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    PROCESS FOR THE HYDROCONVERSION OF HEAVY OILS
    91.
    发明申请
    PROCESS FOR THE HYDROCONVERSION OF HEAVY OILS 审中-公开
    重油加氢过程

    公开(公告)号：US20150184087A1

    公开(公告)日：2015-07-02

    申请号：US14584514

    申请日：2014-12-29

    申请人： Luigi PATRON ,  Alberto MALANDRINO ,  Mario MOLINARI

    发明人： Luigi PATRON ,  Alberto MALANDRINO ,  Mario MOLINARI

    IPC分类号： C10G65/00

    CPC分类号： C10G65/00 ,  C10G47/02 ,  C10G47/26 ,  C10G49/04 ,  C10G2300/1003 ,  C10G2300/1014 ,  C10G2300/1033 ,  C10G2300/107 ,  C10G2300/1077 ,  C10G2300/207 ,  Y02P30/20

    摘要： A process for the conversion of heavy oils comprising sending the heavy oil to hydrotreatment, of the high severity type, in the presence of high concentrations of a suitable hydrogenation catalyst dispersed in slurry phase, effected in a suitable solid accumulation reactor capable of operating stably in the presence of solids deriving from and generated by the feedstock charged, wherein the hydrogen or mixtures thereof is fed at suitable flow-rates and suitably distributed, obtaining the conversion products in vapour phase directly in the reactor.

    摘要翻译： 一种重油转化方法，包括在高浓度的分散在淤浆相中的合适的氢化催化剂存在下将重油送入高浓度类型的加氢处理剂，该合适的固体积聚反应器能够稳定地运行 由所加入的原料产生的固体的存在，其中氢气或其混合物以合适的流速进料并适当分布，直接在反应器中获得汽相转化产物。

    INTEGRATED HYDROCRACKING AND SLURRY HYDROCONVERSION OF HEAVY OILS
    92.
    发明申请
    INTEGRATED HYDROCRACKING AND SLURRY HYDROCONVERSION OF HEAVY OILS 有权
    重油加氢和浆液重油的重油

    公开(公告)号：US20150014217A1

    公开(公告)日：2015-01-15

    申请号：US14308893

    申请日：2014-06-19

    申请人： Randolph J. Smiley ,  Ajit Bhaskar Dandekar ,  Ramanathan Sundararaman ,  Rustom Merwan Billimoria ,  Thomas Francis Degnan, JR.

    发明人： Randolph J. Smiley ,  Ajit Bhaskar Dandekar ,  Ramanathan Sundararaman ,  Rustom Merwan Billimoria ,  Thomas Francis Degnan, JR.

    IPC分类号： C10G65/12

    CPC分类号： C10G65/12 ,  C10G45/16 ,  C10G47/26 ,  C10G49/12

    摘要： Improved yields of fuels and/or lubricants from a resid or other heavy oil feed can be achieved using slurry hydroconversion to convert at least about 90 wt % of the feed. The converted portion of the feed can then be passed into one or more hydroprocessing stages. An initial processing stage can be a hydrotreatment stage for additional removal of contaminants and for passivation of high activity functional groups that may be created during slurry hydroconversion. The hydrotreatment effluent can then be fractionated to separate naphtha boiling range fractions from distillate fuel boiling range fractions and lubricant boiling range fractions. At least the lubricant boiling range fraction can then be hydrocracked to improve the viscosity properties. The hydrocracking effluent can also be dewaxed to improve the cold flow properties. The hydrocracked and/or dewaxed product can then be optionally hydrofinished.

    摘要翻译： 可以使用浆料加氢转化来转化至少约90重量％的进料，从渣油或其他重油进料中提高燃料和/或润滑剂的产率。 然后将进料的转化部分进入一个或多个加氢处理阶段。 初始处理阶段可以是加氢处理阶段，用于额外去除污染物和钝化可能在浆料加氢转化过程中产生的高活性官能团。 然后可以将加氢处理流出物进行分馏，从馏出燃料沸点馏分和润滑剂沸程馏分中分离出石脑油沸程。 至少可以将润滑剂沸程级分进行加氢裂化以提高粘度特性。 加氢裂化流出物也可以脱蜡以改善冷流特性。 加氢裂化和/或脱蜡产物可以任选加氢处理。

    PROCESS FOR CONVERTING A BIOMASS MATERIAL
    93.
    发明申请
    PROCESS FOR CONVERTING A BIOMASS MATERIAL 审中-公开
    转化生物质材料的方法

