the improvement which comprises fractionating a hydrocarbon charge rich in aromatics including benzene and C 8 alkyl aromatics and lean in non-aromatics boiling above about 220°F. to remove therefrom at least a substantial portion of the benzene content thereof together with lighter hydrocarbons and leave an aromatic fraction containing substantially all of the eight carbon atom aromatics of said charge, reacting said aromatic fraction in the presence of hydrogen by contact with a catalyst containing a hydrogenation component and a high silica crystalline aluminosilicate zeolite having at least a portion of its cations in the hydrogen form at conversion conditions to convert aliphatic hydrocarbons to lower boiling material of five carbon atoms and lighter separable from aromatics by distillation including a temperature of about 500 to about 1000°F., a pressure of about 100 to 600 pounds, a hydrogen to hydrocarbon mol ratio of about 1 to 6 and weight hourly space velocity with respect to said zeolite of about 0.5 to about 15, and mixing the hydrocarbon products of said reaction with the hydrocarbon effluent of said isomerization step whereby the said hydrocarbon products of said reaction and hydrocarbon effluent of said isomerization are fractionated together to provide recycle and fresh feed for said separation step.

Claim 6

A process for the manufacture of a xylene isomer by supplying a feed stream containing C 8 hydrocarbons to a process loop which includes the steps of separating a desired xylene isomer, subjecting the remaining hydrocarbons lean in desired isomer to catalytic isomerization which provides additional amounts of the desired isomer together with by-product hydrocarbons of lower and higher boiling point than C 8 aromatics, fractionating the isomerization effluent to remove said by-products of higher and lower boiling point and returning to said separation step the fraction of isomerization effluent from which by-products have been removed; the improvement which comprises fractionating a hydrocarbon charge rich in aromatics including benzene and C 8 alkyl aromatics and lean in non-aromatics boiling above about 220°F. to remove therefrom at least a substantial portion of the benzene content thereof together with lighter hydrocarbons and leave an aromatic fraction containing substantially all of the eight carbon atom aromatics of said charge, reacting said aromatic fraction in the presence of hydrogen by contact with a catalyst containing a hydrogenation component and a high silica crystalline aluminosilicate zeolite having at least a portion of its cations in the hydrogen form at conversion conditions to convert aliphatic hydrocarbons to lower boiling material of five carbon atoms and lighter separable from aromatics by distillation including a temperature of about 500 to about 1000°F., a pressure of about 100 to 600 pounds, a hydrogen to hydrocarbon mol ratio of about 1 to 6 and weight hourly space velocity with respect to said zeolite of about 0.5 to about 15, and mixing the hydrocarbon products of said reaction with the hydrocarbon effluent of said isomerization step whereby the said hydrocarbon products of said reaction and hydrocarbon effluent of said isomerization are fractionated together to provide recycle and fresh feed for said separation step.

Claim 7

The method of claim 1 wherein said hydrocarbon charge rich in aromatic hydrocarbons is a reformate prepared by severe reforming of a petroleum naphtha in admixture with hydrogen over platinum on alumina catalyst.

Claim 8

The method of claim 1 wherein the catalyst contacted with said alkyl aromatic fraction is the nickel and hydrogen form of zeolite ZSM-5.

Claim 9

The process of claim 2 wherein the catalyst of step (b) is the nickel and hydrogen form of zeolite ZSM-5.

Claim 10

The process of claim 3 wherein the hydrocarbon charge rich in aromatics is a reformate prepared by severe reforming of a petroleum naphtha in admixture with hydrogen over platinum on alumina catalyst.

Claim 11

The process of claim 3 wherein the high silica crystalline aluminosilicate zeolite is the hydrogen and nickel form of zeolite ZSM-5.

Claim 12

A process according to claim 2 wherein said conversion conditions are such as to produce toluene from aromatic components of said alkyl aromatic fraction and toluene is separated from said product of said contacting with catalyst, such separated toluene is admixed with said liquid fraction and the mixture is contacted with catalyst as aforesaid.

Claim 13

A process according to claim 2 wherein C 9 + aromatics are components of said alkyl aromatic fraction and C 9 + aromatics are separated from said product of said contacting with catalyst, such separated aromatics are admixed with said liquid fraction and the mixture is contacted with catalyst as aforesaid.