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    • 3. 发明申请
    • METHOD AND SYSTEM FOR THE INTEGRATED PRODUCTION OF UREA AND MELAMINE
    • 综合生产尿素和梅毒的方法和系统
    • WO2016171562A1
    • 2016-10-27
    • PCT/NL2016/050291
    • 2016-04-25
    • STAMICARBON B.V.
    • MENNEN, Johannes Henricus
    • C07C273/12
    • C07C273/12B01J19/245B01J2219/00024B01J2219/24C07D251/60Y02P20/125
    • Disclosed is an integrated process for the production of urea and melamine, as well as a system for carrying out the process. The invention thereby pertains to an integrated process of the type wherein off-gas obtained from the production of melamine is entered into the process for the production of melamine, by condensation in the presence of water. A typical embodiment thereof is the condensation in the presence of an aqueous carbamate solution obtained from urea recovery. In accordance with the invention, said condensation takes place at a substantially lower pressure than the pressure at which the melamine off-gas is obtained. To this end, the pressure of the off-gas is reduced typically by 2-10 bar. In connection herewith, the system of the invention comprises a pressure reducing unit downstream of an outlet for the melamine off-gas, and upstream of a section for the condensation of the off-gas. The invention also includes a method for the modernization of an integrated system for the production of melamine and urea. This is accomplished by adding the aforementioned pressure reducing unit to a pre-existing system.
    • 公开了用于生产尿素和三聚氰胺的综合方法,以及用于进行该方法的系统。 因此,本发明涉及一种其中由三聚氰胺生产得到的废气通过在水存在下的冷凝进入生产三聚氰胺的方法的综合方法。 其典型的实施方案是在由尿素回收获得的氨基甲酸铵水溶液存在下进行缩合。 根据本发明,所述冷凝以比获得三聚氰胺废气的压力低得多的压力进行。 为此,废气的压力通常降低2-10巴。 与此相关的是,本发明的系统包括用于三聚氰胺废气的出口下游的减压单元,以及用于废气冷凝的部分的上游。 本发明还包括一种用于生产三聚氰胺和尿素的综合系统现代化的方法。 这是通过将上述减压单元添加到预先存在的系统来实现的。
    • 10. 发明申请
    • A UREA STRIPPING PROCESS FOR THE PRODUCTION OF UREA
    • 用于生产尿素的尿素剥离方法
    • WO2011084060A1
    • 2011-07-14
    • PCT/NL2011/050012
    • 2011-01-07
    • STAMICARBON B.V.MENNEN, Johannes Henricus
    • MENNEN, Johannes Henricus
    • C07C273/04
    • C07C273/04
    • The invention relates to a process for producing urea wherein an aqueous urea solution, leaving a urea reaction zone is fed to a stripper, where a part of the non-converted ammonia and carbon dioxide is separated from the aqueous urea solution, which solution leaves the stripper to a first recovery section of one or more serial recovery sections and is subsequently fed to one or more urea concentration sections, wherein the urea solution leaving the stripper is subjected to an adiabatic expansion, thus creating a vapor and a liquid, which are separated before the liquid enters a first recovery section and the vapor is condensed. The invention further relates to a urea plant comprising a stripper and a first recovery section, wherein an adiabatic expansion valve and a liquid/gas separator is provided between the stripper and the first recovery section.
    • 本发明涉及生产尿素的方法,其中留下尿素反应区的尿素水溶液被供给到汽提器,其中一部分未转化的氨和二氧化碳与尿素水溶液分离,该溶液离开 汽提器连接到一个或多个连续回收部分的第一回收部分,并且随后被供给到一个或多个尿素浓缩部分,其中离开汽提器的尿素溶液经受绝热膨胀,从而产生蒸气和液体,其被分离 在液体进入第一回收部分并且蒸气冷凝之前。 本发明还涉及一种包括汽提器和第一回收部分的尿素设备,其中绝热膨胀阀和液/气分离器设置在汽提器和第一回收部分之间。