GB1196657A - Process for the Manufacture of Urea from Ammonia and Carbon Dioxide - Google Patents
Process for the Manufacture of Urea from Ammonia and Carbon DioxideInfo
- Publication number
- GB1196657A GB1196657A GB4409767A GB4409767A GB1196657A GB 1196657 A GB1196657 A GB 1196657A GB 4409767 A GB4409767 A GB 4409767A GB 4409767 A GB4409767 A GB 4409767A GB 1196657 A GB1196657 A GB 1196657A
- Authority
- GB
- United Kingdom
- Prior art keywords
- urea
- ammonia
- synthesis
- distillation zone
- carbamate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C273/00—Preparation of urea or its derivatives, i.e. compounds containing any of the groups, the nitrogen atoms not being part of nitro or nitroso groups
- C07C273/02—Preparation of urea or its derivatives, i.e. compounds containing any of the groups, the nitrogen atoms not being part of nitro or nitroso groups of urea, its salts, complexes or addition compounds
- C07C273/04—Preparation of urea or its derivatives, i.e. compounds containing any of the groups, the nitrogen atoms not being part of nitro or nitroso groups of urea, its salts, complexes or addition compounds from carbon dioxide and ammonia
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
1,196,657. Urea. G. GIOMMI. 28 Sept., 1967, No. 44097/67. Heading C2C. A continuous process for the synthesis of urea from ammonia and carbon dioxide under elevated temperatures and pressures comprises the step of splitting the ammonium, carbonate which is not converted into urea into its components by distillation at temperatures and pressures approximately equal to synthesis pressures and temperatures in the presence of an excess quantity of gaseous ammonia, the split products being readmitted to the urea synthesis and the urea being drawn off from the distillation zone, the improvement comprising condensing the split products withdrawn from said distillation zone so as to form liquid carbamate and separating the same from said excess ammonia, returning said carbamate into the urea synthesis, recirculating said ammonia into the distillation zone, and adding at least a portion of the CO 2 used in the synthesis to the gases withdrawn from the distillation zone before their condensation. The gases withdrawn from the distillation zone may be condensed with the simultaneous addition of small quantities of water sufficient to prevent the precipitation of the condensed carbamate. The recirculated excess ammonia, which may be further compressed and separated from inert components, may be admitted to the distillation zone together with at least a part of the total ammonia charged into the synthesis. Suitable forms of apparatus for carrying out the above process are described.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB4409767A GB1196657A (en) | 1967-09-28 | 1967-09-28 | Process for the Manufacture of Urea from Ammonia and Carbon Dioxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB4409767A GB1196657A (en) | 1967-09-28 | 1967-09-28 | Process for the Manufacture of Urea from Ammonia and Carbon Dioxide |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1196657A true GB1196657A (en) | 1970-07-01 |
Family
ID=10431768
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB4409767A Expired GB1196657A (en) | 1967-09-28 | 1967-09-28 | Process for the Manufacture of Urea from Ammonia and Carbon Dioxide |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB1196657A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5750780A (en) * | 1995-06-30 | 1998-05-12 | Snamprogetti S.P.A. | Process for the synthesis of urea comprising two separate reaction zones |
US6342632B1 (en) | 1995-02-01 | 2002-01-29 | Urea Casale | Process and plant for the production of urea with high conversion yield and low energy consumption |
-
1967
- 1967-09-28 GB GB4409767A patent/GB1196657A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6730278B2 (en) | 1995-01-27 | 2004-05-04 | Urea Casale | Process and plant for the production of urea with high conversion yield and low energy consumption |
US6342632B1 (en) | 1995-02-01 | 2002-01-29 | Urea Casale | Process and plant for the production of urea with high conversion yield and low energy consumption |
EP0796244B2 (en) † | 1995-02-01 | 2003-03-05 | Urea Casale S.A. | Process and plant for the production of urea with high conversion yield and low energy consumption |
US5750780A (en) * | 1995-06-30 | 1998-05-12 | Snamprogetti S.P.A. | Process for the synthesis of urea comprising two separate reaction zones |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
732 | Registration of transactions, instruments or events in the register (sect. 32/1977) | ||
PE20 | Patent expired after termination of 20 years |