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    Process for the production of low sulfur, low olefin gasoline
    1.
    发明授权
    Process for the production of low sulfur, low olefin gasoline 失效
    生产低硫，低烯烃汽油的方法

    公开(公告)号：US07431827B2

    公开(公告)日：2008-10-07

    申请号：US10974666

    申请日：2004-10-27

    申请人： Kerry L. Rock ,  Yi-Gang Xiong ,  Arvids Judzis, Jr.

    发明人： Kerry L. Rock ,  Yi-Gang Xiong ,  Arvids Judzis, Jr.

    IPC分类号： C10G45/02

    CPC分类号： C10G45/00 ,  C10G2400/02

    摘要： A process for the production of low sulfur, low olefin gasoline wherein a cracked naphtha, such as a full boiling range cracked naphtha, is first separated by fractional distillation into at least two fractions while simultaneously selectively hydrogenating the polyunsaturated compounds contained therein. The mono olefins in the light fraction are then subjected to etherification with alcohol to produce ethers or hydration with water to produce alcohols. The heavy fraction is subjected to sulfur removal by hydrodesulfurization or chemisorption. The two fractions are then combined to produce a low sulfur, low olefin gasoline.

    摘要翻译： 一种生产低硫低烯烃汽油的方法，其中裂解石脑油，例如全沸点裂化石脑油首先通过分馏分离成至少两个馏分，同时选择性地氢化其中所含的多不饱和化合物。 然后将轻馏分中的单烯烃与醇进行醚化，以产生醚或与水合成以产生醇。 重馏分通过加氢脱硫或化学吸附进行除硫。 然后将两个级分组合以产生低硫，低烯烃汽油。

    Reformate benzene reduction via alkylation
    2.
    发明授权
    Reformate benzene reduction via alkylation 有权
    通过烷基化改性苯还原

    公开(公告)号：US08101810B2

    公开(公告)日：2012-01-24

    申请号：US12195118

    申请日：2008-08-20

    申请人： Christopher C. Boyer ,  Lawrence A. Smith, Jr. ,  Arvids Judzis, Jr. ,  John R. Adams

    发明人： Christopher C. Boyer ,  Lawrence A. Smith, Jr. ,  Arvids Judzis, Jr. ,  John R. Adams

    IPC分类号： C07C2/52

    CPC分类号： C07C2/66 ,  Y02P20/127 ,  C07C15/085 ,  C07C15/02

    摘要： A process for reformate benzene reduction, the process including: feeding a light reformate fraction, an olefin feed, and an alkylation catalyst to an alkylation reaction zone; contacting the light reformate fraction and the olefin feed in the presence of the alkylation catalyst in the alkylation reaction zone to convert at least a portion of the benzene and the olefin to a monoalkylate; recovering a catalyst fraction from an alkylation reaction zone effluent; and recovering a light reformate product having a reduced benzene content.

    摘要翻译： 一种重整苯还原的方法，该方法包括：将轻质重整油馏分，烯烃进料和烷基化催化剂进料至烷基化反应区; 在烷基化反应区中在烷基化催化剂存在下使轻重整油馏分和烯烃进料接触，将至少一部分苯和烯烃转化成单烷基化物; 从烷基化反应区流出物回收催化剂级分; 并回收苯含量降低的轻质重整产物。

    Energy efficient method for exothermic reactions
    4.
    发明授权
    Energy efficient method for exothermic reactions 有权
    放热反应的节能方法

    公开(公告)号：US07320745B2

    公开(公告)日：2008-01-22

    申请号：US11038755

    申请日：2005-01-19

    申请人： Arvids Judzis, Jr. ,  Abraham P. Gelbein ,  John R. Adams ,  Christopher C. Boyer

    发明人： Arvids Judzis, Jr. ,  Abraham P. Gelbein ,  John R. Adams ,  Christopher C. Boyer

    IPC分类号： B01D3/14 ,  C10G7/00

    CPC分类号： B01D3/009 ,  B01J19/0033 ,  B01J2219/00006 ,  Y10S203/08 ,  Y10S585/914

    摘要： An energy efficient process scheme for a highly exothermic reaction-distillation system in which the reactor is external to the distillation column and the feed to the reactor is a mixture of at least one liquid product stream from the distillation column with or without other liquid/vapor reactants. The reactor is operated under adiabatic and boiling point conditions and at a pressure that results in vaporizing a portion of the liquid flow through the reactor due to the heat of reaction. Under these conditions, reaction temperature is controlled by reactor pressure. The pressure (and hence the temperature) is maintained at a sufficiently high level such that the reactor effluent can be efficiently used to provide reboil heat for the distillation column.

    摘要翻译： 用于高放热反应 - 蒸馏系统的能量效率方法，其中反应器在蒸馏塔外部和反应器的进料是来自蒸馏塔的至少一种液体产物流与有或没有其它液体/蒸气的混合物 反应物。 反应器在绝热和沸点条件下运行，并且在由于反应热导致部分液体流过反应器的压力下运行。 在这些条件下，反应温度由反应器压力控制。 压力（因此温度）保持在足够高的水平，使得反应器流出物可以有效地用于为蒸馏塔提供再沸腾热。