Modernization of a reactor
    2.
    发明授权
    Modernization of a reactor 失效
    反应堆的现代化

    公开(公告)号:US5756048A

    公开(公告)日:1998-05-26

    申请号:US375985

    申请日:1995-01-20

    Abstract: A method for in-situ modernization of a reactor for carrying out heterogeneous exothermic synthesis reactions, in particular of the so-called lozenge type including an external shell (2), calls for prearrangement within the shell (2) of a plurality of superimposed catalyst beds (12, 13, 14) supported at a pre-set distance by means of support elements (22, 23, 24) rested on or fixed to, e.g. by welding, a plurality of annular shoulders (8a, 8b, 8c) pre-existing in the reactor.

    Abstract translation: 用于进行异质放热合成反应的反应器的现场现代化方法,特别是包括外壳(2)的所谓的锭剂型的方法,需要在多个叠加催化剂的壳体(2)内进行预先布置 床(12,13,14)通过支撑元件(22,23,24)以预设的距离支撑,搁置在或固定到例如 通过焊接,预先存在于反应器中的多个环形肩部(8a,8b,8c)。

    Process for the modernization of existing urea plants and a modernized
urea plant
    3.
    发明授权
    Process for the modernization of existing urea plants and a modernized urea plant 失效
    现有的尿素植物和现代化尿素植物现代化的方法

    公开(公告)号:US5176800A

    公开(公告)日:1993-01-05

    申请号:US634410

    申请日:1990-12-27

    CPC classification number: C07C273/04 Y02P20/142

    Abstract: A process to modernize existing urea plants which use a stripping with carbon dioxide, and to increase urea yields and flexibility under overload conditions while at the same time reducing energy consumption, corrosion phenomena and possible risks of explosive mixtures. The plant includes: a passivation stage with the introduction of an oxidizing agent and reduction of the air fed to the system; a medium pressure distillation stage of the products leaving the stripping section, and a condensation of the products of the distillation, effected in a pre-evaporation phase to concentrate at low pressure the urea solution.The modernized plant, includes at the start at least a reactor, a scrubber, a condenser, a stripper and the evaporators, includes also a passivation section, a medium pressure distillation section, and a distillation section with double-effect technique.

    System for improve the mixing of reacted gases and quench gases in
heterogeneous synthesis reactors
    5.
    发明授权
    System for improve the mixing of reacted gases and quench gases in heterogeneous synthesis reactors 失效
    用于改善异质合成反应器中反应气体和骤冷气体混合的系统

    公开(公告)号:US4859425A

    公开(公告)日:1989-08-22

    申请号:US54743

    申请日:1987-05-27

    Applicant: Umberto Zardi

    Inventor: Umberto Zardi

    Abstract: The general conditions of the thermal exchange are improved by ameliorating the mixing of reacted gases together with quench gases, in order to increase in the yields and to reduce the energy consumption in reactors used for heterogeneous synthesis (ammonia, methanol, etc.), consisting of an external shell, of an internal cartridge with catalytic baskets lying one above the other, at least one of such baskets being traversed axially by the reaction gas, and of means to feed the quench gas between the bottom of one basket and the top of the following basket, said gas mixing being carried out in a peripheral zone near the internal cartridge wall.

    Abstract translation: 通过改善反应气体与骤冷气体的混合来提高热交换的一般条件,以增加产量并降低用于异相合成的反应器(氨,甲醇等)中的能量消耗,包括 具有一个位于一个上方的催化篮的内部盒体,至少一个这样的篮子被反应气体轴向地横过,并且在一个篮子的底部和顶部之间供给骤冷气体的装置 在下一个篮子中,所述气体混合在靠近内部筒壁的周边区域中进行。

    Method for the preparation of urea with a high-yield reactor
    6.
    发明授权
    Method for the preparation of urea with a high-yield reactor 失效
    用高产率反应器制备尿素的方法

    公开(公告)号:US4210600A

    公开(公告)日:1980-07-01

    申请号:US40863

    申请日:1979-05-21

    Applicant: Umberto Zardi

    Inventor: Umberto Zardi

    Abstract: In a total recycle urea-producing system, the improvement is disclosed which consists in providing in the reactor two adjoining but separated reaction spaces, called first and second reaction zones, the surface which separates the two zones being a heat-exchanging surface. Fresh ammonia and carbon dioxide are fed with a portion of excess recycled ammonia to the first reaction zone, wherein the reaction is exothermic in character, whereas the condensates from the carbamate decomposition and the remaining portion of the excess recycled ammonia are fed to the second reaction zone, wherein the reactions are of an endothermic nature. By so doing, a better thermal balance in the reactor is obtained, concurrently with improved yields.

