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35 条记录 (耗时 0.026 秒)

    Process for flexible vacuum gas oil conversion
    3.
    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

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

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

    IPC分类号： C10G69/04

    CPC分类号： C10G69/06 ,  C10G11/18 ,  C10G51/04 ,  C10G69/02 ,  C10G69/04 ,  C10G2300/1074 ,  C10G2300/4081 ,  C10G2400/02

    摘要： 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.

    摘要翻译： 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。

    Process for flexible vacuum gas oil conversion
    4.
    发明申请
    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：US20100018895A1

    公开(公告)日：2010-01-28

    申请号：US12459729

    申请日：2009-07-07

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

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

    IPC分类号： C10G69/04 ,  C10G47/00

    CPC分类号： C10G69/06 ,  C10G11/18 ,  C10G51/04 ,  C10G69/02 ,  C10G69/04 ,  C10G2300/1074 ,  C10G2300/4081 ,  C10G2400/02

    摘要： 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.

    摘要翻译： 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。

    Delayed coking process
    5.
    发明授权
    Delayed coking process 失效
    延迟焦化工艺

    公开(公告)号：US08147676B2

    公开(公告)日：2012-04-03

    申请号：US11256728

    申请日：2005-10-21

    申请人： Michael Siskin ,  David T. Ferrughelli ,  Martin L. Gorbaty ,  Simon R. Kelemen ,  Leo D. Brown

    发明人： Michael Siskin ,  David T. Ferrughelli ,  Martin L. Gorbaty ,  Simon R. Kelemen ,  Leo D. Brown

    IPC分类号： C10B55/00

    CPC分类号： C10B57/06 ,  C10B55/00 ,  C10B57/08 ,  C10G9/005 ,  C10G55/04 ,  C10G2300/107 ,  C10G2300/1077 ,  C10G2300/202 ,  C10G2300/206

    摘要： The present invention relates to an improved delayed coking process. A coker feed, such as a vacuum resid, is treated with (i) a metal-containing agent and (ii) an oxidizing agent. The feed is treated with the oxidizing agent at an oxidizing temperature. The oxidized feed is then pre-heated to coking temperatures and conducted to a coking vessel for a coking time to allow volatiles to evolve and to produce a substantially free-flowing coke. A metals-containing composition is added to the feed at at least one of the following points in the process: prior to the heating of the feed to coking temperatures, during such heating, and/or after such heating.

    摘要翻译： 本发明涉及一种改进的延迟焦化方法。 用（i）含金属试剂和（ii）氧化剂处理焦化饲料如真空渣油。 在氧化温度下用氧化剂处理进料。 然后将氧化的进料预加热至焦化温度，并导入焦化容器中以获得焦化时间，以允许挥发物放出并产生基本上自由流动的焦炭。 在此过程中，将进料加热至焦化温度，在此加热期间和/或在此类加热之后，将含金属的组合物加入到进料中的至少一个方面。

    Heavy oil upgrading process (LAW813)
    7.
    发明授权
    Heavy oil upgrading process (LAW813) 有权
    重油改造工艺（LAW813）

    公开(公告)号：US06171471B2

    公开(公告)日：2001-01-09

    申请号：US09302622

    申请日：1999-04-30

    申请人： David T. Ferrughelli ,  Martin L. Gorbaty

    发明人： David T. Ferrughelli ,  Martin L. Gorbaty

    IPC分类号： C10G6704

    CPC分类号： C10G67/0463

    摘要： The present invention is a slurry-type process for upgrading heavy oils to FCC and S/C feeds under temperature and pressure conditions similar to MSHP, but employing catalysts in concentrations small enough (e.g.,

    摘要翻译： 本发明是一种用于在与MSHP类似的温度和压力条件下将重油改质为FCC和S / C进料的浆料型方法，但是使用浓度足够小的催化剂（例如，进料上的<300ppm Mo），它们不需要 被回收。

    Hydroconversion process for petroleum resids by hydroconversion over carbon supported metal catalyst followed by selective membrane separation
    10.
    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

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

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

    IPC分类号： C10G47/02 ,  C07C7/144

    CPC分类号： C10G47/12 ,  C10G2300/107

    摘要： 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.

    摘要翻译： 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。