Desulfurization of hot reducing gas

Claim 2

In a process for desulfurizing hot reducing gas by contacting said gas with a desulfurizing agent, then regenerating the spent desulfurizing agent, and then reusing the regenerated desulfurizing agent for desulfurizing hot reducing gas, the improvement wherein the desulfurizing agent comprises a bed of sintered, porous pellets comprising manganese oxide and non-reactive metal oxide comprising finely divided aluminum oxide, wherein the spent desulfurizing agent is regenerated by heating said bed in the presence of an oxidizing gaseous atmosphere, wherein the temperature of the bed is maintained at a temperature between about 500° C. and about 1300° C. in both the desulfurization and the regeneration steps wherein said pellets comprise more than about 50% by weight manganese oxide and less than about 50% by weight of aluminum oxide and wherein said pellets were sintered by heating to a temperature between about 1000° C. and about 1400° C.

Claim 3

Process as in claim 1 wherein said pellets have an average diameter of between about 5 and about 15 mm.

Claim 4

Process as in claim 1 wherein said pellets have a compression strength of at least about 10 pounds and a porosity of at least about 10% of the volume of the pellet.

Claim 5

Process as in claim 1 wherein said hot reducing gas comprises hydrogen, carbon monoxide or mixtures thereof.

Claim 6

Process as in claim 4 wherein said hot reducing gas comprises hydrogen, water vapor, hydrogen sulfide, carbon monoxide, carbon dioxide, carbon oxysulfide and sulfur vapor.

Claim 7

Process as in claim 1 wherein said oxidizing gaseous atmosphere comprises oxygen, carbon dioxide, water vapor or mixtures thereof and a non-reactive carrier gas.

Claim 8

Process as in claim 6 wherein said carrier gas is nitrogen, sulfur dioxide, an inert gas or mixtures thereof.

Claim 9

Process as in claim 1 wherein said bed of pellets is a fixed or moving packed bed.

Claim 10

Process as in claim 1 wherein said packed bed has a diameter of between about 1 and about 20 feet and a height of between about 1 and about 30 feet.

Claim 11

Process as in claim 1 wherein said hot reducing gas comprises about 70% by volume hydrogen, about 20 to 25% by volume carbon monoxide, and between about 0.5 and about 4% hydrogen sulfide.

Claim 12

Process as in claim 1 wherein said hot reducing gas is at a temperature about 700° and about 1000° C.

Claim 13

Process as in claim 1 wherein said hot reducing gas at the end of the desulfurization process has a sulfur content down to the equilibrium value of the equilibrated gas with manganese oxide.

Claim 14

Process as in claim 12 wherein the hydrogen sulfide content of said hot reducing gas at the end of the desulfurization process is reduced to less than about 200 ppm.

Claim 15

Process as in claim 1 wherein said desulfurizing agent is regenerated and reused in the process of claim 1 at least six times.

Claim 16

A process for desulfurizing hot reducing gas containing hydrogen sulfide by intimately contacting the gas with a desulfurizing agent comprising a fixed bed of pellets, said bed having a temperature between about 500° C. and about 1300° C. comprising a porous, sintered reaction product of an intimate mixture of finely divided manganese oxide, and a finely divided, non-reactive aluminum oxide wherein said pellts comprise more than about 50% by weight manganese oide and less than about 50% by weight of aluminum oxide and wherein said pellets were sintered by heating to a temperature between about 1000° C. and about 1400° C.

Claim 17

A process for desulfurizing hot reducing gas containing hydrogen sulfide by intimately contacting the gas with a desulfurizing agent comprising a fixed bed of pellets, said bed having a temperature between about 500° C. and about 1300° C. comprising a porous, sintered reaction product of an intimate mixture of finely divided manganese oxide, and a finely divided, non-reactive aluminum oxide wherein said pellts comprise more than about 50% by weight manganese oide and less than about 50% by weight of aluminum oxide and wherein said pellets were sintered by heating to a temperature between about 1000° C. and about 1400° C.

Claim 18

Process as in claim 15 wherein the pellets have sufficient strength to be used in the fixed bed of this process without serious deterioration and wherein the pellets have sufficient porosity to maintain good reactivity in the desulfurization and regeneration steps.

Claim 19

Process as in claim 15 wherein said pellets have an average diameter of between 7 and 9 mm, wherein the said manganese oxide is MnO, wherein said oxidizing atmosphere comprises oxygen and a non-reactive carrier gas, and wherein said hot reducing gas comprises hydrogen, carbon monoxide, or mixtures thereof.

Claim 20

Process as in claim 17 wherein said fixed bed of pellets has an average diameter of between about 1 and about 20 feet and a height of between about 20 and about 30 feet and wherein said hot reducing gas comprises about 70% by volume hydrogen, between about 20 and about 25 percent by volume carbon monoxide, and between about 0.5 and about 4% by volume hydrogen sulfide.

Claim 21

Process as in claim 18 wherein said hydrogen sulfide in said hot reducing gas at the end of the desulfurization process has been reduced to an amount less than about 200 ppm and wherein said desulfurizing agent is regenerated and reused for desulfurizing hot reducing gas at least six times.

Claim 22

Process as in claim 15 wherein said hot reducing gas contains about 3% hydrogen sulfide.

Claim 23

Process as in claim 15 wherein said hot reducing gas comprises hydrogen, carbon monoxide and carbon dioxide, water vapor, hydrogen sulfide and minor amounts of methane and nitrogen.

Claim 24

A process for desulfurizing hot reducing gas containing hydrogen sulfide by (1) intimately contacting the gas with a desulfurizing agent comprising a fixed bed of pellets, said bed having a temperature between about 500° C. and about 1300° C. and said pellets comprising a sintered, porous reaction product of an intimate mixture of finely divided manganese oxide, and a nonreactive, finely divided aluminum oxide, which pellets were sintered by heating to a temperature of between about 1000° C. and about 1400° C., and which pellets are comprised of more than about 50% by weight manganese oxide and less than about 50% by weight of aluminum oxide, then (2) regenerating the spent desulphurizing agent by heating the bed in the presence of a gaseous oxidizing atmosphere of such composition and under such conditions to maintain the temperature of the bed between about 500° C. and 1300° C. and then reusing the regenerated desulfurizing agent under the above-mentioned conditions for desulfurizing hot reducing gas.

Claim 25

A process for desulfurizing hot reducing gas containing hydrogen sulfide by (1) intimately contacting the gas with a desulfurizing agent comprising a fixed bed of pellets, said bed having a temperature between about 500° C. and about 1300° C. and said pellets comprising a sintered, porous reaction product of an intimate mixture of finely divided manganese oxide, and a nonreactive, finely divided aluminum oxide, which pellets were sintered by heating to a temperature of between about 1000° C. and about 1400° C., and which pellets are comprised of more than about 50% by weight manganese oxide and less than about 50% by weight of aluminum oxide, then (2) regenerating the spent desulphurizing agent by heating the bed in the presence of a gaseous oxidizing atmosphere of such composition and under such conditions to maintain the temperature of the bed between about 500° C. and 1300° C. and then reusing the regenerated desulfurizing agent under the above-mentioned conditions for desulfurizing hot reducing gas.