Process for preparation of anhydrous metallic chlorides from waste catalysts

Claim 2

A process for preparation from waste catalysts on an alumina support base which have been used for the treatment of hydrocarbons, of anhydrous metallic chlorides selected from the group consisting of chlorides of aluminum, molybdenum, vanadium, cobalt and nickel, comprising: (a) separating hydrocarbons which impregnated the waste catalyst support base during use, under conditions wherein a major portion of carbon present in an uncombined state is not oxidized or removed from within the alumina support base; (b) chlorinating the waste catalyst treated as in step (a) by subjecting the catalyst to a flow of gaseous chlorine at a temperature sufficient to sequentially reduce metal oxides present and form volatile and non-volatile chlorides of the reduced metals; (c) passing a gaseous effluent of (b) through an anhydrous sodium chloride at a temperature of between about 115° C. to about 500° C. to selectively fix the aluminum chloride in the form of a complex salt or mixture of low melting point salts; and; (d) at least recovering an aluminum chloride product.

Claim 3

The process as in claim 1, wherein after selective fixation of aluminum chloride by anhydrous sodium chloride, gases which are not retained are passed through an absorption column which contains generally nonanhydrous crystallized potassium chloride brought to a temperature of 100° to 500° C., which fixes the major part of the molybdenum chloride.

Claim 4

The process as in claim 1, wherein the separation of the hydrocarbons impregnated in the waste catalyst is effected by combustion at a temperature of 300° to 500° C.

Claim 5

The process as in claim 2, wherein the separation of the hydrocarbons impregnated in the waste catalyst is effected by combustion at a temperature of 300° to 500° C.

Claim 6

The process as in claim 1, wherein the separation of the hydrocarbons is effected by contact with nitrogen at a temperature between 300° to 500° C.

Claim 7

The process as in claim 2, wherein the separation of the hydrocarbons is effected by contact with nitrogen at a temperature between 300° and 500° C.

Claim 8

The process as in claim 2, wherein the gases issuing from the molybdenum chloride absorption column pass into a condenser at a temperature of approximately 60° to 100° C., to retain vanadium chloride.

Claim 9

The process as in claim 4, wherein the gases issuing from the molybdenum chloride absorption column pass into a condenser at a temperature of approximately 60° to 100° C., to retain vanadium chloride.

Claim 10

The process as in claim 6, wherein the gases issuing from the molybdenum chloride absorption column pass into a condenser at a temperature of approximately 60° to 100° C., to retain vanadium chloride.

Claim 11

The process as in claim 2, wherein the gases issuing from the molybdenum chloride absorption column are bubbled into water which retains a portion of the vanadium tetrachloride, and wherein the solution obtained is treated by ammonium chloride or a metallic chloride, in a basic milieu, to precipitate an insoluble vanadate.

Claim 12

The process as in claim 4, wherein the gases issuing from the molybdenum chloride absorption column are bubbled into water which retains a portion of the vanadium tetrachloride, and wherein the solution obtained is treated by ammonium chloride or a metallic chloride, in a basic milieu, to precipitate an insoluble vanadate.

Claim 13

The process as in claim 6, wherein the gases issuing from the molybdenum chloride absorption column are bubbled into water which retains a portion of the vanadium tetrachloride, and wherein the solution obtained is treated by ammonium chloride or a metallic chloride, in a basic milieu, to precipitate an insoluble vanadate.

Claim 14

The process as in claim 1, wherein a solid residue from the chlorination of the catalyst is treated by water to dissolve the Co and Ni chlorides which are thereafter recovered.

Claim 15

A process for preparation from waste catalysts on an alumina support base which have been used for the treatment of hydrocarbons, of anhydrous metallic chlorides selected from the group consisting of chlorides of aluminum, molybdenum, vanadium, cobalt and nickel, comprising: (a) separating hydrocarbons which impregnated the waste catalyst support base during use, under conditions wherein a major portion of carbon present in an uncombined state is not oxidized or removed from within the alumina support base; (b) chlorinating the waste catalyst treated as in step (a) by subjecting the catalyst to a flow of gaseous chlorine at a temperature sufficient to sequentially reduce metal oxides present and form volatile and non-volatile chlorides of the reduced metals; (c) passing a gaseous effluent of (b) through an anhydrous sodium chloride at a temperature of between about 115° C. to about 500° C. to selectively fix the aluminum chloride in the form of a complex salt or mixture of low melting point salts; (d) at least recovering an aluminum chloride product; and wherein after selective fixation of aluminum chloride by an anhydrous sodium chloride, gases which are not retained are passed through an absorption column which contains generally non-anhydrous crystallized potassium chloride brought to a temperature of 100° to 500° C., which fixes the major part of the molybdenum chloride.

Claim 16

A process for preparation from waste catalysts on an alumina support base which have been used for the treatment of hydrocarbons, of anhydrous metallic chlorides selected from the group consisting of chlorides of aluminum, molybdenum, vanadium, cobalt and nickel, comprising: (a) separating hydrocarbons which impregnated the waste catalyst support base during use, under conditions wherein a major portion of carbon present in an uncombined state is not oxidized or removed from within the alumina support base; (b) chlorinating the waste catalyst treated as in step (a) by subjecting the catalyst to a flow of gaseous chlorine at a temperature sufficient to sequentially reduce metal oxides present and form volatile and non-volatile chlorides of the reduced metals; (c) passing a gaseous effluent of (b) through an anhydrous sodium chloride at a temperature of between about 115° C. to about 500° C. to selectively fix the aluminum chloride in the form of a complex salt or mixture of low melting point salts; (d) at least recovering an aluminum chloride product; and wherein after selective fixation of aluminum chloride by an anhydrous sodium chloride, gases which are not retained are passed through an absorption column which contains generally non-anhydrous crystallized potassium chloride brought to a temperature of 100° to 500° C., which fixes the major part of the molybdenum chloride.

Claim 17

The process as in claim 14, wherein the separation of the hydrocarbons impregnated in the waste catalyst is effected by combustion at a temperature of 300° to 500° C.

Claim 18

The process as in claim 14, wherein the separation of the hydrocarbons is effected by contact with nitrogen at a temperature between 300° and 500° C.

Claim 19

The process as in claim 14, wherein the gases issuing from the molybdenum chloride absorption column pass into a condenser at a temperature of approximately 60° to 100° C., to retain vanadium chloride.

Claim 20

The process as in claim 14, wherein the gases issuing from the molybdenum chloride absorption column are bubbled into water which retains a portion of the vanadium tetrachloride, and wherein the solution obtained is treated by ammonium chloride or a metallic chloride, in a basic milieu, to precipitate an insoluble vanadate.