Regeneration of alkali metal sulfides from alkali metal hydrosulfides

Claim 2

A process for the conversion of an alkali metal hydrosulfide to an alkali metal sulfide, which comprises contacting alkali metal hydrosulfide, produced during the hydroconversion of a heavy carbonaceous feedstock by contact of said feedstock with an alkali metal sulfide, with water and carbon dioxide at a temperature and pressure sufficient to convert about 50% of said alkali metal hydrosulfide to an alkali metal carbonate, and heating a mixture of said alkali metal carbonate, unreacted alkali metal hydrosulfide, and coke to an elevated temperature sufficient to cause reaction of the alkali metal hydrosulfide with the alkali metal carbonate whereby an alkali metal sulfide is formed.

Claim 3

The process of claim 1 wherein the mixture of said alkali metal carbonate, unreacted alkali metal hydrosulfide, and coke is heated to a temperature of from about 1200°-1800° F.

Claim 4

The process of claim 1 wherein the alkali metal of said alkali metal hydrosulfide, said alkali metal carbonate, and said alkali metal sulfide comprises an alkali metal selected from the group consisting of sodium, lithium, potassium, rubidium, cesium, and mixtures thereof.

Claim 5

The process of claim 1 wherein said alkali metal of said alkali metal hydrosulfide, said alkali metal carbonate, and said alkali metal sulfide comprises potassium.

Claim 6

The process of claim 1 wherein said water is in the form of steam and further wherein said temperature and pressure sufficient to convert about 50% of said alkali metal hydrosulfide to said alkali metal carbonate comprises a temperature of from about 800°-1400° F. and atmospheric pressure.

Claim 7

The process of claim 1 wherein said alkali metal hydrosulfide is dissolved in water to form an aqueous solution, and further wherein said temperature and pressure sufficient to cause conversion of about 50% of said alkali metal hydrosulfide to said alkali metal carbonate comprises a temperature of from about 100°-400° F. and a pressure of from about 0-1000 psig.

Claim 8

The process of claim 1 wherein additional coke is added to the mixture of said alkali metal carbonate, alkali metal hydrosulfide, and coke prior to heating.

Claim 9

The process of claim 1 wherein said alkali metal sulfide which has been regenerated from said alkali metal hydrosulfide is recycled to a hydroconversion reactor for use as a hydroconversion reagent.

Claim 10

A process for the hydroconversion of a heavy carbonaceous feedstock by contact of said feedstock with an alkali metal sulfide and regeneration of an alkali metal sulfide from an alkali metal hydrosulfide produced as a result of said hydroconversion which comprises: contacting a heavy carbonaceous feedstock with an alkali metal sulfide in a reaction zone under conditions sufficient to effect hydroconversion of said feedstock; removing spent solids from said reaction zone to a carbonation chamber, said solids comprising primarily an alkali metal hydrosulfide, coke, metals and unconverted alkali metal sulfide; contacting said spent solids with water and carbon dioxide at a temperature and pressure sufficient to convert about 50% of said alkali metal hydrosulfide to an alkali metal carbonate; heating a mixture of said alkali metal carbonate, unreacted alkali metal hydrosulfide, and coke produced during said hydroconversion to an elevated temperature sufficient to cause reaction of the alkali metal hydrosulfide with the alkali metal carbonate whereby an alkali metal sulfide is formed.

Claim 11

A process for the hydroconversion of a heavy carbonaceous feedstock by contact of said feedstock with an alkali metal sulfide and regeneration of an alkali metal sulfide from an alkali metal hydrosulfide produced as a result of said hydroconversion which comprises: contacting a heavy carbonaceous feedstock with an alkali metal sulfide in a reaction zone under conditions sufficient to effect hydroconversion of said feedstock; removing spent solids from said reaction zone to a carbonation chamber, said solids comprising primarily an alkali metal hydrosulfide, coke, metals and unconverted alkali metal sulfide; contacting said spent solids with water and carbon dioxide at a temperature and pressure sufficient to convert about 50% of said alkali metal hydrosulfide to an alkali metal carbonate; heating a mixture of said alkali metal carbonate, unreacted alkali metal hydrosulfide, and coke produced during said hydroconversion to an elevated temperature sufficient to cause reaction of the alkali metal hydrosulfide with the alkali metal carbonate whereby an alkali metal sulfide is formed.

Claim 12

The process of claim 9 wherein the mixture of said alkali metal carbonate, unreacted alkali metal hydrosulfide, and coke is heated to a temperature of from about 1200°-1800° F.

Claim 13

The process of claim 9 wherein the alkali metal of said alkali metal hydrosulfide, said alkali metal carbonate, and said alkali metal sulfide comprises an alkali metal selected from the group consisting of sodium, lithium, potassium, rubidium, cesium, and mixtures thereof.

Claim 14

The process of claim 9 wherein said alkali metal of said alkali metal hydrosulfide, said alkali metal carbonate, and said alkali metal sulfide comprises potassium.

Claim 15

The process of claim 9 wherein said water is in the form of steam, and further wherein said temperature and pressure sufficient to convert about 50% of said alkali metal hydrosulfide to said alkali metal carbonate comprises a temperature of from about 800°-1400° F. and atmospheric pressure.

Claim 16

The process of claim 9 wherein said spent solids are dissolved in water to form an aqueous solution, and further wherein said temperature and pressure sufficient to convert about 50% of said alkali metal hydrosulfide to said alkali metal carbonate comprises a temperature of from about 100°-400° F. and a pressure of from 0-1000 psig.

Claim 17

The process of claim 13 wherein the level of impurity metals present in the regenerated alkali metal sulfide is reduced by removing at least a portion of said spent solids from said reaction zone, dissolving said solids in water to form a solution, and filtering said solution to remove metals.

Claim 18

The process of claim 14 wherein said aqueous solution is filtered to remove metals therefrom.

Claim 19

The process of claim 9 wherein said alkali metal sulfide which has been regenerated from said alkali metal hydrosulfide is recycled to said reaction zone for further hydroconversion of said heavy carbonaceous feedstock.

Claim 20

The process of claim 9 wherein additional coke is added to the mixture of said alkali metal carbonate, said alkali metal hydrosulfide, and coke prior to heating.

Claim 21

The process of claim 9 wherein the level of metals in said spent solids is reduced prior to further processing.