CATALYST PROCESS MODIFICATION AND POLYMERIZATION THEREOF
    3.
    发明申请
    CATALYST PROCESS MODIFICATION AND POLYMERIZATION THEREOF 有权
    催化剂工艺改性及其聚合反应

    公开(公告)号:US20160215077A1

    公开(公告)日:2016-07-28

    申请号:US15007095

    申请日:2016-01-26

    Abstract: The present invention describes a process for preparation of catalyst component comprising contacting magnesium based precursor along with an internal donor based on phenylene dioates with an acyl halides in a solvent to obtain a solid precatalyst component; and contacting the solid precatalyst component with transition metal compound to obtain the catalyst component. The present invention also relates to a process for preparation of a catalyst system from said catalyst component and preparation of a polyolefins having free flowing characteristics with bulk densities (BD) of at least about 0.3 g/cc from the catalyst system.

    Abstract translation: 本发明描述了一种制备催化剂组分的方法,包括使镁基前体与基于二苯基二苯基酯的内部供体与酰基卤在溶剂中接触以获得固体预催化剂组分; 并使固体预催化剂组分与过渡金属化合物接触以获得催化剂组分。 本发明还涉及一种从所述催化剂组分制备催化剂体系的方法,以及制备具有从催化剂体系至少约0.3g / cc的体积密度(BD)的自由流动特性的聚烯烃。

    DEASPHALTING PROCESS FOR PRODUCTION OF FEEDSTOCKS FOR DUAL APPLICATIONS
    4.
    发明申请
    DEASPHALTING PROCESS FOR PRODUCTION OF FEEDSTOCKS FOR DUAL APPLICATIONS 有权
    用于双重应用生产饲料的去除工艺

    公开(公告)号:US20140238903A1

    公开(公告)日:2014-08-28

    申请号:US14347467

    申请日:2012-10-29

    Abstract: The invention concerns with improved and more flexible deasphalting process for production of lube oil base stock as well as feed stock for secondary processes depending on requirement from heavy residual hydrocarbon oil containing saturates, aromatics, resins and asphaltenes etc by contacting the oil with a solvent comprising of hydrocarbon containing two to six carbon atoms, preferably LPG having C3-C4 hydrocarbons and mixture thereof at predetermined deasphalting conditions wherein the yield of deasphalted oil including its quality is controlled by varying the deasphalting conditions including the operating temperature. The yield variations of 15 to 60 wt % is achieved by swinging the temperature by about 10-20° C. within the operative temperature range of 70-130° C. keeping the rest of the operating conditions including solvent to feed ratio same. The LPG solvent can be recovered using supercritical mode of operation using technology known in the art and recycled.

    Abstract translation: 本发明涉及用于生产润滑油基础原料的改进和更灵活的脱沥青方法,以及根据来自含有饱和烃,芳族化合物,树脂和沥青质等的重残余烃油的要求,通过使油与包含 的含有2至6个碳原子的烃,优选具有C 3 -C 4烃的LPG及其混合物在预定的脱沥青条件下,其中包括其质量的脱沥青油的产率通过改变包括操作温度在内的脱沥青条件来控制。 通过在70-130℃的操作温度范围内将温度摆动约10-20℃来实现15至60重量%的产率变化,保持其余的操作条件包括溶剂与进料比相同。 可以使用超临界操作模式使用本领域已知的技术回收LPG溶剂。

    Process for fluid catalytic cracking

    公开(公告)号:US10273417B2

    公开(公告)日:2019-04-30

    申请号:US15988909

    申请日:2018-05-24

    Abstract: An apparatus which is an integral hardware consisting of an annular downer reactor and a concentric upflow riser regenerator for catalytic cracking of hydrocarbon feed to is disclosed. The annular downer reactor terminates in annular stripper which is also concentric with the regenerator. The regenerator, reactor and stripper are in fluid connection with each other. The apparatus is highly compact and provides efficient contact between circulating catalyst and hydrocarbon feed. The proposed hardware includes a novel radial distributor for providing improved control and radial distribution of catalyst inside the downflow reactor. The radial distributor has equal numbers of stationary and movable parts placed one after another to cover the entire annular opening at the bottom of the regenerated catalyst vessel. The radial distributor is concentric with regenerator and located between the catalyst holding vessel and the reactor. A process for catalytic cracking using the invented apparatus is also disclosed.

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