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    • 4. 发明申请
    • ENHANCED PROCESS FOR THE SYNTHESIS OF UREA
    • 用于合成尿素的增强方法
    • US20100217041A1
    • 2010-08-26
    • US12601103
    • 2008-05-19
    • Lino CarlessiAlessandro Gianazza
    • Lino CarlessiAlessandro Gianazza
    • C07C273/04B01J19/00
    • C07C273/04B01J2219/00006B01J2219/0004Y02P20/582
    • An enhanced process is described for the synthesis of urea from ammonia and carbon dioxide, at a high pressure and temperature, with the formation of ammonium carbamate as intermediate, which includes a high pressure synthesis section, comprising at least one separation step by decomposition-stripping with ammonia of the non-converted ammonium carbamate, carried out in a vertical apparatus, commonly called stripper, characterized in that said step also comprises a feeding, in the lower part of said stripper, of a stream of CO2, heated to a temperature ranging from 130 to 230° C., in a quantity of 1 to 15% by weight with respect to the total weight of the fresh CO2 fed to the process, containing a passivating agent in such a quantity that its equivalent content of O2 in moles varies from 0.05% to 0.80% with respect to the moles of CO2 of said stream.
    • 描述了用于在高压和高温下从氨和二氧化碳合成脲的增强方法,其中形成氨基甲酸铵作为中间体,其包括高压合成段,其包括至少一个通过分解汽提的分离步骤 与未转化的氨基甲酸铵的氨在垂直装置(通常称为汽提器)中进行,其特征在于,所述步骤还包括在所述汽提器的下部中进料加热至温度范围的CO 2流 相对于进料至该方法的新鲜CO 2的总重量为130至230℃,其含量为1至15重量%,其含有其当量的O 2的摩尔数相当的量的钝化剂 相对于所述料流的CO 2的摩尔数为0.05%至0.80%。
    • 5. 发明授权
    • Tube bundle equipment with liquid flow regulator elements
    • 管束设备带有液体流量调节元件
    • US09068781B2
    • 2015-06-30
    • US13318793
    • 2010-04-27
    • Alessandro GianazzaLino Carlessi
    • Alessandro GianazzaLino Carlessi
    • F28F25/06F28D3/02F28D3/04B01J19/24F28F19/06
    • F28D3/02B01J19/2425F28D3/04F28F19/06F28F25/06Y10T29/49391
    • Tube-bundle equipment of the falling liquid film type, comprising a vertical cylindrical body closed at the ends and divided into at least an upper section, an intermediate section and a lower section by means of two perforated tube sheets arranged transversally to support the tubes forming the bundle, wherein each of said tubes is surmounted, on the upper end, by a ferrule, for the inlet and distribution of the liquid in the form of a film, which comprises in the upper part, one or more openings for the outlet of vapors, at an intermediate height one or more openings, preferably tangential, for the inlet of the liquid and below, a circular base for resting on said tube from which an internal cylindrical section, inserted in the tube for a length varying from 10 to 200 mm, protrudes downwards together with an outer metallic strip for a length of at least 2 mm, so that, in the circular area defined between said outer metallic strip and said protruding cylindrical section, there is a gasket, inserted between said circular base of the ferrule and said upper edge of the tube.
