Process for purifying urea-containing waste water and process for preparing melamine

Claim 2

In a process for the removal of urea from urea-containing waste water by treating said waste water at elevated temperature and pressure to hydrolyze urea, and desorbing ammonia and carbon dioxide thus formed, the improvement comprising carrying out said urea removal in conjunction with the separation of ammonia and carbon dioxide from a process stream containing mixtures thereof by the steps of: (a) separating, in an ammonia separation zone, an ammonia off-gas substantially free of carbon dioxide and water from a first residual liquid phase containing ammonia, carbon dioxide and water, and introducing said first residual liquid phase into a carbon dioxide separation zone; (b) separating, in said carbon dioxide separation zone, a carbon dioxide off-gas substantially free of ammonia and water from a second residual liquid phase containing ammonia, carbon dioxide and water, and introducing said second residual liquid phase into a desorption zone; and (c) separating, in said desorption zone, an off-gas containing ammonia, carbon dioxide and water vapor from a third residual liquid phase substantially free of ammonia and carbon dioxide, and introducing at least a portion of said off-gas into said ammonia separation zone; wherein said process stream and said urea-containing waste water are introduced into any of steps (a), (b) or (c).

Claim 3

The process of claim 1 wherein said desorption zone is operated at a pressure of between about 5 and 50 bar.

Claim 4

The process of claim 1 wherein said desorption zone is operated at a pressure of between 20 and 40 bar.

Claim 5

The process of claims 1, 2 or 3 wherein said urea-containing waste water is introduced into said carbon dioxide separation zone in step (b).

Claim 6

The process of claim 1 wherein said process is practiced in conjunction with a process for the preparation of melamine from urea and said process stream containing a mixture of ammonia and carbon dioxide is derived from said process from producing melamine.

Claim 7

In a process for the preparation of melamine by the catalytic conversion of urea in the presence of gaseous ammonia to form a gaseous reaction mixture containing melamine, ammonia and carbon dioxide, separation of melamine from the gaseous reaction mixture and thereafter forming an aqueous solution of ammonia and carbon dioxide from the remainder of such mixture, and separating the ammonia and carbon dioxide contained in such solution by the steps of: (a) separating, in an ammonia separation zone, an ammonia off-gas substantially free of carbon dioxide and water from a first residual liquid phase containing ammonia, carbon dioxide and water, and introducing said first liquid residual phase into a carbon dioxide separation zone; (b) separating, in said carbon dioxide separation zone, a carbon dioxide off-gas substantially free of ammonia and water from a second residual liquid phase containing ammonia, carbon dioxide and water, and introducing said second residual liquid phase into a desorption zone; and (c) separating, in said desorption zone, an off-gas containing ammonia, carbon dioxide and water vapor from a third residual liquid phase substantially free of ammonia and carbon dioxide, and introducing at least a portion of said off-gas into said ammonia separation zone; wherein said aqueous solution is introduced into any of steps (a), (b) and (c), the improvement comprising additionally introducing into said carbon dioxide separation zone a urea-containing waste water stream and substantially completely hydrolyzing said urea, and separating the resulting ammonia and carbon dioxide in said steps (a), (b) and (c).

Claim 8

In a process for the preparation of melamine by the catalytic conversion of urea in the presence of gaseous ammonia to form a gaseous reaction mixture containing melamine, ammonia and carbon dioxide, separation of melamine from the gaseous reaction mixture and thereafter forming an aqueous solution of ammonia and carbon dioxide from the remainder of such mixture, and separating the ammonia and carbon dioxide contained in such solution by the steps of: (a) separating, in an ammonia separation zone, an ammonia off-gas substantially free of carbon dioxide and water from a first residual liquid phase containing ammonia, carbon dioxide and water, and introducing said first liquid residual phase into a carbon dioxide separation zone; (b) separating, in said carbon dioxide separation zone, a carbon dioxide off-gas substantially free of ammonia and water from a second residual liquid phase containing ammonia, carbon dioxide and water, and introducing said second residual liquid phase into a desorption zone; and (c) separating, in said desorption zone, an off-gas containing ammonia, carbon dioxide and water vapor from a third residual liquid phase substantially free of ammonia and carbon dioxide, and introducing at least a portion of said off-gas into said ammonia separation zone; wherein said aqueous solution is introduced into any of steps (a), (b) and (c), the improvement comprising additionally introducing into said carbon dioxide separation zone a urea-containing waste water stream and substantially completely hydrolyzing said urea, and separating the resulting ammonia and carbon dioxide in said steps (a), (b) and (c).

Claim 9

The process of claim 6 wherein said process is carried out in conjunction with a process for the synthesis of urea from ammonia and carbon dioxide at an elevated temperature and pressure to produce an aqueous solution of urea, concentrating said aqueous urea solution by evaporation of water thereby forming a vapor phase containing water, ammonia, carbon dioxide and urea, condensing said vapor phase to form said urea-containing waste water introduced into said carbon dioxide separation zone, and utilizing at least a portion of the concentrated urea for the production of said melamine.