Process for the hydrotreatment of hydrocarbons in an expanded or ebullated catalyst bed

Claim 2

In a process for the hydrotreatment, hydrovisbreaking or hydroconversion of hydrocarbons, wherein a liquid hydrocarbon charge and a hydrogen-containing gas are contacted with a solid catalyst, in a reaction zone having substantially the shape of an elongate, substantially vertical volume of revolution, containing the catalyst and having a perforated wall at its lower end which supports the catalyst bed, at least a part of the liquid charge and the hydrogen-containing gas being introduced into the lower part of the reaction zone below said perforated wall, the liquid and gaseous effluent being withdrawn at the upper part of the reaction zone after passage upwardly therethrough, the catalyst particles being introduced at the upper part of the reaction zone and being withdrawn periodically or at the end of the charge treatment from the lower part of the reaction zone through at least one opening provided in said perforated supporting wall, said opening being sufficiently large to permit discharge therethrough of catalyst particles, said perforated supporting wall being provided with a plurality of spaced perforations whose size is sufficiently small to prevent catalyst particles from passing therethrough but sufficiently large to permit upward passage therethrough of fluid charge and hydrogen, the improvment wherein said catalyst is in the form of an expanded or ebullated bed, the expansion and/or ebullition thereof being maintained by the passage therethrough of a fluid mixture of charge and hydrogen-containing gas, the liquid charge and hydrogen-containing gas being injected as a fluid mixture, at least a portion of which is injected into the lower part of said reaction zone through at least one distribution zone located below said perforated support wall, said wall being substantially horizontal, each said distribution zone comprising a distribution ramp terminating in a substantially vertical injection pipe and feeding a plurality of radial branches in a star-shaped array, each branch being provided with a plurality of orifices wherethrough a portion of said fluid mixture is injected into said reaction zone.

Claim 3

A process according to claim 1, wherein the reaction zone is of elongate cylindrical shape.

Claim 4

A process according to claim 1, wherein the branches in star-shaped array are substantially horizontal.

Claim 5

A process according to claim 1, wherein said branches are inclined by an inclination angle of between 0° and 40° to a horizontal line.

Claim 6

A process according to claim 1, wherein said branches are of undulated shape.

Claim 7

A process according to claim 1, wherein the catalyst bed is expanded by about 10-30% by volume with respect to the resting volume of the bed.

Claim 8

In a process for the hydrotreatment, hydrovisbreaking or hydroconversion of hydrocarbons, wherein a liquid hydrocarbon charge and a hydrogen-containing gas are contacted with a solid catalyst, in a reaction zone having substantially the shape of an elongate, substantially vertical volume of revolution, containing the catalyst and having a perforated wall at its lower end which supports the catalyst bed, at least a part of the liquid charge and the hydrogen-containing gas being introduced into the lower part of the reaction zone below said perforated wall, the liquid and gaseous effluent being withdrawn at the upper part of the reaction zone after passage upwardly therethrough, the catalyst particles being introduced at the upper part of the reaction zone and being withdrawn periodically or at the end of the charge treatment from the lower part of the reaction zone through at least one opening provided in said perforated supporting wall, said opening being sufficiently large to permit discharge therethrough of catalyst particles, said perforated supporting wall being provided with a plurality of spaced perforations whose size is sufficiently small to prevent catalyst particles from passing therethrough but sufficiently large or permit upward passage therethrough of fluid charge and hydrogen, the improvement wherein said catalyst is in the form of an expanded or ebullated bed, the expansion and/or ebullition thereof being maintained by the passage therethrough of a fluid mixture of charge and hydrogen-containing gas, the liquid charge and hydrogen-containing gas being injected as a fluid mixture, at least a portion of which is injected into the lower part of said reaction zone through at least one distribution zone located below said perforated support wall, said wall being substantially horizontal, said fluid mixture being directed towards said support wall; and wherein a turbulent mixing means is disposed between said distribution zone and said support wall, comprising as its upper component a perforated horizontal plate having a plurality of orifices therein sufficiently large to permit passage therethrough of the major part of the gaseous phase of said fluid mixture but sufficiently narrow to prevent passage therethrough of the major part of the liquid phase of said fluid mixture, said plate having a plurality of spaced openings therein, from each of which extends downwardly a substantially vertical chimney; whereby the injected fluid mixture accumulates in the space beneath said plate and around said chimneys and generates liquid and gaseous clusters, the major part of the gaseous phase passing through said orifices, and the major part of the liquid phase being pushed up through said chimneys and through the openings in said plate, the liquid and gaseous phases being admixed above said plate to produce a turbulent fluid mixture which enters said reaction zone and expands and/or ebullates said catalyst.

