Ammonia scrubbing

Claim 2

A process for reducing the concentration of ammonia in the effluent from the combustion of a carbonaceous fuel, the process comprising introducing a non-nitrogenous treatment agent which comprises a paraffinic, olefinic, aromatic oxygenated hydrocarbon into the effluent at a ratio of non-nitrogenous treatment agent to effluent ammonia of about 2:1 to about 200:1 to combine with ammonia present in the effluent, wherein the effluent temperature is about 1350° F. to about 2000° F. and further wherein said non-nitrogenous treatment agent is introduced under conditions effective to perform ammonia scrubbing.

Claim 3

The process of claim 1 wherein said non-nitrogenous treatment agent is introduced into the effluent to provide a vaporized volume ratio of non-nitrogenous treatment agent to the effluent of about 0.000002:1 to about 0.0005:1.

Claim 4

The process of claim 1 wherein said non-nitrogenous treatment agent is present in a solution, mixture, dispersion or emulsion.

Claim 5

The process of claim 3 wherein the solvent in said solution, mixture, dispersion or emulsion comprises water.

Claim 6

The process of claim 4 wherein said non-nitrogenous treatment agent is present in said solution, mixture, dispersion or emulsion at a concentration of about 1% to about 50% by weight.

Claim 7

The process of claim 1 wherein said conditions effective to perform ammonia scrubbing comprise introducing said non-nitrogenous treatment agent into the effluent to react with ammonia present in the effluent wherein the effluent temperature at said introduction is such that the resulting non-nitrogenous treatment agent/ammonia combination is operating further to the right on its nitrogen oxides reduction versus effluent temperatuee curve than the effluent ammonia was operating on its nitrogen oxides reduction versus effluent temperature curve.

Claim 8

The process of claim 1 wherein said oxygenated hydrocarbon is selected from the group consisting of alcohols, sugars, ketones, furfural and furfural derivatives, organic acids and salts thereof, esters, ethers and aldehydes.

Claim 9

The process of claim 7 wherein said oxygenated hydrocarbon is selected from the group consisting of ethylene glycol, methanol, molasses, sugar, acetone, methylethyl ketone, glycerol and fish oil, and mixtures thereof.

Claim 10

The process of claim 8 wherein said hydrocarbon comprises a mixture of ethylene glycol and sugar.

Claim 11

A process for reducing the concentration of ammonia in the effluent from the combustion of a carbonaceous fuel, the process comprising introducing an aqueous solution which comprises about 1% to about 50% of a non-nitrogenous treatment agent comprising a paraffinic, olefinic, aromatic or oxygenated hydrocarbon into the effluent to react with ammonia present in the effluent, wherein said non-nitrogenous treatment agent is introduced at an effluent temperature of about 1350° F. to about 2000° F. and a ratio of non-nitrogenous treatment agent to effluent ammonia of about 2:1 to about 200:1.

Claim 12

A process for reducing the concentration of ammonia in the effluent from the combustion of a carbonaceous fuel, the process comprising introducing an aqueous solution which comprises about 1% to about 50% of a non-nitrogenous treatment agent comprising a paraffinic, olefinic, aromatic or oxygenated hydrocarbon into the effluent to react with ammonia present in the effluent, wherein said non-nitrogenous treatment agent is introduced at an effluent temperature of about 1350° F. to about 2000° F. and a ratio of non-nitrogenous treatment agent to effluent ammonia of about 2:1 to about 200:1.

Claim 13

The process of claim 10 wherein the introduction of said non-nitrogenous treatment agent into the effluent to react with ammonia present in the effluent is under conditions such that the resulting non-nitrogenous treatment agent/ammonia combination is operating further to the right on its nitrogen oxides reduction versus effluent temperature curve than the effluent ammonia was operating on its nitrogen oxides reduction versus effluent temperature curve.

Claim 14

The process of claim 11 wherein the effluent temperature is about 1350° F. to about 1800° F.

Claim 15

The process of claim 10 wherein said oxygenated hydrocarbon is selected from the group consisting of alcohols, sugars, ketones, furfural and furfural derivatives, organic acids and salts thereof, esters, ethers and aldehydes.

