会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 2. 发明授权
    • Commercial Fischer-Tropsch reactor
    • 商业费 - 托反应堆
    • US09416320B2
    • 2016-08-16
    • US14852248
    • 2015-09-11
    • RES USA, LLC
    • Mark IbsenSergio MohedasFrank HogsettMark BohnHarold A. Wright
    • C07C27/00C10G2/00B01J8/22B01J8/00B03C1/28B03C1/30C10G45/00C10G45/58C10G47/00
    • B03C1/02B01J8/005B01J8/007B01J8/22B01J8/228B01J35/0033B03C1/288B03C1/30B03C2201/18C10G2/33C10G2/332C10G2/342C10G45/00C10G45/58C10G47/00
    • A method for converting synthesis gas into liquid hydrocarbons by introducing a synthesis gas feed into a Fischer-Tropsch system that includes a catalytic reactor fluidly connected with at least two slurry loops, the reactor comprising at least as many reactor product outlets and slurry return inlets as slurry loops; each slurry loop comprising a separation system comprising at least one separator, an inlet of each separator fluidly connected to a reactor product outlet via a slurry offtake, and an outlet of each separator fluidly connected to a slurry return inlet via a slurry return; separating concentrated catalyst slurry from the reaction product via the slurry loops; removing liquid hydrocarbon product from each separator; and returning concentrated catalyst slurry to the catalytic reactor via the slurry returns and slurry return inlets. A system for converting synthesis gas into liquid hydrocarbons via the method is also disclosed.
    • 通过将合成气进料引入费 - 托系统中来将合成气转化成液体烃的方法,所述费 - 托系统包括与至少两个浆液回路流体连接的催化反应器,所述反应器至少包含反应器产物出口和浆料返回入口 浆液回路; 每个浆料回路包括分离系统,该分离系统包括至少一个分离器,每个分离器的入口经由浆料出口流体连接到反应器产物出口,以及每个分离器的出口通过浆料回流器流体连接到浆料返回入口; 通过浆料循环从反应产物中分离浓缩的催化剂浆料; 从每个分离器去除液体烃产物; 并通过浆料返回和浆料返回入口将浓缩的催化剂浆料返回到催化反应器。 还公开了一种通过该方法将合成气转化为液态烃的系统。
    • 3. 发明授权
    • Acetic anhydride production by way of carbonylation with enhanced reaction and flashing
    • 通过羰基化反应生成乙酸酐,反应和闪烁
    • US08455685B2
    • 2013-06-04
    • US12924429
    • 2010-09-27
    • Mark O. Scates
    • Mark O. Scates
    • C07C51/12
    • B01J8/382B01J8/007B01J8/20B01J2208/00283B01J2219/00006B01J2219/0004C07C51/12C07C51/54C07C53/08C07C53/12
    • A method of making acetic anhydride or a mixture of acetic anhydride and acetic acid comprising: (a) catalytically reacting a feedstock containing methyl acetate and/or dimethyl ether with carbon monoxide in the presence of a homogeneous rhodium catalyst and methyl iodide in a reactor vessel which contains a substantially anhydrous liquid reaction mixture including acetic acid, acetic anhydride, methyl acetate and/or dimethyl ether, methyl iodide and the homogeneous catalyst, the reactor vessel being operated at a reactor pressure; (b) withdrawing reaction mixture from the reaction vessel and feeding the withdrawn reaction mixture along with additional carbon monoxide to a pre-flasher/post reactor vessel operated at a reduced pressure below the reactor vessel pressure; (c) venting light ends in the pre-flasher vessel and concurrently consuming methyl acetate and/or dimethyl ether in the pre-flasher/post reactor vessel to produce a pre-flash mixture which is enriched in acetic anhydride and diminished in methyl iodide and methyl acetate and/or dimethyl ether as compared with the reaction mixture; (d) withdrawing the pre-flash reaction mixture from the pre-flasher/post reactor vessel and feeding the pre-flash mixture to a flash vessel; and (e) flashing a crude product stream from the mixture in a flash vessel operated at a pressure substantially below the pressure of the pre-flasher/post reactor vessel.