    公开(公告)号：US20140330057A1

    公开(公告)日：2014-11-06

    申请号：US14265411

    申请日：2014-04-30

    申请人： SHELL OIL COMPANY

    发明人： Ivo Johannes DIJS ,  Arjen NIEUWHOF ,  Johannes Pieter HAAN ,  Josiane Marie-Rose GINESTRA ,  Jozef Jacobus Titus SMITS ,  Colin John SCHAVERIEN ,  Leticia ESPINOSA ALONSO ,  Wouter SPIERING

    IPC分类号： C10G1/04

    CPC分类号： C10G1/045 ,  C10B53/02 ,  C10G33/00 ,  C10G47/00 ,  C10G47/24 ,  C10G47/26 ,  C10G47/28 ,  C10L1/02 ,  Y02E50/14

    摘要： A process for converting a biomass material comprising a) pyrolyzing a biomass material to produce a biomass-derived pyrolysis product; b) mixing at least part of the biomass-derived pyrolysis product and a petroleum-derived hydrocarbon composition, which petroleum derived hydrocarbon composition has a C7-asphaltenes content of equal to or more than 0.2 wt %, based on the total weight of the petroleum-derived hydrocarbon composition, to produce a hydrocarbon-containing mixture; c) dewatering the hydrocarbon-containing mixture to produce a dewatered hydrocarbon-containing mixture; d) contacting the dewatered hydrocarbon-containing mixture with hydrogen in one or more ebullating bed reactors comprising a catalyst at a temperature in the range from 350 to 500° C. to produce a reaction product.

    摘要翻译： 一种用于转化生物质材料的方法，包括a）热解生物质材料以产生生物质衍生的热解产物; b）将至少部分生物质衍生的热解产物和石油衍生的烃组合物混合，所述石油衍生的烃组合物具有基于石油的总重量等于或大于0.2重量％的C7-沥青质含量 得到的含烃混合物; c）使含烃混合物脱水以产生脱水的含烃混合物; d）使脱水的含烃混合物与氢在一个或多个沸腾床反应器中接触，所述反应床包含催化剂，温度为350-500℃，以产生反应产物。

    Process for treating a hydrocarbon-containing feed
    96.
    发明授权
    Process for treating a hydrocarbon-containing feed 有权
    处理含烃原料的方法

    公开(公告)号：US08834707B2

    公开(公告)日：2014-09-16

    申请号：US13314781

    申请日：2011-12-08

    申请人： Stanley Nemec Milam ,  Michael Anthony Reynolds ,  Scott Lee Wellington ,  Frederik Arnold Buhrman

    发明人： Stanley Nemec Milam ,  Michael Anthony Reynolds ,  Scott Lee Wellington ,  Frederik Arnold Buhrman

    IPC分类号： C10G65/12 ,  C10G47/06 ,  C10G47/26 ,  B01J27/043

    CPC分类号： C10G65/12 ,  B01J27/043 ,  C10G47/06 ,  C10G47/26 ,  C10G2300/202 ,  C10G2300/207 ,  C10G2300/301 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2400/30

    摘要： A process for treating a hydrocarbon-containing feedstock is provided in which a hydrocarbon-containing feedstock comprising at least 20 wt. % of heavy hydrocarbons is mixed with hydrogen, hydrogen sulfide and a metal-containing catalyst at a temperature of 375° C. to 500° C. and a pressure of from 6.9 MPa to 27.5 MPa to produce a vapor comprising a first hydrocarbon-containing product, where the hydrogen sulfide is mixed with the feedstock, metal-containing catalyst, and hydrogen at a mole ratio of hydrogen sulfide to hydrogen of at least 1:10. The vapor comprising the first hydrocarbon-containing product is separated from the mixture, and, apart from the mixture, the first hydrocarbon-containing product is contacted with hydrogen and a catalyst containing a Column 6 metal at a temperature of 260° C.-425° C. and a pressure of from 3.4 MPa to 27.5 MPa to produce a second hydrocarbon-containing product.

