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    PRODUCTION OF NON-CARCINOGENIC BRIGHTSTOCK EXTRACTS
    43.
    发明申请
    PRODUCTION OF NON-CARCINOGENIC BRIGHTSTOCK EXTRACTS 有权
    生产非致癌性亮点提取物

    公开(公告)号：US20140262958A1

    公开(公告)日：2014-09-18

    申请号：US13803454

    申请日：2013-03-14

    Applicant: EXXONMOBIL RESEARCH AND ENGINEERING COMPANY

    Inventor： Cristina M. Sircar ,  Keith K. Aldous ,  James J. Freeman ,  Katy O. Goyak

    IPC: G01N33/28

    CPC classification number: G01N33/2823 ,  C10G7/12 ,  C10G21/003 ,  C10G53/06 ,  C10G2300/1077 ,  C10G2300/201 ,  C10G2300/301 ,  C10G2300/4006

    Abstract: Provided are multiple correlations for relationships between MI value for a brightstock extract and the distillation cut point temperature used for separation of the vacuum resid that is used to form the brightstock extract. Based on these correlations, a BSE having a desired MI value can be formed based on an adjustment of the distillation cut point temperature. A first correlation establishes a relationship between a fractional weight boiling temperature for a vacuum resid fraction and a distillation cut point temperature for separating the vacuum resid fraction from at least one distillate fraction in a feedstock. A second correlation establishes a relationship between a fractional weight boiling temperature for a brightstock extract derived from the vacuum resid fraction, and the fractional weight boiling temperature for the vacuum resid fraction. A third correlation has been established between the fractional weight boiling temperature for the brightstock extract and a mutagenicity index value.

    Abstract translation: 对于明矾提取物的MI值与用于分离用于形成亮片提取物的真空渣油的蒸馏切割点温度之间的关系，提供多重相关性。 基于这些相关性，可以基于蒸馏切割点温度的调节形成具有期望MI值的BSE。 第一相关性建立了真空残渣馏分的分数重量沸点温度与用于将减压渣油馏分与原料中的至少一个馏出物馏分分离的蒸馏切割点温度之间的关系。 第二相关性确定了来自真空残渣馏分的亮片提取物的分数重量沸点温度与减压渣油馏分的分数重量沸点温度之间的关系。 在亮片提取物的分数重量沸点温度和致突变性指数值之间已经建立了第三个相关性。

    THERMAL DE-POLYMERIZATION PROCESS OF PLASTIC WASTE MATERIALS
    44.
    发明申请
    THERMAL DE-POLYMERIZATION PROCESS OF PLASTIC WASTE MATERIALS 审中-公开
    塑料废料的热脱聚工艺

    公开(公告)号：US20140155662A1

    公开(公告)日：2014-06-05

    申请号：US14234381

    申请日：2012-07-23

    Applicant: Shamsul Bahar bin Mohd Nor

    Inventor： Shamsul Bahar bin Mohd Nor

    IPC: C10G1/10

    CPC classification number: C10G1/10 ,  C08J11/12 ,  C08J11/14 ,  C10G2300/1003 ,  C10G2300/201 ,  C10G2300/202 ,  C10G2300/307 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2400/04 ,  C10L1/04 ,  Y02W30/703 ,  Y02W30/704

    Abstract: The present invention relates to a process for producing liquid transportation fuel (15) based on plastic waste materials (10), comprising the step of: providing (S101) plastic waste materials (10) in molten form; de-polymerizing (S103) molten plastic waste materials (10) into a reaction chamber using a limestone catalyst (20) at a temperature ranging 420° C. to 450° C. under normal atmospheric pressure condition of 1 Bar; and introducing (S106) gaseous de-polymerized products (25) to a distillation unit thereby allows the gaseous de-polymerized products (25) to be fractionally distilled and condensed into liquid transportation fuels (15).

    Abstract translation: 本发明涉及一种基于塑料废料（10）生产液体运输燃料（15）的方法，包括以下步骤：提供（S101）熔融形式的塑料废料（10）; 在1巴的正常大气压条件下，使用石灰石催化剂（20）在420℃至450℃的温度下将熔融塑料废料（10）去聚合（S103）到反应室中; 并将（S106）气态脱聚合产物（25）引入蒸馏单元，从而允许将气态脱聚产物（25）分馏并冷凝成液体运输燃料（15）。

    PROCESS TO MAKE OLEFINS FROM ISOBUTANOL
    45.
    发明申请
    PROCESS TO MAKE OLEFINS FROM ISOBUTANOL 有权
    从ISOBUTANOL制造OLEFINS的过程

