Process for reduction of the content of SO2 and/or NOx in flue gas

Claim 2

Process for reduction of the content of NO and NO 2 in flue gas containing also substantial quantities of H 2 O vapor comprising mixing the flue gas with NH 3 and irradiating the mixture with ultraviolet radiation of wavelength at least as great as about 190 nm and containing at least one component of wavelength in the range from about 190 to about 220 nm, said radiation being substantially wholly free of any component with a wavelength below about 190 nm, and said process taking place in the absence of a solid state catalyst.

Claim 3

Process as claimed in claim 1 wherein said radiation is provided from a high pressure short arc mercury-xenon lamp providing a continuous spectrum output from 190 nm to above 300 nm.

Claim 4

Process as claimed in claim 1 wherein the gaseous mixture after irradiation is passed direct to the atmosphere.

Claim 5

Process as claimed in claim 1 wherein the gaseous mixture is subjected to a total quantity of radiant energy flux of radiation in said wavelength range of from about 10 18 to 10 19 photon/cm 2 of the irradiated area.

Claim 6

Process as claimed in claim 1 wherein said mixture contains about 5×10 -6 to about 5×10 -3 mol/l NH 3 .

Claim 7

Process as claimed in claim 5 wherein said NH 3 content is about 1×10 -5 to about 1×10 -3 mol/l.

Claim 8

Process as claimed in claim 6 wherein said content is about 1×10 -5 to about 2×10 -5 mol/l.

Claim 9

Process as claimed in claim 1 wherein the NH 3 is added to the flue gas when the latter is at a temperature of up to about 400° C.

Claim 10

Process as claimed in claim 8 wherein said temperature is about 150° to about 250° C.

Claim 11

Process as claimed in claim 1 in which the gas is a flue gas containing at least about 1×10 -6 mol/l SO 2 .

Claim 12

Process as claimed in claim 10 in which the gas contains about 1×10 -6 to about 1×10 -4 mol/l SO 2 .

Claim 13

Process as claimed in claim 10 in which the gas contains about 1100 to 1600 ppm SO 2 .

Claim 14

Process for reacting a flue gas containing at least about 1×10 -6 mol/l SO 2 to convert said SO 2 to an oxidized acidic species, in the absence of a solid state catalyst, said flue gas containing also substantial quantities of H 2 O vapor and O 2 , comprising irradiating the gas with ultraviolet radiation nm.

Claim 15

Process for reacting a flue gas containing at least about 1×10 -6 mol/l SO 2 to convert said SO 2 to an oxidized acidic species, in the absence of a solid state catalyst, said flue gas containing also substantial quantities of H 2 O vapor and O 2 , comprising irradiating the gas with ultraviolet radiation nm.

Claim 16

Process as claimed in claim 13 wherein the content of SO 2 in the gas is about 1×10 -6 to about 1×10 -4 mol/l.

Claim 17

Process as claimed in claim 13 wherein said radiation is from a low pressure mercury arc lamp providing strong emission lines at 184.9 and 253.7 nm.

Claim 18

Process as claimed in claim 13 wherein said gaseous mixture is subjected to a total quantity of radiant energy flux of radiation in said wavelength range of from about 5×10 18 to about 5×10 19 photon/cm 2 of the irradiated area.

Claim 19

Process as claimed in claim 13 including contacting the irradiated mixture with an alkaline-reacting medium to absorb acid species.

Claim 20

Process as claimed in claim 13 including contacting the irradiated mixture with gaseous ammonia to absorb acid species.

Claim 21

Process as claimed in claim 1 or 13 wherein said flue gas contains 1×10 -4 to 1×10 -2 mol/l H 2 O vapor and 1×10 -6 to 1×10 -2 mol/l O 2 .

Claim 22

Process as claimed in claim 1 or 13 wherein said flue gas contains no more than 1×10 -8 mol/l hydrocarbons.

Claim 23

Process as claimed in claim 13 wherein the radiation contains a component in the range about 170 to about 190 nm.

Claim 24

Process for reduction of the content of NO and NO 2 in flue gas containing also substantial quantities of H 2 O vapor, comprising mixing the flue gas with NH 3 blowing the mixture containing NH 3 through a fan to an irradiation site, and irradiating the mixture at the irradiation site with ultraviolet radiation of wavelength at least as great as about 190 nm and containing at least one component of wavelength in the range from about 190 to about 220 nm, said radiation being substantially wholly free of any component with a wavelength below about 190 nm, and said process taking place in the absence of a solid state catalyst.

Claim 25

Process for reduction of the content of NO and NO 2 in flue gas containing also substantial quantities of H 2 O vapor, comprising mixing the flue gas with NH 3 blowing the mixture containing NH 3 through a fan to an irradiation site, and irradiating the mixture at the irradiation site with ultraviolet radiation of wavelength at least as great as about 190 nm and containing at least one component of wavelength in the range from about 190 to about 220 nm, said radiation being substantially wholly free of any component with a wavelength below about 190 nm, and said process taking place in the absence of a solid state catalyst.