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    • 4. 发明申请
    • METHOD FOR THE RECOVERY OF AMMONIA FROM A GASEOUS STREAM IN A SYNTHESIS PROCESS OF UREA
    • 在尿素合成过程中从气体流中恢复氨的方法
    • US20110091369A1
    • 2011-04-21
    • US12743717
    • 2008-11-14
    • Paolo CasaraAlessandro GianazzaIvano MiraccaGiuseppe MerelliGustavo CapannelliAldo Bottino
    • Paolo CasaraAlessandro GianazzaIvano MiraccaGiuseppe MerelliGustavo CapannelliAldo Bottino
    • C01C1/04C07C273/02B01D61/42
    • C07C273/04B01D53/326B01D53/58B01D53/75B01D61/44B01D61/445C02F1/20C02F1/441C02F1/4693C07C273/16Y02P20/582
    • The present invention relates to a process for the recovery of ammonia contained in a gaseous purging stream produced in a synthesis process of urea, comprising the following phases: a) subjecting the gaseous purging stream to a washing with an aqueous acidic solution, at a pH ranging from 1 to 6, with the formation of a first purified gaseous stream and an aqueous solution containing an ammonium salt; b) subjecting the aqueous solution containing the ammonium salt coming from phase a) to stripping, after treatment with a strong base, at a temperature ranging from 50 to 250° C. and a pressure ranging from 1 to 40 absolute bar, with the formation of a second gaseous stream comprising NH3, H2O and possibly CO2 and a solution containing a salt of the cation of said strong base; c) subjecting the solution containing the salt of the cation of the strong base coming from phase b) to a Membrane Electrochemical Process (MEP) with the formation of an aqueous solution of the acid used in phase a), an aqueous solution of the base used in phase b) and possibly a diluted aqueous solution of the cation salt of the strong base; d) recycling said aqueous solution of the acid and aqueous solution of the base to phase a) and to phase b) respectively, and recycling said second gaseous stream coming from phase b) to the urea synthesis process. The relative equipment is also described.
    • 本发明涉及一种在尿素合成过程中产生的气态吹扫液中所含的氨的回收方法,包括以下阶段:a)在酸性溶液中以pH值进行洗涤, 形成第一纯化气流和含有铵盐的水溶液; b)使来自a)相的含有铵盐的水溶液在强碱处理后,在50-250℃的温度和1至40绝对巴的压力下进行汽提,同时形成 包含NH 3,H 2 O和可能的CO 2的第二气流和含有所述强碱的阳离子的盐的溶液; c)在相a)中使用的酸的水溶液的形成,将含有来自相b)的强碱的阳离子盐的溶液经受膜电化学工艺(MEP),将碱的水溶液 在阶段b)中使用,并且可能是强碱的阳离子盐的稀释水溶液; d)将所述碱的酸和水溶液的所述水溶液分别循环到a)相和b相,并将来自b)相的所述第二气流再循环到尿素合成过程。 还描述了相关设备。