Recovery of ammonia from aqueous streams

Claim 3

The method of claim 1 which comprises the step of contacting the aqueous stream with the ammonia-rich product vapor before mixing the aqueous stream with the lime slurry solution.

Claim 4

The method of claim 1 wherein the aqueous stream contains an ammonium compound selected from the group consisting of ammonium fluoride, ammonium sulfate and ammonium carbonate.

Claim 5

The method of claim 1 wherein the lime slurry is added in at least about the stoichiometric proportion for reacting with the ammonium compound in the aqueous stream.

Claim 6

The method of claim 1 wherein the stripping zone is a packed column.

Claim 7

The method of claim 1 comprising the step of equilibrating the ammonia-rich product vapor with the heated liquid mixture in the mixing zone.

Claim 8

The method of claim 1 comprising the step of condensing ammonia-rich product vapor withdrawn from the mixing zone.

Claim 11

The method of claim 8 wherein the aqueous stream contains an ammonium compound selected from the group consisting of ammonium fluoride, ammonium sulfate, and ammonium carbonate.

Claim 12

The method of claim 8 wherein the lime slurry is added in at least about the stoichiometric proportion for reacting with the ammonium compound in the aqueous stream.

Claim 13

The method of claim 8 wherein the stripping zone is a packed column.

Claim 14

The method of claim 8 wherein the liquid mixture is heated to a temperature of at least about 95° C.

Claim 15

The method of claim 8 which comprises the step of equilibrating the ammonia-rich product vapor with the heated liquid mixture.

Claim 16

A continuous method for recovering ammonia from a continuously circulating aqueous stream containing an ammonium compound capable of reacting with lime to form free ammonia in solution, which consists essentially of the steps of: (a) establishing a circulating liquid mixture heated to a temperature of at least about 95° C. in a mixing zone, the circulating mixture comprising an ammonium compound capable of reacting with lime to form free ammonia in solution and lime in a proportion sufficient for reacting with at least a portion of said ammonium compound and continuing the circulating of the mixture to maintain solids thereof in suspension; (b) continuously introducing into the mixing zone a lime slurry stream and an aqueous stream containing said ammonium compound; (c) continuously withdrawing a stream of heated liquid mixture from the mixing zone and continuously introducing the stream into a steam stripping zone to produce vapor containing ammonia and steam and a waste liquid stripped of ammonia; (d) continuously withdrawing a recycle stream of heated liquid mixture from the mixing zone, contacting the recycle stream with steam and the vapor from the stripping zone, and introducing the resulting liquid and vapor into the mixing zone, whereby the liquid mixture in the mixing zone is heated and an ammonia-rich product vapor is produced; and (e) continuously withdrawing ammonia-rich product vapor from the mixing zone.

Claim 17

A continuous method for recovering ammonia from a continuously circulating aqueous stream containing an ammonium compound capable of reacting with lime to form free ammonia in solution, which consists essentially of the steps of: (a) establishing a circulating liquid mixture heated to a temperature of at least about 95° C. in a mixing zone, the circulating mixture comprising an ammonium compound capable of reacting with lime to form free ammonia in solution and lime in a proportion sufficient for reacting with at least a portion of said ammonium compound and continuing the circulating of the mixture to maintain solids thereof in suspension; (b) continuously introducing into the mixing zone a lime slurry stream and an aqueous stream containing said ammonium compound; (c) continuously withdrawing a stream of heated liquid mixture from the mixing zone and continuously introducing the stream into a steam stripping zone to produce vapor containing ammonia and steam and a waste liquid stripped of ammonia; (d) continuously withdrawing a recycle stream of heated liquid mixture from the mixing zone, contacting the recycle stream with steam and the vapor from the stripping zone, and introducing the resulting liquid and vapor into the mixing zone, whereby the liquid mixture in the mixing zone is heated and an ammonia-rich product vapor is produced; and (e) continuously withdrawing ammonia-rich product vapor from the mixing zone.

Claim 18

The method of claim 14 wherein the aqueous stream contains an ammonium compound selected from the group consisting of ammonium fluoride, ammonium sulfate, and ammonium carbonate.

Claim 19

The method of claim 14 wherein the lime slurry is introduced in at least about the stoichiometric proportion for reacting with the ammonium compound in the aqueous stream.

Claim 20

The method of claim 14 wherein the stripping zone is a packed column.

Claim 21

The method of claim 14 which comprises the step of equilibrating the ammonia-rich product vapor with the heated liquid mixture.

Claim 22

The method of claim 8 or 1 or 14 wherein during the step of contacting the mixture of step (a) with the vapor stream and steam, the mixture and vapor stream are intimately mixed for a time sufficient for establishing a thermal equilibrium between the mixture and vapor stream and equilibrium between the ammonia in the vapor stream and ammonia in the mixture.

Claim 23

The methd of claim 8 or 1 or 14 wherein the contacting of the mixture with the vapor stream and steam heats the liquid mixture to a temperature sufficient for preventing scaling in the stripping zone.

Claim 24

The method of claim 8 or 1 or 14 wherein the contacting of the mixture with the vapor stream and steam heats the liquid mixture to a temperature for providing upon introducing the liquid mixture to the stripping zone, a sufficiently small temperature differential between the liquid mixture and the stripping zone for preventing scaling within the stripping zone.