Claim 9

In a process for the hydrotreatment, hydrovisbreaking or hydroconversion of hydrocarbons, wherein a liquid hydrocarbon charge and a hydrogen-containing gas are contacted with a solid catalyst, in a reaction zone having substantially the shape of an elongate, substantially vertical volume of revolution, containing the catalyst and having a perforated wall at its lower end which supports the catalyst bed, at least a part of the liquid charge and the hydrogen-containing gas being introduced into the lower part of the reaction zone below said perforated wall, the liquid and gaseous effluent being withdrawn at the upper part of the reaction zone after passage upwardly therethrough, the catalyst particles being introduced at the upper part of the reaction zone and being withdrawn periodically or at the end of the charge treatment from the lower part of the reaction zone through at least one opening provided in said perforated supporting wall, said opening being sufficiently large to permit discharge therethrough of catalyst particles, said perforated supporting wall being provided with a plurality of spaced perforations whose size is sufficiently small to prevent catalyst particles from passing therethrough but sufficiently large or permit upward passage therethrough of fluid charge and hydrogen, the improvement wherein said catalyst is in the form of an expanded or ebullated bed, the expansion and/or ebullition thereof being maintained by the passage therethrough of a fluid mixture of charge and hydrogen-containing gas, the liquid charge and hydrogen-containing gas being injected as a fluid mixture, at least a portion of which is injected into the lower part of said reaction zone through at least one distribution zone located below said perforated support wall, said wall being substantially horizontal, said fluid mixture being directed towards said support wall; and wherein a turbulent mixing means is disposed between said distribution zone and said support wall, comprising as its upper component a perforated horizontal plate having a plurality of orifices therein sufficiently large to permit passage therethrough of the major part of the gaseous phase of said fluid mixture but sufficiently narrow to prevent passage therethrough of the major part of the liquid phase of said fluid mixture, said plate having a plurality of spaced openings therein, from each of which extends downwardly a substantially vertical chimney; whereby the injected fluid mixture accumulates in the space beneath said plate and around said chimneys and generates liquid and gaseous clusters, the major part of the gaseous phase passing through said orifices, and the major part of the liquid phase being pushed up through said chimneys and through the openings in said plate, the liquid and gaseous phases being admixed above said plate to produce a turbulent fluid mixture which enters said reaction zone and expands and/or ebullates said catalyst.

Claim 10

A process according to claim 7, wherein the reaction zone is of elongate cylindrical shape.

Claim 11

A process according to claim 7, wherein the catalyst bed is expanded by about 10-30% by volume with respect to the resting volume of the bed.

Claim 12

In a process for the hydrotreatment, hydrovisbreaking or hydroconversion of hydrocarbons, wherein a liquid hydrocarbon charge and a hydrogen-containing gas are contacted with a solid catalyst, in a reaction zone having substantially the shape of an elongate, substantially vertical volume of revolution, containing the catalyst and having a perforated wall at its lower end which supports the catalyst bed, at least a part of the liquid charge and the hydrogen-containing gas being introduced into the lower part of the reaction zone below said perforated wall, the liquid and gaseous effluent being withdrawn at the upper part of the reaction zone after passage upwardly therethrough, the catalyst particles being introduced at the upper part of the reaction zone and being withdrawn periodically or at the end of the charge treatment from the lower part of the reaction zone through at least one opening provided in said perforated supporting wall, said opening being sufficiently large to permit discharge therethrough of catalyst particles, said perforated supporting wall being provided with a plurality of spaced perforations whose size is sufficiently small to prevent catalyst particles from passing therethrough but sufficiently large to permit upward passage therethrough of fluid charge and hydrogen, the improvement wherein said catalyst is in the form of an expanded or ebullated bed, the expansion and/or ebullition thereof being maintained by the passage therethrough of a fluid mixture of charge and hydrogen-containing gas, the liquid charge and hydrogen-containing gas being injected as a fluid mixture, at least a portion of which is injected into the lower part of said reaction zone through at least one distribution zone located below said perforated support wall, said wall being substantially horizontal, said fluid mixture being directed toward said support wall; and wherein a plurality of juxtaposed cellular layers is disposed between said distribution zone and said support wall, said cellular layers providing a plurality of divided passages therethrough; whereby said fluid mixture passes through said passages and into said reaction zone to produce a regular and homogeneous expansion and/or ebullition of said catalyst.

Claim 13

In a process for the hydrotreatment, hydrovisbreaking or hydroconversion of hydrocarbons, wherein a liquid hydrocarbon charge and a hydrogen-containing gas are contacted with a solid catalyst, in a reaction zone having substantially the shape of an elongate, substantially vertical volume of revolution, containing the catalyst and having a perforated wall at its lower end which supports the catalyst bed, at least a part of the liquid charge and the hydrogen-containing gas being introduced into the lower part of the reaction zone below said perforated wall, the liquid and gaseous effluent being withdrawn at the upper part of the reaction zone after passage upwardly therethrough, the catalyst particles being introduced at the upper part of the reaction zone and being withdrawn periodically or at the end of the charge treatment from the lower part of the reaction zone through at least one opening provided in said perforated supporting wall, said opening being sufficiently large to permit discharge therethrough of catalyst particles, said perforated supporting wall being provided with a plurality of spaced perforations whose size is sufficiently small to prevent catalyst particles from passing therethrough but sufficiently large to permit upward passage therethrough of fluid charge and hydrogen, the improvement wherein said catalyst is in the form of an expanded or ebullated bed, the expansion and/or ebullition thereof being maintained by the passage therethrough of a fluid mixture of charge and hydrogen-containing gas, the liquid charge and hydrogen-containing gas being injected as a fluid mixture, at least a portion of which is injected into the lower part of said reaction zone through at least one distribution zone located below said perforated support wall, said wall being substantially horizontal, said fluid mixture being directed toward said support wall; and wherein a plurality of juxtaposed cellular layers is disposed between said distribution zone and said support wall, said cellular layers providing a plurality of divided passages therethrough; whereby said fluid mixture passes through said passages and into said reaction zone to produce a regular and homogeneous expansion and/or ebullition of said catalyst.

Claim 14

A process according to claim 10, wherein the reaction zone is of elongate cylindrical shape.

Claim 15

A process according to claim 10, wherein said distribution zone comprises break-jet means to provide a spray of fluid to said cellular layers.

Claim 16

A process according to claim 10, wherein the catalyst bed is expanded by about 10-30% by volume with respect to the resting volume of the bed.