    摘要翻译： 提供了一种处理含烃原料的方法，其中含烃原料包含至少20wt。 ％的重质烃与氢，硫化氢和含金属的催化剂在375℃至500℃的温度和6.9MPa至27.5MPa的压力下混合以产生包含第一含烃的 产物，其中硫化氢与原料，含金属的催化剂和氢气以硫化氢与氢气的摩尔比混合至至少1:10。 包含第一含烃产物的蒸汽与混合物分离，除混合物外，第一含烃产物与氢气和含有第6列金属的催化剂在260℃-255℃的温度下接触 ℃，压力为3.4MPa至27.5MPa，以产生第二含烃产物。

    SLURRY HYDROCRACKING PROCESS
    98.
    发明申请
    SLURRY HYDROCRACKING PROCESS 有权
    水泥加工工艺

    公开(公告)号：US20140102944A1

    公开(公告)日：2014-04-17

    申请号：US13652439

    申请日：2012-10-15

    申请人： UOP LLC

    发明人： Lorenz J. Bauer ,  Maureen L. Bricker ,  Beckay J. Mezza ,  Alakananda Bhattacharyya

    IPC分类号： C10G47/02 ,  C10G47/04

    CPC分类号： C10G47/02 ,  C10G47/04 ,  C10G47/26

    摘要： One exemplary embodiment can be a slurry hydrocracking process. The process can include providing one or more hydrocarbon compounds having an initial boiling point temperature of at least about 340° C., and a slurry catalyst to a slurry hydrocracking zone. The slurry catalyst may have about 32- about 50%, by weight, iron; about 3- about 14%, by weight, aluminum; no more than about 10%, by weight, sodium; and about 2- about 10%, by weight, calcium. Typically, all catalytic component percentages are as metal and based on the weight of the dried slurry catalyst.

    摘要翻译： 一个示例性实施方案可以是浆料加氢裂化方法。 该方法可以包括提供一种或多种具有至少约340℃的初始沸点温度的烃化合物，以及将淤浆催化剂提供给浆料加氢裂化区。 浆料催化剂可以具有约32-约50重量％的铁; 约3-约14重量％的铝; 不超过约10重量％的钠; 和约2-约10重量％的钙。 通常，所有的催化组分百分数都是金属，并且基于干浆料催化剂的重量。

    SYSTEMS FOR HYDROPROCESSING HEAVY OIL
    100.
    发明申请
    SYSTEMS FOR HYDROPROCESSING HEAVY OIL 有权
    用于加氢重油的系统

    公开(公告)号：US20140093433A1

    公开(公告)日：2014-04-03

    申请号：US14095698

    申请日：2013-12-03

    申请人： HEADWATERS HEAVY OIL, LLC

    发明人： Roger K. Lott ,  Lap Keung Lee

    IPC分类号： C10G49/00

    CPC分类号： C10G47/06 ,  B01J8/08 ,  B01J8/22 ,  B01J8/226 ,  C10G45/04 ,  C10G45/16 ,  C10G45/34 ,  C10G45/46 ,  C10G45/56 ,  C10G47/26 ,  C10G49/005 ,  C10G49/12 ,  C10G65/00 ,  C10G65/02 ,  C10G67/08 ,  C10G2300/1033 ,  C10G2300/107 ,  C10G2300/1077 ,  C10G2300/202 ,  C10G2300/206 ,  C10G2300/4056 ,  C10G2300/70 ,  C10G2300/703 ,  C10G2300/802

    摘要： A hydroprocessing system involves introducing heavy oil and in situ formed metal sulfide catalyst particles, or a catalyst precursor capable of forming metal sulfide catalyst particles in situ within the heavy oil, into a hydroprocessing reactor. The metal sulfide catalyst particles are formed in situ by 1) premixing a catalyst precursor with a hydrocarbon diluent to form a precursor mixture, 2) mixing the precursor mixture with heavy oil to form a conditioned feedstock, and 3) heating the conditioned feedstock to decompose the catalyst precursor and cause or allow metal from the precursor to react with sulfur in the heavy oil to form the metal sulfide catalyst particles in situ in the heavy oil. The in situ formed metal sulfide catalyst particles catalyze beneficial upgrading reactions between the heavy oil and hydrogen and eliminates or reduces formation of coke precursors and sediment.

    摘要翻译： 加氢处理系统包括将重油和原位形成的金属硫化物催化剂颗粒或能够在重油内原位形成金属硫化物催化剂颗粒的催化剂前体引入加氢处理反应器。 金属硫化物催化剂颗粒是通过以下步骤形成的：1）将催化剂前体与烃稀释剂预混合以形成前体混合物，2）将前体混合物与重油混合以形成调节原料，和3）加热经调节的原料以分解 催化剂前体并使来自前体的金属与重油中的硫反应，以在重油中原位形成金属硫化物催化剂颗粒。 原位形成的金属硫化物催化剂颗粒催化重油和氢之间的有益升级反应，消除或减少焦炭前体和沉积物的形成。