    公开(公告)号：US20140148630A1

    公开(公告)日：2014-05-29

    申请号：US13813168

    申请日：2011-07-08

    Applicant: Cindy Adam ,  Delphine Minoux ,  Nikolai Nesterenko ,  Sander Van Donk ,  Jean-Pierre Dath

    Inventor： Cindy Adam ,  Delphine Minoux ,  Nikolai Nesterenko ,  Sander Van Donk ,  Jean-Pierre Dath

    IPC: C07C1/22

    CPC classification number: C07C1/24 ,  B01J29/40 ,  B01J2229/42 ,  C07C1/22 ,  C07C4/06 ,  C07C6/04 ,  C07C2529/40 ,  C08F10/02 ,  C10G3/42 ,  C10G3/44 ,  C10G3/49 ,  C10G2300/1014 ,  C10G2300/1022 ,  C10G2300/201 ,  C10G2300/4081 ,  C10G2400/20 ,  C10G2400/22 ,  C12P5/026 ,  C12P7/16 ,  Y02E50/10 ,  Y02P20/52 ,  Y02P30/20 ,  Y02P30/42 ,  C07C11/08 ,  C07C11/06

    Abstract: The present invention relates to a process for the conversion of an alcohol mixture (A) comprising about 20 w % to 100% isobutanol to make essentially propylene, comprising: a) introducing in a reactor (A) a stream comprising the mixture (A), optionally water, optionally an inert component, b) contacting said stream with a catalyst (A1) at a temperature above 450° C. in said reactor (A) at conditions effective to dehydrate at least a part of the isobutanol and other alcohols, if any, and make a cracking, c) recovering from said reactor (A) an effluent comprising: ethylene, propylene, water, optionally unconverted alcohols of the mixture (A), various hydrocarbons, and the optional inert component of step a), d) fractionating said effluent of step c) to produce at least an ethylene stream, a propylene stream, a fraction consisting essentially of hydrocarbons having 4 carbon atoms or more, water and the optional inert component of step a), optionally recycling ethylene in whole or in part at the inlet of the reactor (A), optionally recycling the fraction consisting essentially of hydrocarbons having 4 carbon atoms or more at the inlet of the reactor (A).

    Abstract translation: 本发明涉及一种将包含约20％至100％异丁醇的醇混合物（A）转化成基本上丙烯的方法，其包括：a）在反应器（A）中引入包含混合物（A）的料流， 任选的水，任选的惰性组分，b）在有效使至少一部分异丁醇和其它醇脱水的条件下，使所述物流与催化剂（A1）在高于450℃的温度下在所述反应器（A）中接触， c）从所述反应器（A）回收包含乙烯，丙烯，水，任选未转化的混合物（A）的醇，各种烃和步骤a）的任选的惰性组分的流出物， d）将步骤c）的所述流出物分馏以产生至少一种乙烯流，丙烯流，基本上由具有4个碳原子或更多的烃组成的级分，水和步骤a）的任选的惰性组分，任选地将乙烯全部回收 或在par 在反应器（A）的入口处，任选地在反应器（A）的入口处循环基本上由具有4个或更多个碳原子的烃组成的馏分。

    INTEGRATED HYDROTREATING AND STEAM PYROLYSIS PROCESS INCLUDING RESIDUAL BYPASS FOR DIRECT PROCESSING OF A CRUDE OIL
    49.
    发明申请
    INTEGRATED HYDROTREATING AND STEAM PYROLYSIS PROCESS INCLUDING RESIDUAL BYPASS FOR DIRECT PROCESSING OF A CRUDE OIL 有权
    一体化加氢和蒸汽热分解过程，包括用于直接加工原油的残留旁路

    公开(公告)号：US20130233767A1

    公开(公告)日：2013-09-12

    申请号：US13865060

    申请日：2013-04-17

    Applicant: Raheel SHAFI ,  Abdennour BOURANE ,  Ibrahim A. ABBA ,  Abdul Rahman Zafer AKHRAS

    Inventor： Raheel SHAFI ,  Abdennour BOURANE ,  Ibrahim A. ABBA ,  Abdul Rahman Zafer AKHRAS

    IPC: C10G69/06

    CPC classification number: C10G69/06 ,  C10G9/36 ,  C10G45/00 ,  C10G2300/201 ,  C10G2300/308 ,  C10G2300/4081 ,  C10G2400/20 ,  C10G2400/30

    Abstract: A process is provided that is directed to a steam pyrolysis zone integrated with a hydroprocessing zone including residual bypass to permit direct processing of crude oil feedstocks to produce petrochemicals including olefins and aromatics. The integrated hydrotreating and steam pyrolysis process for the direct processing of a crude oil to produce olefinic and aromatic petrochemicals comprises separating the crude oil into light components and heavy components; charging the light components and hydrogen to a hydroprocessing zone operating under conditions effective to produce a hydroprocessed effluent reduced having a reduced content of contaminants, an increased paraffinicity, reduced Bureau of Mines Correlation Index, and an increased American Petroleum Institute gravity; thermally cracking the hydroprocessed effluent in the presence of steam to produce a mixed product stream; separating the mixed product stream; purifying hydrogen recovered from the mixed product stream and recycling it to the hydroprocessing zone; recovering olefins and aromatics from the separated mixed product stream; and recovering a combined stream of pyrolysis fuel oil from the separated mixed product stream and heavy components from step (a) as a fuel oil blend.

