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    Hydroconversion process for petroleum resids by hydroconversion over carbon supported metal catalyst followed by selective membrane separation
    5.
    发明授权
    Hydroconversion process for petroleum resids by hydroconversion over carbon supported metal catalyst followed by selective membrane separation 有权
    通过在碳负载的金属催化剂上加氢转化，然后进行选择性膜分离，石油的加氢转化方法残留

    公开(公告)号：US07931798B2

    公开(公告)日：2011-04-26

    申请号：US12073843

    申请日：2008-03-11

    Applicant: Martin L. Gorbaty ,  David T. Ferrughelli ,  Edward W. Corcoran ,  Stephen M. Cundy ,  Andrew Kaldor

    Inventor： Martin L. Gorbaty ,  David T. Ferrughelli ,  Edward W. Corcoran ,  Stephen M. Cundy ,  Andrew Kaldor

    IPC: C10G47/02 ,  C07C7/144

    CPC classification number: C10G47/12 ,  C10G2300/107

    Abstract: A heavy residual petroleum feed boiling above 650° F.+ (345° C.+) is subjected to hydroconversion at elevated temperature in the presence of hydrogen at a hydrogen pressure not normally higher than 500 psig (3500 kPag) using a dispersed metal-on-carbon catalyst to produce a hydroconverted effluent which is fractionated to form a low boiling fraction and a relatively higher boiling fraction which is subjected to membrane separation to produce a permeate which is low in metals and Microcarbon Residue (MCR) as well as a retentate, containing most of the MCR and metals. The process has the advantage that the hydroconversion may be carried out in low pressure equipment with a low hydrogen consumption as saturation of aromatics is reduced.

    Abstract translation: 在氢气存在下，在通常不高于500psig（3500kPag）的氢气压力下，在高温下在高于650°F +（345℃+）下沸腾的重残余石油原料进行加氢转化， 碳酸催化剂以产生加氢转化的流出物，其被分馏以形成低沸点馏分和相对较高沸点馏分，其进行膜分离以产生低金属和微碳残余物（MCR）的渗透物以及滞留物 ，含有大部分MCR和金属。 该方法的优点是可以在具有低氢消耗的低压设备中进行加氢转化，从而降低芳族化合物的饱和度。

    Hydroconversion process for petroleum resids using selective membrane separation followed by hydroconversion over carbon supported metal catalyst
    6.
    发明申请
    Hydroconversion process for petroleum resids using selective membrane separation followed by hydroconversion over carbon supported metal catalyst 有权
    使用选择性膜分离，然后在碳负载金属催化剂上加氢转化，石油渣的加氢转化法

    公开(公告)号：US20090230022A1

    公开(公告)日：2009-09-17

    申请号：US12073844

    申请日：2008-03-11

    Applicant: Martin L. Gorbaty ,  David T. Ferrughelli ,  Edward W. Corcoran ,  Stephen M. Cundy

    Inventor： Martin L. Gorbaty ,  David T. Ferrughelli ,  Edward W. Corcoran ,  Stephen M. Cundy

    IPC: C10G47/02

    CPC classification number: C10G67/02 ,  C10G65/14 ,  C10G69/14

    Abstract: A heavy residual petroleum feed boiling above 650° F.+ (345° C.+) is subjected to membrane separation to produce a produce a permeate which is low in metals and Microcarbon Residue (MCR) as well as a retentate, containing most of the MCR and metals, the retentate is then subjected to hydroconversion at elevated temperature in the presence of hydrogen at a hydrogen pressure not higher than 500 psig (3500 kPag) using a dispersed metal-on-carbon catalyst to produce a hydroconverted effluent which is fractionated to give naphtha, distillate and gas oil fractions. The permeate from the membrane separation may be used as FCC feed either as such or with moderate hydrotreatment to remove residual heteroatoms. The process has the advantage that the hydroconversion may be carried out in low pressure equipment with a low hydrogen consumption as saturation of aromatics is reduced.

    Abstract translation: 将高于650°F +（345°C +）沸腾的重残余石油原料进行膜分离以产生低金属和微量残渣（MCR）的渗透物以及含有大部分 MCR和金属，然后使用分散的金属对碳催化剂在氢气压力不高于500psig（3500kPag）的氢气存在下，在升高的温度下对渗余物进行加氢转化，以产生分级的加氢转化的流出物 得到石脑油，馏出物和瓦斯油馏分。 来自膜分离的渗透物可以如本文使用或作为FCC进料或中等加氢处理以除去残留的杂原子。 该方法的优点是可以在具有低氢消耗的低压设备中进行加氢转化，从而降低芳族化合物的饱和度。

    Process for flexible vacuum gas oil conversion
    10.
    发明授权
    Process for flexible vacuum gas oil conversion 有权
    柔性真空瓦斯油转化工艺

    公开(公告)号：US08163168B2

    公开(公告)日：2012-04-24

    申请号：US12459729

    申请日：2009-07-07

    Applicant: Martin L. Gorbaty ,  Bruce R. Cook ,  David T. Ferrughelli ,  Jason B. English ,  Steven S. Lowenthal

    Inventor： Martin L. Gorbaty ,  Bruce R. Cook ,  David T. Ferrughelli ,  Jason B. English ,  Steven S. Lowenthal

    IPC: C10G69/04

    CPC classification number: C10G69/06 ,  C10G11/18 ,  C10G51/04 ,  C10G69/02 ,  C10G69/04 ,  C10G2300/1074 ,  C10G2300/4081 ,  C10G2400/02

    Abstract: The present invention relates to a process for the selective conversion of hydrocarbon feed having a Conradson Carbon Residue content of 0 to 6 wt %, based on the hydrocarbon feed. The hydrocarbon feed is treated in a two-step process. The first is thermal conversion and the second is catalytic cracking of the products of the thermal conversion. The present invention results in a process for increasing the distillate production from a hydrocarbon feedstream for a fluid catalytic cracking unit. The resulting product slate from the present invention can be further varied by changing the conditions in the thermal and catalytic cracking steps as well as by changing the catalyst in the cracking step.

    Abstract translation: 本发明涉及一种基于烃进料选择性转化具有0至6重量％的康拉德森碳残余物的烃进料的方法。 烃进料以两步法处理。 第一种是热转化，第二种是热转化产物的催化裂化。 本发明导致用于增加用于流化催化裂化装置的烃进料流的馏出物生产的方法。 通过改变热和催化裂化步骤的条件以及通过改变裂化步骤中的催化剂，可进一步改变本发明产生的产品板条。

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