Method of hydrolyzing urea contained in waste water streams

Claim 2

In a process which comprises hydrolyzing urea which is contained in a waste water stream, the improvement which comprises effecting said hydrolysis in a carbon dioxide recovery system wherein (a) carbon dioxide is absorbed into an aqueous solution from a gas mixture, (b) said absorbed carbon dioxide and water vapor are stripped from said aqueous solution, (c) said stripped mixture of carbon dioxide and water vapor is cooled in order to condense a major portion of said water vapor into liquid water, (d) said liquid water is separated from said carbon dioxide, and (e) said liquid water is recycled back to said stripping step (b).

Claim 3

The process of claim 1 wherein the operation of said carbon dioxide recovery system further includes venting to the atmosphere of a portion of said stripped carbon dioxide and water vapor before said cooling step and said waste water stream is added into the carbon dioxide recovery system after said venting step and before said cooling step.

Claim 4

The process of claim 2 wherein said waste water stream contains from about 0.01% to about 20% by weight urea.

Claim 5

The process of claim 3 wherein said carbon dioxide recovery system is operated at a temperature from about 90° C to about 130° C.

Claim 6

The process of claim 4 wherein said aqueous solution in said carbon dioxide recovery system contains potassium carbonate.

Claim 7

The process of claim 5 wherein said waste water stream contains from about 0.05% to about 10% by weight urea.

Claim 8

The process of claim 6 wherein said waste water stream is from a urea production process.

Claim 9

The process of claim 7 wherein said carbon dioxide recovery system is part of an ammonia production process.

Claim 10

In a combined process for producing ammonia and urea comprising the steps of (a) forming a gas mixture comprised of nitrogen, hydrogen and carbon dioxide, (b) removing and recovering a major portion of the carbon dioxide from said gas mixture in a carbon dioxide recovery system wherein (i) a major portion of said carbon dioxide is absorbed into an aqueous solution, and (ii) substantially all of said absorbed carbon dioxide is then stripped from said aqueous solution, (c) utilizing the remaining gas mixture to form ammonia by the reaction of nitrogen with hydrogen, (d) reacting at least a portion of said ammonia with carbon dioxide to form a reaction mixture comprised of urea and water, and (e) recovering a major portion of said urea, leaving a waste water stream containing a minor proportion of urea, wherein the improvement comprises introducing said waste water stream into said carbon dioxide recovery system and therein hydrolyzing substantially all of said urea in the waste water stream.

Claim 11

In a combined process for producing ammonia and urea comprising the steps of (a) forming a gas mixture comprised of nitrogen, hydrogen and carbon dioxide, (b) removing and recovering a major portion of the carbon dioxide from said gas mixture in a carbon dioxide recovery system wherein (i) a major portion of said carbon dioxide is absorbed into an aqueous solution, and (ii) substantially all of said absorbed carbon dioxide is then stripped from said aqueous solution, (c) utilizing the remaining gas mixture to form ammonia by the reaction of nitrogen with hydrogen, (d) reacting at least a portion of said ammonia with carbon dioxide to form a reaction mixture comprised of urea and water, and (e) recovering a major portion of said urea, leaving a waste water stream containing a minor proportion of urea, wherein the improvement comprises introducing said waste water stream into said carbon dioxide recovery system and therein hydrolyzing substantially all of said urea in the waste water stream.

Claim 12

The process of claim 9 wherein said waste water stream contains from about 0.01% to about 20% by weight urea.

Claim 13

The process of claim 9 wherein said carbon dioxide recovery system is operated at a temperature from about 90° C to about 130° C.

Claim 14

The process of claim 9 wherein water vapor is stripped from said aqueous solution with said carbon dioxide and in the operation of said carbon dioxide recovery system (iii) the stripped mixture of carbon dioxide and water vapor is cooled in order to condense a major portion of said water vapor into a liquid water phase, (iv) said liquid water phase is separated from said carbon dioxide, and (v) said liquid water phase is then recycled back to the stripping operation of (ii).

Claim 15

The process of claim 12 wherein in the operation of said carbon dioxide recovery system (vi) a portion of said stripped carbon dioxide and water vapor is vented before the cooling operation of (iii) and said waste water stream is added into said carbon dioxide recovery system after said venting operation (vi) and before said cooling operation (iii).

Claim 16

The process of claim 13 wherein said waste water stream contains from about 0.01% to about 20% by weight urea.

Claim 17

The process of claim 14 wherein said waste water stream contains from about 0.05% to about 10% by weight urea.

Claim 18

The process of claim 15 wherein said carbon dioxide recovery system is operated at a temperature from about 90° C to about 130° C.

Claim 19

The process of claim 16 wherein said aqueous solution in said carbon dioxide recovery system contains potassium carbonate.