中科微点-全球专利检索

  1. Login
  2. Sign Up

Search Results

65 records (took 0.015 seconds)

    PYROLYSIS GASOLINE TREATMENT PROCESS
    2.
    发明公开
    PYROLYSIS GASOLINE TREATMENT PROCESS 审中-公开
    PYROLYSEBENZIN-BEHANDLUNGSVERFAHREN

    公开(公告)号：EP3060627A4

    公开(公告)日：2017-05-31

    申请号：EP14856399

    申请日：2014-10-08

    Applicant: UOP LLC

    Inventor： SCHMIDT ROBERT J ,  LUEBKE CHARLES P ,  JANULIS ROSE M

    IPC: C10G9/00

    CPC classification number: C07C5/05 ,  C10G7/00 ,  C10G45/02 ,  C10G45/22 ,  C10G45/38 ,  C10G45/40 ,  C10G65/06 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2400/02 ,  C10G2400/22 ,  C10G2400/30

    Abstract: A process for treating pyrolysis gasoline that includes providing a first stage di-olefin reactor that includes a first bed and a second bed and introducing a pyrolysis gasoline stream to the first bed of the first stage di-olefin reactor. The process also preferably includes providing interstage cooling to the pyrolysis gasoline stream between the first and second beds of the first stage di-olefin reactor and routing the cooled pyrolysis gasoline stream through the second bed of the first stage di-olefin reactor. Finally, embodiments of the process also preferably involve routing at least a portion of an effluent stream from the second bed of the first stage di-olefin reactor to a location upstream of the first bed of the first stage di-olefin reactor, such that the effluent stream is configured to be combined with the pyrolysis gasoline stream.

    Abstract translation: 一种处理裂解汽油的方法，其包括提供包含第一床和第二床的第一阶段二烯烃反应器，并将裂解汽油物流引入第一阶段二烯烃反应器的第一床。 该方法还优选包括对第一级二烯烃反应器的第一和第二床之间的裂解汽油流提供级间冷却，并将冷却的裂解汽油流引导通过第一级二烯烃反应器的第二床。 最后，该方法的实施方式还优选涉及将来自第一阶段二烯烃反应器的第二床的流出物流的至少一部分引导至第一阶段二烯烃反应器的第一床的上游位置，使得 流出物流被配置为与裂解汽油流结合。

    GASOLINE DESULFURIZATION PROCESS
    7.
    发明公开
    GASOLINE DESULFURIZATION PROCESS 失效
    工艺脱硫汽油的

    公开(公告)号：EP0854901A4

    公开(公告)日：1999-07-14

    申请号：EP96924474

    申请日：1996-07-12

    Applicant: CHEMICAL RES & LICENSIN

    Inventor： HEARN DENNIS ,  HICKEY THOMAS P

    IPC: C10G65/04 ,  C10G35/06 ,  C10G45/06 ,  C10G45/08 ,  C10G45/10 ,  C10G45/32 ,  C10G65/06 ,  C10G45/00

    CPC classification number: C10G65/06 ,  C10G2300/4087 ,  C10G2400/02 ,  Y02P20/127

    Abstract: A catalytic cracked naphtha is desulfurized with minimum loss of olefins and octane. The naphtha is fed to a first distillation column reactor (10) which acts as a depentanizer or dehexanizer with the lighter material containing most of the olefins and mercaptans being boiled up into a first distillation reaction zone (11) where the mercaptans are reacted with diolefins to form sulfides which are removed in the bottoms along with any higher boiling sulfur compounds. The bottoms are subjected to hydrodesulfurization in a second distillation column reactor (20) where the sulfur compounds are converted to H2S and removed. The lighter fraction containing most of the olefins is thus not subjected to the more harsh hydrogenation conditions of the second reactor (20).

    Verfahren zur Aufbereitung von Rohbenzol
    8.
    发明公开
    Verfahren zur Aufbereitung von Rohbenzol 失效
    Verfahren zur Aufbereitung von Rohbenzol。

    公开(公告)号：EP0582723A1

    公开(公告)日：1994-02-16

    申请号：EP92113272.6

    申请日：1992-08-04

    Applicant: NEUMANN + STALLHERM GmbH ,  RUHR OEL GmbH

    Inventor： Klein, Wolfdieter ,  Flügge, Helmut ,  Laege, Jürgen Dr.

    IPC: C10G65/00 ,  C10G65/06

    CPC classification number: C10G65/06 ,  C10G65/00

    Abstract: Verfahren zur Aufbereitung von Rohbenzol (1), das bei der Verkokung kohlenstoffhaltiger Materialien, insbesondere von Kohle, anfällt, mittels katalytischer Vor- und Haupthydrierung unter Druck bei erhöhten Temperaturen in Gegenwart von Wasserstoff, bei dem das Rohbenzol einer Destillation unter Vakuum (2) bei Temperaturen von

    Abstract translation: 通过催化预氢化和在氢气存在下在升高的温度下在压力下主要氢化的含碳原料，特别是煤的焦化过程中产生的粗苯（1）的改质方法，其中粗苯为 在<100℃的温度下真空蒸馏（2），分离成含有苯和含有苯乙烯的级分（4）的级分（3），将含有苯的馏分进行主要氢化（8），馏分 （15）在不高于280℃的温度下进行预氢化，形成含有芳族化合物的初始产物，将含有苯乙烯的馏分加热到在热循环中发生的氢化温度（14） 与预水合产物，并且含有芳族化合物的初始产物随后进行主要氢化（20）。

    Two step process for selectively isomerizing olefins in gasoline streams
    9.
    发明公开
    Two step process for selectively isomerizing olefins in gasoline streams 失效
    Zweistufenprozess zur selektiven Isomerisierung von Olefinen在Benzinströmen。

    公开(公告)号：EP0537372A1

    公开(公告)日：1993-04-21

    申请号：EP91117002.5

    申请日：1991-10-05

    Applicant: UOP

    Inventor： Gajda, Gregory Joseph

    IPC: C10G65/06 ,  C10G69/08 ,  C07C11/02

    CPC classification number: C10G65/06 ,  C10G61/02 ,  C10G69/08

    Abstract: Olefins in a gasoline boiling range feed stream also containing highly unsaturated hydrocarbons are selectively isomerized by a two step process involving treating the feed stream to reduce the content of highly unsaturated hydrocarbons to form a stable olefinic stream and thereafter contacting the stabilized olefinic stream with an isomerization catalyst containing at least one medium pore molecular sieve at olefin isomerization conditions effective to produce an isomerized product stream having a ratio of branched to unbranched olefins of at least 2:1. The process features yields of C₅+ isomerized product and avoids conversion of highly branched paraffins to equilibrium values.

    Abstract translation: 还含有高度不饱和烃的汽油沸程进料流中的烯烃通过两步法选择性异构化，该方法涉及处理进料流以降低高度不饱和烃的含量以形成稳定的烯烃流，然后使稳定的烯烃流与异构化 在烯烃异构化条件下含有至少一种中孔分子筛的催化剂有效地产生具有至少2:1的支链至无支链烯烃的比例的异构化产物流。 该方法具有C psi +异构化产物的产率，并避免高支化链烷烃转化为平衡值。

Patent Agency Ranking