    • 一种制备乙酸酐或乙酸酐和乙酸的混合物的方法,包括:(a)在均匀的铑催化剂和甲基碘存在下在反应器容器中催化反应含有乙酸甲酯和/或二甲醚的原料与一氧化碳 其包含基本上无水的液体反应混合物,包括乙酸,乙酸酐,乙酸甲酯和/或二甲醚,甲基碘和均相催化剂,反应器容器在反应器压力下操作; (b)从反应容器中取出反应混合物,并将排出的反应混合物与另外的一氧化碳一起送入反应器/反应器前的反应器容器中,该反应器容器在低于反应器容器压力的压力下操作; (c)在预闪蒸器容器内放出轻质的末端,同时在预闪蒸发器/反应器容器中消耗乙酸甲酯和/或二甲醚,以产生富含乙酸酐并在甲基碘中减少的预闪蒸混合物, 与反应混合物相比,乙酸甲酯和/或二甲醚; (d)将预闪蒸反应混合物从预闪蒸发器/反应堆容器中取出并将预闪蒸混合物送入闪蒸容器; 和(e)在以基本上低于预闪蒸发器/反应器反应器容器的压力的压力下操作的闪蒸容器中从混合物中闪蒸粗产物流。
    • 9. 发明申请
    • Loop Reactor Suitable for Olefin Polymerization with Improved Product Removal Means
    • 循环反应器适用于具有改进的产品去除手段的烯烃聚合
    • US20110124828A1
    • 2011-05-26
    • US12675005
    • 2008-08-29
    • Louis Fouarge
    • Louis Fouarge
    • C08F2/01B01J19/00
    • B01J19/1837B01J8/0055B01J8/007B01J19/1818B01J2219/0004B01J2219/00094B01J2219/00162B01J2219/00184B01J2219/00247C08F10/00Y10S526/918Y10S526/92C08F2/001C08F2/14
    • The present invention relates to a loop reactor suitable for olefin polymerization process comprising: a plurality of interconnected pipes defining a flow path for a polymer slurry, said slurry consisting essentially of an olefin reactant, a polymerization catalyst, liquid diluent and solid olefin polymer particles, means for introducing olefin reactant, polymerization catalyst and diluent into said reactor, a pump suitable for maintaining the polymer slurry in circulation in said reactor, and single settling leg connected to said loop reactor through (a) a take off line extending from said reactor to said settling leg and configured to remove said polymer slurry from said reactor, and (b) a return line extending from said settling leg to said reactor, characterized in that said take off line is radially connected to said single settling leg.
    • 本发明涉及一种适用于烯烃聚合方法的环流反应器,包括:多个互连的管,其限定聚合物浆料的流动路径,所述淤浆基本上由烯烃反应物,聚合催化剂,液体稀释剂和固体烯烃聚合物颗粒组成, 用于将烯烃反应物,聚合催化剂和稀释剂引入所述​​反应器的装置,适合于将所述聚合物浆料保持在所述反应器中循环的泵,以及通过(a)从所述反应器延伸到所述反应器的脱水管连接到所述环管反应器的单个沉降腿 所述沉降腿并且构造成从所述反应器中除去所述聚合物浆料,和(b)从所述沉降腿延伸到所述反应器的返回管线,其特征在于,所述脱出线径向连接到所述单个沉降腿。
    • 10. 发明申请
    • SYNTHESIS REACTION SYSTEM
    • 合成反应体系
    • US20100239474A1
    • 2010-09-23
    • US12733784
    • 2008-09-26
    • Yasuhiro Onishi
    • Yasuhiro Onishi
    • B01J10/00
    • C10G2/32B01J8/007B01J8/1818B01J8/226B01J8/228B01J2208/00132B01J2208/003
    • There is provided a synthesis reaction system which synthesizes a hydrocarbon compound by a chemical reaction of a synthesis gas including hydrogen and carbon monoxide as main components, and a slurry having solid catalyst particles suspended in liquid and which extracts the hydrocarbon compound from the slurry. The synthesis reaction system includes a reactor main body which accommodates the slurry, a separator which separates the hydrocarbon compound included in the slurry from the slurry, a first flow passage which allows the slurry including the hydrocarbon compound to flow to the separator from the reactor main body, a second flow passage which allows the slurry to flow to the reactor main body from the separator, and a fluid supply nozzle which supplies a fluid toward at least any one of the separator, the first flow passage, and the second flow passage.
    • 提供了通过包含氢和一氧化碳作为主要成分的合成气的化学反应合成烃化合物的合成反应体系,以及悬浮在液体中的固体催化剂颗粒的浆料,并从浆料中提取烃化合物。 合成反应系统包括容纳浆料的反应器主体,将浆料中包含的烃化合物与浆料分离的分离器,允许包含烃化合物的浆料从反应器主体流到分离器的第一流动通道 主体,允许浆料从分离器流向反应器主体的第二流动通道,以及朝向分离器,第一流动通道和第二流动通道中的至少任一个提供流体的流体供应喷嘴。