Process for producing aqueous solution of calcium nitrite

Claim 2

In a process for producing an aqueous solution of calcium nitrite having high purity and high concentration by contacting a nitrogen oxides containing gas with an aqueous slurry of calcium hydroxide, the improvement wherein a gas having a temperature of 170°-180° C. and having a nitrogen oxide concentration of 5 to 10 vol.% and a molar ratio of NO/NO 2 of 1.2 to 1.5 is contacted with the aqueous slurry having 20 to 40 wt.% of a calcium hydroxide content at 40° to 70° C. until the calcium hydroxide content is reduced to a range of 3 to 6 wt.% as a first stage; and the unabsorbed and unreacted gas is separated and the gas is oxidized at 60°-80° C. to form a gas having a nitrogen oxides concentration of 1 to 3 vol.% and a molar ratio NO/NO 2 of 1.2 to 1.5 and the resulting gas is contacted with the aqueous slurry separated from the first stage and having 3 to 6 wt.% of a calcium hydroxide content and containing calcium nitrite, at 40° to 70° C. to reduce the calcium hydroxide content to less than 3 wt.% as a second stage and filtering the resulting solution.

Claim 3

A process for producing an aqueous solution of calcium nitrite according to claim 1 wherein the nitrogen oxides containing gas used in the first stage is obtained by oxidizing ammonia.

Claim 4

A process for producing an aqueous solution of calcium nitrite according to any of claims 1 or 2 wherein the calcium hydroxide content of the aqueous solution obtained in the second stage is less than 1 wt.%.

Claim 5

A process for producing an aqueous solution of calcium nitrite according to any of claims 1 or 2 wherein calcium hydroxide as the starting material which is used in the first stage is a slaked lime.

Claim 6

A continuous process for producing an aqueous solution of calcium nitrite having high purity and high concentration by contacting a nitrogen oxides containing gas with an aqueous slurry of calcium hydroxide, which comprises (a) feeding continuously an aqueous slurry having 20 to 40 wt.% of slaked lime content and a nitrogen oxide containing gas having a temperature of 170°-180° C. and having a nitrogen oxides concentration of 5 to 10 vol.% and a molar ratio of NO/NO 2 of 1.2 to 1.5 obtained by oxidizing ammonia into a first reaction zone to contact them under conditions of temperature of 40° to 70° C. until the calcium hydroxide content is reduced to a range of 3 to 6 wt.%; (b) discharging continuously the unabsorbed gas and the reaction mixture from the first reaction zone and separating and feeding continuously the reaction mixture to a second reaction zone and feeding continuously the unabsorbed gas into an oxidizing device; (c) oxidizing the unabsorbed gas in the oxidizing device at 60°-80° C. to control it to a nitrogen oxides concentration of 1 to 3 vol.% and a molar ratio of NO/NO 2 of 1.2 to 1.5, and feeding the resulting gas into the second reaction zone; (d) contacting continuously the resulting gas with the aqueous slurry separated from the first reaction zone and having 3 to 6 wt.% of a calcium hydroxide content under conditions of temperature of 40° to 70° C. to reduce the calcium hydroxide content in the second reaction zone to less than 3 wt.%; and (e) discharging continuously the unabsorbed gas and the reaction mixture from the second reaction zone while separating and feeding continuously the reaction mixture to a filter to separate the remaining calcium hydroxide.

Claim 7

A continuous process for producing an aqueous solution of calcium nitrite having high purity and high concentration by contacting a nitrogen oxides containing gas with an aqueous slurry of calcium hydroxide, which comprises (a) feeding continuously an aqueous slurry having 20 to 40 wt.% of slaked lime content and a nitrogen oxide containing gas having a temperature of 170°-180° C. and having a nitrogen oxides concentration of 5 to 10 vol.% and a molar ratio of NO/NO 2 of 1.2 to 1.5 obtained by oxidizing ammonia into a first reaction zone to contact them under conditions of temperature of 40° to 70° C. until the calcium hydroxide content is reduced to a range of 3 to 6 wt.%; (b) discharging continuously the unabsorbed gas and the reaction mixture from the first reaction zone and separating and feeding continuously the reaction mixture to a second reaction zone and feeding continuously the unabsorbed gas into an oxidizing device; (c) oxidizing the unabsorbed gas in the oxidizing device at 60°-80° C. to control it to a nitrogen oxides concentration of 1 to 3 vol.% and a molar ratio of NO/NO 2 of 1.2 to 1.5, and feeding the resulting gas into the second reaction zone; (d) contacting continuously the resulting gas with the aqueous slurry separated from the first reaction zone and having 3 to 6 wt.% of a calcium hydroxide content under conditions of temperature of 40° to 70° C. to reduce the calcium hydroxide content in the second reaction zone to less than 3 wt.%; and (e) discharging continuously the unabsorbed gas and the reaction mixture from the second reaction zone while separating and feeding continuously the reaction mixture to a filter to separate the remaining calcium hydroxide.

Claim 8

A process for producing an aqueous solution of calcium nitrite according to claim 5 wherein the calcium hydroxide content in the reaction mixture obtained in the second reaction zone is less than 1 wt.%.