Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
222 words
In a process for preparing urea by reacting ammonia and carbon dioxide to form an ammonium carbamate intermediate product in a first reaction zone, and then converting ammonium carbamate into urea in an additional reaction zone at a higher pressure, partially expanding the resulting urea synthesis solution and subjecting the urea synthesis solution to a stripping treatment, and separating gases released in the stripping treatment and from the urea synthesis solution and recycling the separated gases to the first reaction zone, the improvement comprising conducting the formation of ammonium carbamate from ammonia and carbon dioxide in said first reaction zone at a pressure of 90 - 140 atmospheres and a temperature of about 150° to 173° C, thereafter partly converting the ammonium carbamate into urea in a second reaction zone at substantially the same pressure as said first reaction zone and a temperature of about 165 to 183° C until at least 40% of the equilibrium amount of urea has been formed, and thereafter converting ammonium carbamate present in the synthesis solution from the second reaction zone into additional urea in a third reaction zone at a pressure of at least 160 atmospheres and a temperature of about 190° to 220° C until at least 85% of the equilibrium amount of urea that can be obtained in this zone has been formed.
Claim 2
Dependent Claim
222 words
In a process for preparing urea by reacting ammonia and carbon dioxide to form an ammonium carbamate intermediate product in a first reaction zone, and then converting ammonium carbamate into urea in an additional reaction zone at a higher pressure, partially expanding the resulting urea synthesis solution and subjecting the urea synthesis solution to a stripping treatment, and separating gases released in the stripping treatment and from the urea synthesis solution and recycling the separated gases to the first reaction zone, the improvement comprising conducting the formation of ammonium carbamate from ammonia and carbon dioxide in said first reaction zone at a pressure of 90 - 140 atmospheres and a temperature of about 150° to 173° C, thereafter partly converting the ammonium carbamate into urea in a second reaction zone at substantially the same pressure as said first reaction zone and a temperature of about 165 to 183° C until at least 40% of the equilibrium amount of urea has been formed, and thereafter converting ammonium carbamate present in the synthesis solution from the second reaction zone into additional urea in a third reaction zone at a pressure of at least 160 atmospheres and a temperature of about 190° to 220° C until at least 85% of the equilibrium amount of urea that can be obtained in this zone has been formed.
Claim 3
Dependent Claim
23 words
Process according to claim 1, wherein from 70 - 95% of the equilibrium amount of urea is formed in said second reaction zone.
Claim 4
Dependent Claim
63 words
Process according to claim 1, wherein carbon dioxide is incompletely converted into ammonium carbamate in the first reaction zone and at least most of the unconverted carbon dioxide is converted into ammonium carbamate in the second reaction zone, whereby the heat of ammonium carbamate formation in said second reaction zone supplies substantially all the heat required for urea formation in said reaction zone.
Claim 5
Dependent Claim
39 words
Process according to claim 1, wherein substantially all the heat required for the formation of urea in said third reaction zone is supplied by forming additional ammonium carbamate in said third reaction zone from ammonia and additional carbon dioxide.
Claim 6
Dependent Claim
18 words
Process according to claim 1, wherein the pressure in said third reaction zone is 160 - 300 atmospheres.
Claim 7
Dependent Claim
18 words
Process according to claim 1, wherein the pressure in said third reaction zone is 180 - 200 atmospheres.
Claim 8
Dependent Claim
33 words
Process according to claim 1, wherein ammonium carbamate is converted into urea in said second reaction zone in an amount corresponding to about 40 - about 90% of the equilibrium amount of urea.