Processes for removing nitrogen oxides, sulfur oxides and hydrogen sulfide from gas streams

Claim 2

A process for the removal of nitrogen oxides and/or sulfur oxides from a gas containing nitrogen oxides and /or sulfur oxides which comprises contacting said gas with a sorbent, said sorbent comprising: (a) a gamma alumina substrate having a surface area between 100 m 2 /g and 500 m 2 /g and a pore volume between 0.4 and 0.8 cc/g, said gamma alumina substrate having a bimodal pore size distribution comprising micropores and macropores, said micropores having an average pore diameter d 1 in the range of between 30 and 400 Angstroms and said macropores having an average pore diameter d 2 in the range of between 80 and 3000 Angstroms, (b) an alkali metal component, said substrate impregnated with said alkali metal component and the amount of said alkali metal component being between 50 and 400 μg per m 2 of said substrate.

Claim 3

A process for the continuous removal of nitrogen oxides and sulfur oxides from a gas containing them with a sorbent and for regenerating said sorbent comprising: (a) contacting said gas at a temperature of about 85° C. to about 200° C. with said sorbent comprising: (i) a gamma alumina substrate having a surface area between 100 m 2 /g and 500 m 2 /g and a pore volume between 0.4 and 0.8 cc/g, said gamma alumina substrate having a bimodal pore size distribution comprising micropores and macropores, said micropores having an average pore diameter d 1 in the range between 30 and 400 Angstroms and said macropores having an average pore diameter d 2 in the range of between 80 and 3000 Angstroms, (ii) an alkali metal component, said substrate impregnated with said alkali metal component and the amount of said alkali metal component being between 50 and 400 μg per m 2 of said substrate, to adsorb said nitrogen oxides and sulfur oxides on said sorbent and remove said nitrogen oxides and sulfur oxides from said gas; (b) subsequently, withdrawing said nitrogen oxides adsorbed on said sorbent in the form of nitrogen oxides carried away in a hot gas stream; and (c) subsequently, withdrawing said sulfur oxides adsorbed on said sorbent in the form of a stream of elemental sulfur; (d) subsequently, cooling said sorbent; and (e) repeating steps (a), (b), (c) and (d).

Claim 4

A process for the continuous removal of nitrogen oxides and sulfur oxides from a gas containing them with a sorbent and for regenerating said sorbent comprising: (a) contacting said gas at a temperature of about 85° C. to about 200° C. with said sorbent comprising: (i) a gamma alumina substrate having a surface area between 100 m 2 /g and 500 m 2 /g and a pore volume between 0.4 and 0.8 cc/g, said gamma alumina substrate having a bimodal pore size distribution comprising micropores and macropores, said micropores having an average pore diameter d 1 in the range between 30 and 400 Angstroms and said macropores having an average pore diameter d 2 in the range of between 80 and 3000 Angstroms, (ii) an alkali metal component, said substrate impregnated with said alkali metal component and the amount of said alkali metal component being between 50 and 400 μg per m 2 of said substrate, to adsorb said nitrogen oxides and sulfur oxides on said sorbent and remove said nitrogen oxides and sulfur oxides from said gas; (b) subsequently, withdrawing said nitrogen oxides adsorbed on said sorbent in the form of nitrogen oxides carried away in a hot gas stream; and (c) subsequently, withdrawing said sulfur oxides adsorbed on said sorbent in the form of a stream of elemental sulfur; (d) subsequently, cooling said sorbent; and (e) repeating steps (a), (b), (c) and (d).

Claim 5

A process for the continuous removal of nitrogen oxides and sulfur oxides from a gas containing them with a sorbent and for regenerating said sorbent, comprising: (a) contacting said gas at a temperature of about 85° C. to about 200° C. with said sorbent comprising: (i) a gamma alumina substrate having a surface area between 100 m 2 /g and 500 m 2 /g and a pore volume between 0.6 and 0.8 cc/g, and (ii) an alkali metal component, said substrate impregnated with said alkali metal component and the amount of said alkali metal component being between 150 and 250 μg per m 2 of said substrate, to adsorb said nitrogen oxides and said sulfur oxides on said sorbent and remove said nitrogen oxides and said sulfur oxides from said gas; (b) subsequently, withdrawing said nitrogen oxides adsorbed on said sorbent in the form of nitrogen oxides carried away in a hot gas stream; and (c) subsequently, withdrawing said sulfur oxides adsorbed on said sorbent in the form of a stream of elemental sulfur; (d) subsequently, cooling said sorbent; and (e) repeating steps (a), (b), (c) and (d).

Claim 6

A process for the continuous removal of nitrogen oxides and sulfur oxides from a gas containing them with a sorbent and for regenerating said sorbent, comprising: (a) contacting said gas at a temperature of about 85° C. to about 200° C. with said sorbent comprising: (i) a gamma alumina substrate having a surface area between 100 m 2 /g and 500 m 2 /g and a pore volume between 0.6 and 0.8 cc/g, and (ii) an alkali metal component, said substrate impregnated with said alkali metal component and the amount of said alkali metal component being between 150 and 250 μg per m 2 of said substrate, to adsorb said nitrogen oxides and said sulfur oxides on said sorbent and remove said nitrogen oxides and said sulfur oxides from said gas; (b) subsequently, withdrawing said nitrogen oxides adsorbed on said sorbent in the form of nitrogen oxides carried away in a hot gas stream; and (c) subsequently, withdrawing said sulfur oxides adsorbed on said sorbent in the form of a stream of elemental sulfur; (d) subsequently, cooling said sorbent; and (e) repeating steps (a), (b), (c) and (d).

Claim 7

Process according to claim 2 or 3 wherein said gas containing said nitrogen and sulfur oxides is flue gas from a power plant which power plant utilizes a combustion air stream, and wherein said process includes the further step of mixing said hot gas stream carrying said removed nitrogen oxides with said combustion air stream.

Claim 8

Process according to claim 2 or 3 wherein said step (b) comprises the step of contacting said sorbent containing said nitrogen and sulfur oxides with a stream of high temperature air heated to a temperature of about 532° C. and wherein said stream of high temperature air is supplied by an air heater, wherein said step (d) of cooling said sorbent comprises the steps of contacting said sorbent with ambient air to reduce the sorbent temperature to about 120° C. and wherein such contact heats said ambient air and provides a stream of heated ambient air, and wherein said process includes the further step of transporting said stream of heated ambient air to a heater for use in supplying said stream of air heated to about 532° C.

Claim 9

Process according to claim 2 or 3 wherein said step (b) of withdrawing said nitrogen oxide adsorbed on said sorbent comprises the step of contacting said sorbent with a stream of high temperature air heated to about 532° C. to carry said nitrogen oxide away in said hot gas stream.

Claim 10

Process according to claim 2 or 3 wherein said step (c) of withdrawing said sulfur oxide adsorbed on said sorbent comprises the step of contacting said sorbent with a regenerant gas stream which reacts with the sorbed sulfur to produce a sulfur oxides stream and transporting said sulfur oxides stream into a sulfur condenser and mist eliminator to produce said stream of elemental sulfur and a stream of steam.

Claim 11

Process according to claim 2 or 3 wherein said step (d) of cooling said sorbent comprises the step of contacting said sorbent removed of said nitrogen and sulfur oxides with a stream of atmospheric air.