    Abstract translation: 在总再生尿素生产系统中,公开了一种改进,其在反应器中提供称为第一和第二反应区的相邻但分离的反应空间,即分离作为热交换表面的两个区的表面。 将新鲜的氨和二氧化碳与一部分过量的再循环氨进料到第一反应区,其中反应具有放热特性,而来自氨基甲酸酯分解的冷凝物和剩余的部分过量的再循环氨进料到第二反应 区,其中反应具有吸热性质。 通过这样做,在反应器中获得更好的热平衡,同时提高了产率。

    Mixing assembly for gaseous flows at different temperatures, in particular for heterogeneous exothermic synthesis reactors
    8.
    发明授权
    Mixing assembly for gaseous flows at different temperatures, in particular for heterogeneous exothermic synthesis reactors 有权
    用于不同温度气体流的混合组件,特别是用于异相放热合成反应器

    公开(公告)号:US06290920B1

    公开(公告)日:2001-09-18

    申请号:US09315975

    申请日:1999-05-21

    Abstract: The present invention relates generally an apparatus for uniformly mixing gaseous flows at different temperatures. In particular, a preferred embodiment of the present invention relates to a heterogeneous exothermic synthesis reactor including a plurality of superimposed catalytic beds wherein at least one of the beds is provided with a gas permeable wall for outlet of a hot gas flow. In this embodiment, a baffle extends below and parallel to the gas permeable wall, thereby defining an air space to collect the hot gas flow. An annular opening is provided for outlet of the hot gas flow from the air space defined between the baffle and a side wall supporting the beds associated with the reactor and a perforated distributor for cooling a gas flow supported below said baffle at a predetermined distance from the annular opening. Further, the air space which collects the hot gas flow has a constant thickness in correspondence with the annular opening and the ratio of the width of the annular opening to the thickness of the air space is between 0.2 and 1.

    Abstract translation: 本发明一般涉及在不同温度下均匀混合气流的装置。 特别地,本发明的优选实施方案涉及一种异质放热合成反应器,其包括多个叠加的催化床,其中至少一个床设有用于热气流出口的气体渗透壁。 在该实施例中,挡板延伸到气体可渗透壁的下方并平行,由此限定空气空间以收集热气流。 设置环形开口用于来自限定在挡板和支撑与反应器相关联的床的侧壁之间的空气空间的出口,以及穿孔分配器,用于将支撑在所述挡板下方的气流以预定距离离开 环形开口。 此外,收集热气流的空气空间与环形开口相对应地具有恒定的厚度,并且环形开口的宽度与空气空间的厚度的比率在0.2和1之间。

    Process for urea production
    9.
    发明授权
    Process for urea production 失效
    尿素生产工艺

    公开(公告)号:US6150555A

    公开(公告)日:2000-11-21

    申请号:US405912

    申请日:1995-03-16

    CPC classification number: C07C273/04 Y02P20/142 Y02P20/582

    Abstract: An improved process for urea production as well as a method of retrofitting a pre-existing urea plant based on the Stamicarbon process are disclosed. According to the invention, a high yield reaction space fed by highly pure reagents (NH3 and CO2) and a separating section of the solution leaving the high yield reaction space are added to the pre-existing urea plant, means being provided for recirculating ammonia and carbammate solutions obtained in the separating section to the added high yield reaction space and to the pre-existing reactor respectively.

    Abstract translation: 公开了一种用于尿素生产的改进方法以及基于Stamicarbon方法改造预先存在的尿素装置的方法。 根据本发明,将高纯度试剂(NH 3和CO 2)供给的高产率反应空间和离开高产率反应空间的溶液的分离段加入到预先存在的尿素装置中,提供用于再循环氨和 在分离部分中获得的添加的高产率反应空间和先前存在的反应器的碳酸溶液。

    Process and plant for the production of urea with differentiated yield
reaction spaces
    10.
    发明授权
    Process and plant for the production of urea with differentiated yield reaction spaces 失效
    用于生产具有差异产量反应空间的尿素的工艺和设备

    公开(公告)号:US5380943A

    公开(公告)日:1995-01-10

    申请号:US947287

    申请日:1992-09-16

    CPC classification number: C07C273/04 Y02P20/582

    Abstract: Process for the industrial synthesis of urea, by reacting ammonia (NH.sub.3) and carbon dioxide (CO.sub.2) in at least one reaction space, at high pressures and temperatures and by recirculating at least part of the non-reacted products obtained in a recovery section, characterized by the fact that the following takes place : a synthesis reaction A) between highly pure reagents, and a synthesis reaction B) between less pure reagents, substantially recycled from the said recovery section, the reaction A) being either of adiabatic type A1) or with partial reaction heat removal A2).

    Abstract translation: 通过在高压和高温下使至少一个反应空间中的氨(NH 3)和二氧化碳(CO 2)反应并通过再循环至少部分在回收段中获得的未反应的产物来工业合成尿素的方法, 其特征在于发生以下事实:高纯试剂之间的合成反应A)和较不纯的试剂之间的合成反应B),基本上从所述回收部分再循环,反应A)为绝热型A1) 或部分反应除热A2)。

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