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    • 2. 发明申请
    • Process for Urea Production and Related Plant
    • 尿素生产工艺及相关工厂
    • US20100063321A1
    • 2010-03-11
    • US12513487
    • 2007-10-09
    • Federico ZardiPaolo BrunengoPaolo Sticchi
    • Federico ZardiPaolo BrunengoPaolo Sticchi
    • C07C273/04B01J10/00
    • C07C273/04
    • A process for urea production from ammonia and carbon dioxide, in which part of the aqueous solution comprising urea, ammonium carbamate and ammonia obtained in a urea synthesis section is subjected to dissociation in a treatment section operating at a predetermined medium pressure for the recovery of the ammonium carbamate and of the ammonia contained in it, comprises the steps of subjecting the urea aqueous solution resulting from the aforementioned dissociation step to decomposition in a low pressure urea recovery section and of using at least a part of the condensed steam, obtained by indirect thermal exchange with a second part of said aqueous solution comprising urea, ammonium carbmate and ammonia in a high-pressure stripping unit, as a heating fluid for the dissociation of the first part of the aqueous solution comprising urea, ammonium carbmate and ammonia in the medium-pressure treatment section.
    • 一种由氨和二氧化碳生产尿素的方法,其中在尿素合成段中得到的包含尿素,氨基甲酸铵和氨水的部分水溶液在预定介质压力下操作的处理段中解离,以回收 氨基甲酸铵和其中所含的氨的方法包括以下步骤:将由上述解离步骤产生的尿素水溶液在低压尿素回收段中分解并使用至少一部分冷凝蒸汽,通过间接热 在包含尿素,氨基甲酸铵和氨的第二部分的高压汽提装置中与第二部分水溶液交换,所述加热流体用于在介质中包含尿素,氨基甲酸铵和氨的水溶液的第一部分的解离, 压力处理部。
    • 3. 发明申请
    • Process for Urea Production and Related Plant
    • 尿素生产工艺及相关工厂
    • US20080219900A1
    • 2008-09-11
    • US11817186
    • 2005-11-15
    • Domenico RomitiPaolo Sticchi
    • Domenico RomitiPaolo Sticchi
    • B01J19/00C07C273/04
    • C07C273/04B01J2219/00006B01J2219/00103B01J2219/00108B01J2219/182B01J2219/185Y02P20/142
    • A process for urea production from ammonia and carbon dioxide, made to react at a predetermined high pressure in an appropriate synthesis reactor (112), from the reaction between NH3 and CO2 being obtained a reaction mixture comprising urea, ammonium carbamate and free ammonia in aqueous solution, from which a recovery of ammonium carbamate and ammonia is carried out with their subsequent recycle to the synthesis reactor (112), said recovery from the reaction mixture taking place through operative steps of decomposition of the ammonium carbamate into NH3 and CO2 and of their stripping and a subsequent operative step of their recondensation into ammonium carbamate that is recycled to the synthesis reactor, the said reaction mixture obtained from the reaction between ammonia and carbon dioxide being pumped to the operative steps of decomposition and stripping.
    • 一种由氨和二氧化碳生产尿素的方法,其在合适的合成反应器(112)中以预定的高压反应,从NH 3和CO 2之间的反应 得到包含尿素,氨基甲酸铵和游离氨水溶液的反应混合物,从其中进行氨基甲酸铵和氨的回收,随后再循环到合成反应器(112),所述从反应混合物中回收的物质发生 通过氨基甲酸铵分解成NH 3和CO 2 2及其汽提的操作步骤和随后的再次还原成氨基甲酸铵的操作步骤,其被再循环到合成物 将从氨和二氧化碳之间的反应获得的所述反应混合物泵送到分解和汽提的操作步骤。
    • 4. 发明授权
    • Process for urea production and related plant
    • 尿素生产工艺及相关工厂
    • US08383856B2
    • 2013-02-26
    • US11817186
    • 2005-11-15
    • Domenico RomitiPaolo Sticchi
    • Domenico RomitiPaolo Sticchi
    • C07C273/04C07C273/14C07C275/02C01B21/12
    • C07C273/04B01J2219/00006B01J2219/00103B01J2219/00108B01J2219/182B01J2219/185Y02P20/142
    • A process for urea production from ammonia and carbon dioxide, made to react at a predetermined high pressure in an appropriate synthesis reactor (112), from the reaction between NH3 and CO2 being obtained a reaction mixture comprising urea, ammonium carbamate and free ammonia in aqueous solution, from which a recovery of ammonium carbamate and ammonia is carried out with their subsequent recycle to the synthesis reactor (112), said recovery from the reaction mixture taking place through operative steps of decomposition of the ammonium carbamate into NH3 and CO2 and of their stripping and a subsequent operative step of their recondensation into ammonium carbamate that is recycled to the synthesis reactor, the said reaction mixture obtained from the reaction between ammonia and carbon dioxide being pumped to the operative steps of decomposition and stripping.
    • 由氨和二氧化碳制备的尿素在适当的合成反应器(112)中由NH 3和CO 2之间的反应在预定的高压下反应得到包含尿素,氨基甲酸铵和游离氨水溶液的反应混合物 溶液,其中氨基甲酸铵和氨的回收率随后再循环到合成反应器(112)中,所述从反应混合物中回收,通过氨基甲酸铵分解成NH 3和CO 2以及它们的操作步骤进行 汽提和随后的将其再缩合成氨基甲酸铵再循环到合成反应器中的操作步骤,将从氨和二氧化碳之间的反应获得的所述反应混合物泵送到分解和汽提的操作步骤。
    • 5. 发明授权
    • Process for urea production and related plant
    • 尿素生产工艺及相关工厂
    • US07982068B2
    • 2011-07-19
    • US12513487
    • 2007-10-09
    • Federico ZardiPaolo BrunengoPaolo Sticchi
    • Federico ZardiPaolo BrunengoPaolo Sticchi
    • C07C273/16C07C273/04
    • C07C273/04
    • A process for urea production from ammonia and carbon dioxide, in which part of the aqueous solution comprising urea, ammonium carbamate and ammonia obtained in a urea synthesis section is subjected to dissociation in a treatment section operating at a predetermined medium pressure for the recovery of the ammonium carbamate and of the ammonia contained in it, comprises the steps of subjecting the urea aqueous solution resulting from the aforementioned dissociation step to decomposition in a low pressure urea recovery section and of using at least a part of the condensed steam, obtained by indirect thermal exchange with a second part of said aqueous solution comprising urea, ammonium carbmate and ammonia in a high-pressure stripping unit, as a heating fluid for the dissociation of the first part of the aqueous solution comprising urea, ammonium carbmate and ammonia in the medium-pressure treatment section.
    • 一种由氨和二氧化碳生产尿素的方法,其中在尿素合成段中得到的包含尿素,氨基甲酸铵和氨水的部分水溶液在预定介质压力下操作的处理段中解离,以回收 氨基甲酸铵和其中所含的氨的方法包括以下步骤:将由上述解离步骤产生的尿素水溶液在低压尿素回收段中分解并使用至少一部分冷凝蒸汽,通过间接热 在包含尿素,氨基甲酸铵和氨的第二部分的高压汽提装置中与第二部分水溶液交换,所述加热流体用于在介质中包含尿素,氨基甲酸铵和氨的水溶液的第一部分的解离, 压力处理部。