    Abstract translation: 提供了一种方法，其涉及与包含残留旁路的加氢处理区整合的蒸汽热解区，以允许原油原料直接加工以生产包括烯烃和芳族化合物的石油化学品。 用于直接加工原油以生产烯烃和芳族石油化学品的综合加氢处理和蒸汽热解方法包括将原油分离成轻组分和重组分; 将轻组分和氢充入加氢处理区，其工作条件有效地产生具有降低的污染物含量，增加的链烷烃含量，减少的矿物相关指数和美国石油公司重力增加的加氢处理废水。 在蒸汽存在下对加氢处理的流出物进行热裂解以产生混合产物流; 分离混合产物流; 净化从混合产物流中回收的氢并将其再循环到加氢处理区; 从分离的混合产物流中回收烯烃和芳族化合物; 并从分离的混合产物流和作为燃料油混合物的步骤（a）的重组分回收热解燃料油的混合物流。

    COMBINED PROCESS TO MAKE OLEFINS FROM ISOBUTANOL
    50.
    发明申请
    COMBINED PROCESS TO MAKE OLEFINS FROM ISOBUTANOL 有权

    公开(公告)号：US20130204058A1

    公开(公告)日：2013-08-08

    申请号：US13813107

    申请日：2011-07-08

    Applicant: Cindy Adam ,  Delphine Minoux ,  Nikolai Nesterenko ,  Sander Van Donk ,  Jean-Pierre Dath

    Inventor： Cindy Adam ,  Delphine Minoux ,  Nikolai Nesterenko ,  Sander Van Donk ,  Jean-Pierre Dath

    IPC: C07C1/24 ,  C07C4/06

    CPC classification number: C07C1/24 ,  B01J21/04 ,  B01J29/40 ,  B01J29/65 ,  C07C4/06 ,  C07C2521/04 ,  C07C2529/40 ,  C07C2529/65 ,  C07C2529/85 ,  C10G3/44 ,  C10G3/49 ,  C10G2300/1014 ,  C10G2300/201 ,  C10G2300/4081 ,  C10G2400/20 ,  C10G2400/22 ,  C12P5/026 ,  C12P7/16 ,  Y02E50/10 ,  Y02P20/52 ,  Y02P30/20 ,  Y02P30/42 ,  C07C11/08 ,  C07C11/06

    Abstract: The present invention relates to a process for the conversion of an alcohols mixture (A) comprising about 20 w % to 100% isobutanol to make essentially propylene, comprising: a) introducing in a reactor (A) (also called the first reaction zone or low temperature reaction zone) a stream comprising the mixture (A), optionally water, optionally an inert component, b) contacting said stream with a catalyst (A1) in said reactor (A) at conditions effective to dehydrate: at least a portion of the isobutanol to essentially butenes, at least a portion of other alcohols, if any, to essentially olefins other than butene having the same carbon number as the alcohol precursor, c) recovering from said reactor (A) an effluent comprising: butenes, optionally olefins other than butene, water, optionally unconverted alcohols of the mixture (A), various hydrocarbons, and the optional inert component of step a), d) fractionating said effluent of step c) to remove a portion or all the water, unconverted alcohols, optionally the inert component, and optionally the whole or a part of the various hydrocarbons to get a stream (D) comprising essentially olefins and optionally the inert component, e) introducing at least a part of said stream (D) in an OCP reactor (also called the second reaction zone or high temperature zone), f) contacting said stream comprising at least a part of (D), optionally in combination with a stream (D1) comprising olefins having 4 carbon atoms or more (C4+ olefins), in said OCP reactor with a catalyst which is selective towards light olefins in the effluent, to produce an effluent with an olefin content of lower molecular weight than that of the feedstock, g) fractionating said effluent of step f) to produce at least an ethylene stream, a propylene stream and a fraction consisting essentially of hydrocarbons having 4 carbon atoms or more, optionally recycling ethylene in whole or in part at the inlet of the OCP reactor of step f), or at the inlet of the reactor (A) or at the inlet of both the OCP reactor of step f) and the reactor (A), optionally recycling the fraction consisting essentially of hydrocarbons having 4 carbon atoms or more at the inlet of the OCP reactor.

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