GB1060781A - Improvements relating to the production of urea - Google Patents
Improvements relating to the production of ureaInfo
- Publication number
- GB1060781A GB1060781A GB633264A GB633264A GB1060781A GB 1060781 A GB1060781 A GB 1060781A GB 633264 A GB633264 A GB 633264A GB 633264 A GB633264 A GB 633264A GB 1060781 A GB1060781 A GB 1060781A
- Authority
- GB
- United Kingdom
- Prior art keywords
- urea
- reactor
- cos
- seconds
- produced
- 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
Abstract
Urea is prepared by reacting CO with sulphur vapour at 250 DEG -700 DEG C. for 0.01-20 seconds in the presence of a sulphide of a metal of Group V, VI, VII or VIII of the Periodic Table, cooling the resulting COS, adding NH3, and passing the mixture at 60 DEG -100 DEG C. over a microporous material (such as active alumina, silica gel, pumice or active carbon); with the proviso that when active carbon is used as the microporous material and the COS is produced at 300 DEG -700 DEG C., the reaction time for the production of the COS is not 1-20 seconds. The urea is produced on the microporous material, together with H2S; the latter may be desorbed with CO-containing gas which is then fed to the COS reactor. The urea is extracted from the reactor by means of liquid ammonia, or aqueous urea solutions obtained from previous extractions. More than one urea reactor may be used. The last reactor may be operated at below 40 DEG C., when residual NH3 is bound as NH4SH, which will react to form urea when another reactor is switched in and the temperature of the previously last reactor is raised.ALSO:Carbonyl sulphide is produced by reacting CO with sulphur vapour at 250-700 DEG C. for 0.01-20 seconds in the presence of a sulphide of a metal of Group V, VI, VII or VIII of the Periodic Table.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEN22758A DE1161256B (en) | 1963-02-16 | 1963-02-16 | Process for the production of urea from carbon monoxide and ammonia |
DEN0023568 | 1963-08-06 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1060781A true GB1060781A (en) | 1967-03-08 |
Family
ID=25988847
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB633264A Expired GB1060781A (en) | 1963-02-16 | 1964-02-14 | Improvements relating to the production of urea |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE1468401A1 (en) |
GB (1) | GB1060781A (en) |
-
1963
- 1963-08-06 DE DE19631468401 patent/DE1468401A1/en active Pending
-
1964
- 1964-02-14 GB GB633264A patent/GB1060781A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
DE1468401A1 (en) | 1969-03-06 |
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