Regeneration of aromatics processing catalysts

Claim 2

In a process for the conversion of an aromatic containing feedstock in which said feedstock is contacted in a reactor vessel, under conversion conditions, with a catalyst comprising a ZSM-5 type zeolite having a silica to alumina mole ratio of at least 12 and a constraint index within the approximate range of 1 to 12, and which includes a regeneration step to burn off carbonaceous materials which deposit on said catalyst, said regeneration step comprising contacting said catalyst containing carbonaceous materials with a continuous closed loop flow of a gas stream comprising oxidizing gas and steam at regeneration conditions including a steam partial pressure of between about 0.1 psi and about 4.0 psi, a contact time of between about 12 hours and about 72 hours and a temperature of between about 700° F. and about 1000° F. the improvement which comprises: (a) removing from said continuous closed loop flow a portion of said gas stream, and (b) introducing into said continuous closed loop flow a quantity of a low moisture content, molecular-oxygen containing gas, said portion and said quantity being effective, collectively, to maintain, in the closed loop flow at the inlet to said reactor vessel, a molecular oxygen content no greater than about 1.0 mole percent and a water partial pressure no greater than about 1.0 psi.

Claim 3

A process according to claim 1 wherein the molecular-oxygen containing gas comprises air.

Claim 4

A process according to claim 1 wherein the molecular-oxygen containing gas comprises oxygen and an inert gas.

Claim 5

A process according to claim 3 wherein the inert gas comprises nitrogen.

Claim 6

A process according to claim 1 wherein the molecular-oxygen containing gas is a mixture of air and nitrogen.

Claim 7

A process according to claim 1 wherein the low moisture content molecular oxygen containing gas has a dew point of less than about -15° F.

Claim 8

A process according to claim 1 including the following additional step: (c) following the breakthrough of oxygen in the gas stream leaving said reactor vessel, increasing the molecular oxygen content at the inlet to said reactor vessel above about 1.0 mole percent while maintaining the water partial pressure at no greater than about 1.0 psi until there is essentially no temperature difference across the catalyst bed.

Claim 9

A process according to claim 1 wherein the zeolite is ZSM-5, ZSM-11, ZSM-12, ZSM-35 or ZSM-38.

Claim 10

A process according to claim 1 wherein the zeolite is ZSM-5.

Claim 11

A process according to claim 1 wherein the feedstock is a mixture of eight carbon atom aromatic hydrocarbon compounds comprising xylene and ethylbenzene and the conversion is xylene isomerization.

Claim 12

A process according to claim 10 wherein the zeolite has been steamed under conditions of temperature, pressure and time such that the steamed zeolite requires an increased isomerization reaction temperature of at least 50° F. to equal the ethylbenzene conversion by the unsteamed zeolite.

Claim 13

In a process for isomerizing the xylene content of a charge mixture of eight carbon atom aromatic hydrocarbon compounds which mixture contains xylene and ethylbenzene by contact at conversion conditions including a temperature of about 700° to about 1000° F. with a catalyst comprising a ZSM-5 type zeolite having a silica/alumina ratio greater than 12 and a constraint index of 1 to 12, said zeolite having been steamed prior to said contact under temperature and pressure conditions and a period of time such that the steamed zeolite requires an increased reaction temperature of at least 50° F. to equal the ethylbenzene conversion by the unsteamed zeolite and regenerating said catalyst to burn off carbonaceous materials which deposit on said catalyst by contacting said catalyst containing carbonaceous materials with a continuous closed loop flow of a gas stream comprising molecular-oxygen containing gas under regeneration conditions comprising a water partial pressure of between about 0.1 and about 1.0 psi, a contact time of between about 12 and about 120 hours and a temperature of between about 700° and about 925° F., the improvement in the regeneration which comprises: (a) removing from said continuous closed loop flow a portion of said gas stream, and (b) introducing into said continuous closed loop flow a quantity of a low moisture content, molecular-oxygen containing gas, said portion and said quantity being effective, collectively, to maintain, in the closed loop flow at the inlet to said reactor vessel, a molecular oxygen content no greater than about 1.0 mole percent and a water partial pressure no greater than about 1.0 psi.

Claim 14

In a process for isomerizing the xylene content of a charge mixture of eight carbon atom aromatic hydrocarbon compounds which mixture contains xylene and ethylbenzene by contact at conversion conditions including a temperature of about 700° to about 1000° F. with a catalyst comprising a ZSM-5 type zeolite having a silica/alumina ratio greater than 12 and a constraint index of 1 to 12, said zeolite having been steamed prior to said contact under temperature and pressure conditions and a period of time such that the steamed zeolite requires an increased reaction temperature of at least 50° F. to equal the ethylbenzene conversion by the unsteamed zeolite and regenerating said catalyst to burn off carbonaceous materials which deposit on said catalyst by contacting said catalyst containing carbonaceous materials with a continuous closed loop flow of a gas stream comprising molecular-oxygen containing gas under regeneration conditions comprising a water partial pressure of between about 0.1 and about 1.0 psi, a contact time of between about 12 and about 120 hours and a temperature of between about 700° and about 925° F., the improvement in the regeneration which comprises: (a) removing from said continuous closed loop flow a portion of said gas stream, and (b) introducing into said continuous closed loop flow a quantity of a low moisture content, molecular-oxygen containing gas, said portion and said quantity being effective, collectively, to maintain, in the closed loop flow at the inlet to said reactor vessel, a molecular oxygen content no greater than about 1.0 mole percent and a water partial pressure no greater than about 1.0 psi.

Claim 15

A process according to claim 12 wherein the molecular-oxygen containing gas comprises air.

Claim 16

A process according to claim 12 wherein the molecular-oxygen containing gas comprises oxygen and an inert gas.

Claim 17

A process according to claim 14 wherein the inert gas comprises nitrogen.

Claim 18

A process according to claim 12 wherein the molecular-oxygen containing gas is a mixture of air and nitrogen.

Claim 19

A process according to claim 12 wherein the low moisture content molecular oxygen containing gas has a dew point of less than about -15° F.

Claim 20

A process according to claim 12 including the following additional step: (c) following the breakthrough of oxygen in the gas stream leaving said reactor vessel, increasing the molecular oxygen content at the inlet to said reactor vessel above about 1.0 mole percent while maintaining the water partial pressure at no greater than about 1.0 psi until there is essentially no temperature difference across the catalyst bed.

Claim 21

A process according to claim 12 wherein the zeolite is ZSM-5, ZSM-11, ZSM-12, ZSM-35 or ZSM-38.

Claim 22

A process according to claim 12 wherein the zeolite is ZSM-5.