Claim 16

The process of claim 13 wherein said oxygenated hydrocarbon is selected from the group consisting of ethylene glycol, methanol, molasses, sugar, acetone, methylethyl ketone, glycerol and fish oil, and mixtures thereof.

Claim 17

The process of claim 14 wherein said hydrocarbon comprises a mixture of ethylene glycol and sugar.

Claim 18

A process for reducing the concentration of ammonia in the effluent from the combustion of a carbonaceous fuel while concomitantly reducing the concentratinn of nitrogen oxides in the effluent, the process comprising: a. introducing a nitrogenous treatment agent into the effluent at a first nitrogenous treatment agent temperature zone under conditions effective to reduce the concentration of nitrogen oxides in the effluent; and b. introducing a non-nitrogenous treatment agent comprising a paraffinic, olefinic, aromatic or oxygenated hydrocarbon into the effluent at a temperature zone downstream from said first nitrogenous treatment agent temperature zone wherein the temperature at said downstream temperature zone is about 1350° F. to about 1800° F. to combine with ammonia present in the effluent after introduction of said nitrogenous treatment agent at a weight ratio of non-nitrogenoua treatment agent to effluent ammonia of about 2:1 to about 200:1, wherein said non-nitrogenous treatment agent is introduced under conditions effective to perform ammonia scrubbing.

Claim 19

A process for reducing the concentration of ammonia in the effluent from the combustion of a carbonaceous fuel while concomitantly reducing the concentratinn of nitrogen oxides in the effluent, the process comprising: a. introducing a nitrogenous treatment agent into the effluent at a first nitrogenous treatment agent temperature zone under conditions effective to reduce the concentration of nitrogen oxides in the effluent; and b. introducing a non-nitrogenous treatment agent comprising a paraffinic, olefinic, aromatic or oxygenated hydrocarbon into the effluent at a temperature zone downstream from said first nitrogenous treatment agent temperature zone wherein the temperature at said downstream temperature zone is about 1350° F. to about 1800° F. to combine with ammonia present in the effluent after introduction of said nitrogenous treatment agent at a weight ratio of non-nitrogenoua treatment agent to effluent ammonia of about 2:1 to about 200:1, wherein said non-nitrogenous treatment agent is introduced under conditions effective to perform ammonia scrubbing.

Claim 20

The process of claim 16 wherein said non-nitrogenous treatment agent is introduced into the effluent to provide a weight ratio of non-nitrogenous treatment agent to effluent ammonia of about 2:1 to about 200:1.

Claim 21

The process of claim 16 wherein said non-nitrogenous treatment agent is introduced into the effluent to provide a vaporized volume ratio of non-nitrogenous treatment agent to the effluent of about 0.000002:1 to about 0.0005:1.

Claim 22

The process of claim 16 wherein said non-nitrogenous treatment agent is present in a solution, mixture, dispersion or emulsion.

Claim 23

The process of claim 19 wherein the solvent in said solution, mixture, dispersion or emulsion comprises water.

Claim 24

The process of claim 20 wherein said non-nitrogenous treatment agent is present in said solttion, mixture, dispersion or emulsion at a concentration of about 1% to about 50% by weight.

Claim 25

The process of claim 16 wherein said conditions effective to perform ammonia scrubbing comprise introducing said non-nitrogenous treatment agent into the effluent to react with ammonia present in the effluent wherein the effluent temperature at said introduction is such that the resulting non-nitrogenous treatment agent/ammonia combination is operating further to the right on its nitrogen oxides reduction versus effluent temperature curve than the effluent ammonia was operating on its nitrogen oxides reduction versus effluent temperature curve.

Claim 26

The process of claim 16 wherein said oxygenated hydrocarbon is selected from the group consisting of alcohols, sugars, ketones, furfural and furfural derivatives, organic acids and salts thereof, esters, ethers and aldehydes.

Claim 27

The process of claim 23 wherein said oxygenated hydrocarbon is selected from the group consisting of ethylene glycol, methanol, molasses, sugar, acetone, methylethyl ketone, glycerol and fish oil, and mixtures thereof.

Claim 28

The process of claim 24 wherein said hydrocarbon comprises a mixture of ethylene glycol and sugar.