Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
266 words
In a process for the preparation of melamine from urea or thermal decomposition products thereof wherein a gaseous reaction mixture containing melamine, ammonia, and carbon dioxide is formed, and wherein said ammonia and carbon dioxide, after separation of melamine therefrom, and water vapor are condensed in a condensing zone maintained at a pressure of between about 0.5 and 70 bar to form an aqueous solution of ammonium carbamate, and said aqueous solution of ammonium carbamate is increased in pressure to at least about 100 bar, heated and introduced into a urea synthesis zone wherein at least a portion of said ammonium carbamate is converted into urea at a pressure of between about 100 and 200 bar to form a urea synthesis effluent containing urea, unconverted ammonium carbamate and water, the improvement essentially comprising heating said aqueous solution of ammonium carbamate from said condensing zone, after being increased in pressure to at least about the pressure in said urea synthesis zone, sufficiently to decompose at least a portion of said ammonium carbamate into carbon dioxide and ammonia, to form a gas-liquid mixture, and introducing said gas liquid mixture into said urea synthesis zone in which said ammonia and carbon dioxide are recondensed to form ammonium carbamate, and ammonium carbamate is converted into urea, wherein the amount of ammonium carbamate decomposed in said aqueous solution and introduced into said urea synthesis zone is such that the heat released by said recondensation of ammonia and carbon dioxide to ammonium carbamate is at least sufficient to provide all of the heat required for said conversion of ammonium carbamate into urea.
Claim 2
Dependent Claim
266 words
In a process for the preparation of melamine from urea or thermal decomposition products thereof wherein a gaseous reaction mixture containing melamine, ammonia, and carbon dioxide is formed, and wherein said ammonia and carbon dioxide, after separation of melamine therefrom, and water vapor are condensed in a condensing zone maintained at a pressure of between about 0.5 and 70 bar to form an aqueous solution of ammonium carbamate, and said aqueous solution of ammonium carbamate is increased in pressure to at least about 100 bar, heated and introduced into a urea synthesis zone wherein at least a portion of said ammonium carbamate is converted into urea at a pressure of between about 100 and 200 bar to form a urea synthesis effluent containing urea, unconverted ammonium carbamate and water, the improvement essentially comprising heating said aqueous solution of ammonium carbamate from said condensing zone, after being increased in pressure to at least about the pressure in said urea synthesis zone, sufficiently to decompose at least a portion of said ammonium carbamate into carbon dioxide and ammonia, to form a gas-liquid mixture, and introducing said gas liquid mixture into said urea synthesis zone in which said ammonia and carbon dioxide are recondensed to form ammonium carbamate, and ammonium carbamate is converted into urea, wherein the amount of ammonium carbamate decomposed in said aqueous solution and introduced into said urea synthesis zone is such that the heat released by said recondensation of ammonia and carbon dioxide to ammonium carbamate is at least sufficient to provide all of the heat required for said conversion of ammonium carbamate into urea.
Claim 3
Dependent Claim
23 words
The process of claim 1 or 2 wherein said urea synthesis zone is maintained at a temperature of between 180° and 200° C.
Claim 4
Dependent Claim
33 words
The process of claim 1 wherein urea from urea synthesis zone is processed to form a substantially water-free urea melt, which is thereafter utilized for the preparation of a further quantity of melamine.
Claim 5
Dependent Claim
38 words
The process of claim 1 wherein said urea synthesis effluent is heated in at least one pressure stage to decompose ammonium carbamate, and the ammonia and carbon dioxide thus formed are separated from the remaining product urea stream.
Claim 6
Dependent Claim
28 words
The process of claim 4 wherein the gaseous mixture of ammonia and carbon dioxide separated from said product urea stream is condensed to form an ammonium carbamate solution.
Claim 7
Dependent Claim
47 words
The process of claim 4 wherein said urea synthesis effluent is heated in a plurality of pressure stages so as to decompose ammonium carbamate, and the ammonia and carbon dioxide thus formed are separated as a gaseous mixture from the remaining product urea stream in each stage.
Claim 8
Dependent Claim
31 words
The process of claim 6 wherein said gaseous mixtures containing ammonia and carbon dioxide separated from said product urea streams are separately or jointly condensed to form an ammonium carbamate solution.
Claim 9
Dependent Claim
94 words
The process of claim 7 wherein said urea synthesis effluent is heated at a pressure of between about 10 and 70 bar in a first pressure stage to form a first gaseous mixture containing ammonia and carbon dioxide and a first product urea solution still containing unconverted ammonium carbamate, and said first urea product stream is heated at a pressure of between about 0.5 and 7 bar in a second pressure stage thereby forming a second urea product stream substantially free of ammonium carbamate, and a second gaseous mixture containing ammonia and carbon dioxide.
Claim 10
Dependent Claim
36 words
The process of claim 8 wherein said second gaseous mixture is condensed to form a second aqueous ammonium carbamate solution, and said first gaseous mixture is condensed in the presence of said second ammonium carbamate solution.
Claim 11
Dependent Claim
57 words
The process of claim 4, 5, 6, 7, 8, or 9 wherein at least one gaseous mixture obtained by the decomposition of ammonium carbamate present in said urea synthesis effluent is introduced into a condensing zone and condensed together with said ammonia and carbon dioxide from said melamine preparation to form an aqueous solution of ammonium carbamate.
Claim 12
Dependent Claim
48 words
The process of claim 4, 5, 6, 7, 8, or 9 wherein at least one gaseous mixture obtained by the decomposition of ammonium carbamate present in said urea synthesis effluent is condensed separate from said condensing zone, and the condensate thus formed is introduced into said condensing zone.