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公开(公告)号:OA8383A
公开(公告)日:1988-02-29
申请号:OA58927
申请日:1986-08-12
Applicant: STAMICARBON
Inventor: MEESSEN JOZEF HUBERT , SIPKEMA RUDOLF
IPC: C07C67/00 , C07C239/00 , C07C273/04 , C07C126/02
CPC classification number: C07C273/04
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公开(公告)号:OA08383A
公开(公告)日:1988-02-29
申请号:OA58927
申请日:1986-08-12
Applicant: STAMICARBON
Inventor: MEESSEN JOZEF HUBERT , SIPKEMA RUDOLF
IPC: C07C67/00 , C07C239/00 , C07C273/04 , C07C126/02
Abstract: Process for the preparation of urea in which- a urea synthesis solution containing carbamate and free ammonia is formed in a high-pressure part in a synthesis zone at an NH₃/CO₂ molar ratio of up to 4 : 1, a temperature of at least 175 ◊C and the corresponding pressure,- a portion of the carbamate is decomposed in a first decomposition stage at synthesis pressure or lower pressure by a stripping treatment with carbon dioxide while heating is applied, and the gas mixture thus obtained is at least in part condensed and the condensate and the non-condensed portion of the gas mixture, if any, are returned to the synthesis zone,- in at least two further decomposition stages a further portion of the carbamate still present is decomposed and the gas mixture formed is separated, in the first of the further decomposition stages a pressure of 12-30 bar being maintained and heat being supplied,- and the remaining urea-containing solution is processed further by evaporation to a concentrated urea solution and, if desired, solid urea.The gas mixture, formed on expansion of the stripped urea synthesis solution to a pressure equal to or higher than the pressure in the first one of the further decomposition stages, is brought into direct contact in a contact zone with the solution remaining after further amounts of carbamate still present have herein been decomposed and the gases thus formed have been separated. The remaining gas mixture is thereafter discharged from the contract zone and is condensed. The condensate is returned to the high-pressure part of the urea synthesis.
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公开(公告)号:BR8603801A
公开(公告)日:1987-03-17
申请号:BR8603801
申请日:1986-08-08
Applicant: STAMICARBON
Inventor: MEESSEN JOZEF HUBERT , SPIKEMA RUDOLF
IPC: C07C67/00 , C07C239/00 , C07C273/04 , C07C126/02
Abstract: Process for the preparation of urea in which- a urea synthesis solution containing carbamate and free ammonia is formed in a high-pressure part in a synthesis zone at an NH₃/CO₂ molar ratio of up to 4 : 1, a temperature of at least 175 ◊C and the corresponding pressure,- a portion of the carbamate is decomposed in a first decomposition stage at synthesis pressure or lower pressure by a stripping treatment with carbon dioxide while heating is applied, and the gas mixture thus obtained is at least in part condensed and the condensate and the non-condensed portion of the gas mixture, if any, are returned to the synthesis zone,- in at least two further decomposition stages a further portion of the carbamate still present is decomposed and the gas mixture formed is separated, in the first of the further decomposition stages a pressure of 12-30 bar being maintained and heat being supplied,- and the remaining urea-containing solution is processed further by evaporation to a concentrated urea solution and, if desired, solid urea.The gas mixture, formed on expansion of the stripped urea synthesis solution to a pressure equal to or higher than the pressure in the first one of the further decomposition stages, is brought into direct contact in a contact zone with the solution remaining after further amounts of carbamate still present have herein been decomposed and the gases thus formed have been separated. The remaining gas mixture is thereafter discharged from the contract zone and is condensed. The condensate is returned to the high-pressure part of the urea synthesis.
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公开(公告)号:AU6103986A
公开(公告)日:1987-02-19
申请号:AU6103986
申请日:1986-08-11
Applicant: STAMICARBON
Inventor: MEESSEN JOZEF HUBERT , SIPKEMA RUDOLF
IPC: C07C67/00 , C07C239/00 , C07C273/04 , C07C126/02
Abstract: Process for the preparation of urea in which- a urea synthesis solution containing carbamate and free ammonia is formed in a high-pressure part in a synthesis zone at an NH₃/CO₂ molar ratio of up to 4 : 1, a temperature of at least 175 ◊C and the corresponding pressure,- a portion of the carbamate is decomposed in a first decomposition stage at synthesis pressure or lower pressure by a stripping treatment with carbon dioxide while heating is applied, and the gas mixture thus obtained is at least in part condensed and the condensate and the non-condensed portion of the gas mixture, if any, are returned to the synthesis zone,- in at least two further decomposition stages a further portion of the carbamate still present is decomposed and the gas mixture formed is separated, in the first of the further decomposition stages a pressure of 12-30 bar being maintained and heat being supplied,- and the remaining urea-containing solution is processed further by evaporation to a concentrated urea solution and, if desired, solid urea.The gas mixture, formed on expansion of the stripped urea synthesis solution to a pressure equal to or higher than the pressure in the first one of the further decomposition stages, is brought into direct contact in a contact zone with the solution remaining after further amounts of carbamate still present have herein been decomposed and the gases thus formed have been separated. The remaining gas mixture is thereafter discharged from the contract zone and is condensed. The condensate is returned to the high-pressure part of the urea synthesis.
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公开(公告)号:NO863211A
公开(公告)日:1987-02-13
申请号:NO863211
申请日:1986-08-08
Applicant: STAMICARBON
Inventor: MEESSEN JOZEF HUBERT , SIPKEMA RUDOLF
IPC: C07C67/00 , C07C239/00 , C07C273/04 , C07C126/00
CPC classification number: C07C273/04
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公开(公告)号:MY190234A
公开(公告)日:2022-04-06
申请号:MYPI2014703218
申请日:2013-05-02
Applicant: STAMICARBON
IPC: C07C273/04
Abstract: Method for the production of urea from ammonia and carbon dioxide in a urea plant containing a high-pressure synthesis section with a horizontal pool condenser, wherein the method comprises exchanging heat from a high pressure process medium received in a shell section of the pool condenser to a medium pressure urea containing solution received in a first heat exchanging section provided in the pool condenser to at least decompose ammonium carbamate into NH3 and CO2, wherein the method further comprises exchanging heat from the high pressure process medium to a low pressure steam condensate received in a second heat exchanging section provided in the pool condenser to produce low pressure steam. The invention also relates to an apparatus for the production of urea from ammonia and carbon dioxide. [Fig. 1]
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公开(公告)号:PL3190101T3
公开(公告)日:2020-03-31
申请号:PL17151200
申请日:2013-05-02
Applicant: STAMICARBON
IPC: C07C273/04
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公开(公告)号:PL2844640T3
公开(公告)日:2018-12-31
申请号:PL13724000
申请日:2013-05-02
Applicant: STAMICARBON
Inventor: MENNEN JOHANNES HENRICUS , MEESSEN JOZEF HUBERT
IPC: C07C273/04
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公开(公告)号:PL2297094T3
公开(公告)日:2018-04-30
申请号:PL09749836
申请日:2009-05-19
Applicant: STAMICARBON
IPC: C07C273/04
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公开(公告)号:AU2013257378B2
公开(公告)日:2017-03-09
申请号:AU2013257378
申请日:2013-05-02
Applicant: STAMICARBON
IPC: C07C273/04
Abstract: Method for the production of urea from ammonia and carbon dioxide in a urea plant containing a high-pressure synthesis section with a horizontal pool condenser, wherein the method comprises exchanging heat from a high pressure process medium received in a shell section of the pool condenser to a medium pressure urea containing solution received in a first heat exchanging section provided in the pool condenser to at least decompose ammonium carbamate into NH
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