    • 下降液膜类型的管束设备包括垂直圆柱体,其端部封闭,并且通过横向布置以支撑管形成的两个穿孔管板至少分成上部段,中间部分和下部段 其中每个所述管在上端被一个套圈覆盖,用于将膜形式的液体入口和分配,其中在上部包括用于出口的一个或多个开口 在中间高度处的一个或多个开口,优选是切向的,用于液体入口和下方的蒸汽,用于搁置在所述管上的圆形基部,从该管的内部插入管中的长度为10至200的长度的内部圆柱形部分 mm,与外部金属条一起向下突出至少2mm的长度,使得在限定在所述外部金属条和所述突出圆柱形部分之间的圆形区域中,存在气体 插入在所述套圈的所述圆形基座和所述管的所述上边缘之间。
    • 6. 发明申请
    • TUBE BUNDLE EQUIPMENT WITH LIQUID FLOW REGULATOR ELEMENTS
    • 具有液体流量调节器元件的管道装置
    • US20120097378A1
    • 2012-04-26
    • US13318793
    • 2010-04-27
    • Alessandro GianazzaLino Carlessi
    • Alessandro GianazzaLino Carlessi
    • F28F1/00B23P15/26
    • F28D3/02B01J19/2425F28D3/04F28F19/06F28F25/06Y10T29/49391
    • Tube-bundle equipment of the falling liquid film type, comprising a vertical cylindrical body closed at the ends and divided into at least an upper section, an intermediate section and a lower section by means of two perforated tube sheets arranged transversally to support the tubes forming the bundle, wherein each of said tubes is surmounted, on the upper end, by a ferrule, for the inlet and distribution of the liquid in the form of a film, which comprises in the upper part, one or more openings for the outlet of vapours, at an intermediate height one or more openings, preferably tangential, for the inlet of the liquid and below, a circular base for resting on said tube from which an internal cylindrical section, inserted in the tube for a length varying from 10 to 200 mm, protrudes downwards together with an outer metallic strip for a length of at least 2 mm, so that, in the circular area defined between said outer metallic strip and said protruding cylindrical section, there is a gasket, inserted between said circular base of the ferrule and said upper edge of the tube.
    • 下降液膜类型的管束设备包括垂直圆柱体,其端部封闭,并且通过横向布置以支撑管形成的两个穿孔管板至少分成上部段,中间部分和下部段 其中每个所述管在上端被一个套圈覆盖,用于将膜形式的液体入口和分配,其中在上部包括用于出口的一个或多个开口 在中间高度处的一个或多个开口,优选是切向的,用于液体入口和下方的蒸汽,用于搁置在所述管上的圆形基部,从该管的内部插入管中的长度为10至200的长度的内部圆柱形部分 mm,与外部金属条一起向下突出至少2mm的长度,使得在限定在所述外部金属条和所述突出圆柱形部分之间的圆形区域中,存在ga 插入在所述套圈的所述圆形基座和所述管的所述上边缘之间。
    • 7. 发明授权
    • Enhanced process for the synthesis of urea
    • 增强尿素合成工艺
    • US08106241B2
    • 2012-01-31
    • US12601103
    • 2008-05-19
    • Lino CarlessiAlessandro Gianazza
    • Lino CarlessiAlessandro Gianazza
    • C07C273/04
    • C07C273/04B01J2219/00006B01J2219/0004Y02P20/582
    • An enhanced process is described for the synthesis of urea from ammonia and carbon dioxide, at a high pressure and temperature, with the formation of ammonium carbamate as intermediate, which includes a high pressure synthesis section, comprising at least one separation step by decomposition-stripping with ammonia of the non-converted ammonium carbamate, carried out in a vertical apparatus, commonly called stripper, characterized in that said step also comprises a feeding, in the lower part of said stripper, of a stream of CO2, heated to a temperature ranging from 130 to 230° C., in a quantity of 1 to 15% by weight with respect to the total weight of the fresh CO2 fed to the process, containing a passivating agent in such a quantity that its equivalent content of O2 in moles varies from 0.05% to 0.80% with respect to the moles of CO2 of said stream.
    • 描述了用于在高压和高温下从氨和二氧化碳合成脲的增强方法,其中形成氨基甲酸铵作为中间体,其包括高压合成段,其包括至少一个通过分解汽提的分离步骤 与未转化的氨基甲酸铵的氨在垂直装置(通常称为汽提器)中进行,其特征在于,所述步骤还包括在所述汽提器的下部中进料加热至温度范围的CO 2流 相对于进料至该方法的新鲜CO 2的总重量为130至230℃,其含量为1至15重量%,其含有其当量的O 2的摩尔数相当的量的钝化剂 相对于所述料流的CO 2的摩尔数为0.05%至0.80%。