Patent US4066693A successfully refreshed from Google Patents.
← Back to Patent Explorer
US4066693A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the preparation of urea

Assignee: Stamicarbon BV
•
Filing: 1972-08-29
•
Granted: 1978-01-03
•
Expires: 1992-08-29
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A process for preparing urea by the intermediate formation of ammonium carbamate is disclosed, wherein the process involves reduced use of high pressure steam, and the reduced production, as a by-product, of low pressure steam, compared to prior art processes. Ammonium carbamate is formed from ammonia and carbon dioxide in a first reaction zone at a pressure of 90 - 140 atmospheres. Thereafter, the ammonium carbamate is partly converted into urea in a second reaction zone at about the same pressure as the first reaction zone until at least 40% of the equilibrium amount of the urea has formed, and then ammonium carbamate present in the solution from the second reaction zone is converted into additional urea in the third reaction zone at a pressure of at least 160 atmospheres until at least 85% of the equilibrium amount of urea has been formed. The resulting urea synthesis solution is partially expanded and subjected to a stripping treatment, with the gases released in the stripping treatment recycled to the first reaction zone.

Inventors

  • 👤 Dirk J. Venderbos

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 15:00
CPC Classifications
C; C07; C07C; C07C273/00; C07C273/02; C07C273/04

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.

References Cited (Backward Citations)

US3105093A Cited
US3270051A Cited
US3090811A Cited
US3356723A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-01-02 1981-07-04 1982-01-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-01-02 1985-07-04 1986-01-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-01-02 1989-07-04 1990-01-03 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag