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    PROCESS TO MAKE OLEFINS FROM METHANOL AND ISOBUTANOL
    121.
    发明申请
    PROCESS TO MAKE OLEFINS FROM METHANOL AND ISOBUTANOL 审中-公开
    从甲醇和异丁醇制备油脂的方法

    公开(公告)号：US20130217935A1

    公开(公告)日：2013-08-22

    申请号：US13813170

    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: C07C1/22 ,  B01J29/40 ,  B01J2229/42 ,  C07C1/20 ,  C07C1/24 ,  C07C4/06 ,  C07C2529/40 ,  C10G3/44 ,  C10G3/49 ,  C10G3/62 ,  C10G2300/1014 ,  C10G2300/1022 ,  C10G2300/201 ,  C10G2300/4081 ,  C10G2400/20 ,  C12P5/026 ,  C12P7/16 ,  Y02E50/10 ,  Y02P20/52 ,  Y02P30/42 ,  C07C11/02 ,  C07C11/06 ,  C07C11/08 ,  C07C11/04

    Abstract: The present invention relates to a process for making essentially ethylene and propylene comprising: a) providing an alcohol mixture (A) comprising about 20 w % to 100% isobutanol, b) introducing in a reactor (A) a stream comprising the mixture (A) mixed with methanol or dimethyl ether or mixture thereof, optionally water, optionally an inert component, c) contacting said stream with a catalyst (A1) in said reactor (A), the MTO reactor, at conditions effective to convert at least a part of the alcohol mixture (A) and at least a part of the methanol and/or dimethyl ether to olefins, d) recovering from said reactor (A) an effluent comprising: ethylene, propylene, butene, water, optionally unconverted alcohols, various hydrocarbons, and the optional inert component of step b), e) fractionating said effluent of step d) 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: 本发明涉及一种基本上制备乙烯和丙烯的方法，包括：a）提供包含约20重量％至100重量％异丁醇的醇混合物（A），b）在反应器（A）中引入包含混合物（A ）与甲醇或二甲醚或其混合物，任选的水，任选的惰性组分混合，c）使所述流与所述反应器（A）中的催化剂（A1），所述MTO反应器在有效地转化至少一部分 的醇混合物（A）和至少一部分甲醇和/或二甲醚至烯烃，d）从所述反应器（A）回收包含乙烯，丙烯，丁烯，水，任选未转化的醇，各种烃 和步骤b）的任选的惰性组分，e）将步骤d）的所述流出物分馏以产生至少一种乙烯流，丙烯料流，基本上由具有4个或更多个碳原子的烃组成的馏分，水和任选的惰性 com 步骤a）的方法，任选地在反应器（A）的入口处全部或部分地回收乙烯，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。

    Methods for removal of colored- and sulfur-containing impurities from hydrocarbon streams
    125.
    发明授权
    Methods for removal of colored- and sulfur-containing impurities from hydrocarbon streams 有权
    从烃流中除去有色和含硫杂质的方法

    公开(公告)号：US08361312B2

    公开(公告)日：2013-01-29

    申请号：US12706923

    申请日：2010-02-17

    Applicant: Amy Sealey ,  Randi Wytcherley

    Inventor： Amy Sealey ,  Randi Wytcherley

    IPC: C07C7/12

    CPC classification number: B01J20/28052 ,  B01J20/12 ,  B01J2220/603 ,  C10G25/003 ,  C10G25/12 ,  C10G2300/104 ,  C10G2300/1096 ,  C10G2300/201 ,  C10G2300/202 ,  C10G2400/02

    Abstract: In various embodiments, the present disclosure describes methods for removing impurities from a hydrocarbon stream containing at least one vinyl aromatic compound such as, for example, styrene. The methods include pretreating at least one sorbent to make the at least one sorbent operable for adsorbing the impurities, contacting the hydrocarbon stream with the at least one sorbent in order to adsorb at least a portion of the impurities and separating the hydrocarbon stream from the at least one sorbent. Impurities include, for example, colored impurities, sulfur-containing impurities and combinations thereof.

    Abstract translation: 在各种实施方案中，本公开描述了从含有至少一种乙烯基芳族化合物例如苯乙烯的烃流中除去杂质的方法。 所述方法包括预处理至少一种吸附剂，以使至少一种吸附剂可操作以吸附杂质，使烃流与至少一种吸附剂接触，以便吸附至少一部分杂质，并将烃流与at 至少一种吸附剂。 杂质包括例如有色杂质，含硫杂质及其组合。

    Process for measuring and adjusting halide in an alkylation reactor
    127.
    发明授权
    Process for measuring and adjusting halide in an alkylation reactor 有权
    在烷基化反应器中测量和调节卤化物的方法

    公开(公告)号：US08323478B2

    公开(公告)日：2012-12-04

    申请号：US13187656

    申请日：2011-07-21

    Applicant: Sven Ivar Hommeltoft ,  Howard S. Lacheen

    Inventor： Sven Ivar Hommeltoft ,  Howard S. Lacheen

    IPC: C07C2/58

    CPC classification number: C10G29/205 ,  C10G45/32 ,  C10G2300/1081 ,  C10G2300/1088 ,  C10G2300/1096 ,  C10G2300/201 ,  C10G2300/305 ,  C10G2300/4025 ,  C10G2300/80 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/10

    Abstract: A process, comprising: a. taking a sample from a continuous alkylation reactor process; b. measuring a content of a halide in the sample; and c. within 45 minutes from the taking a sample, adjusting a flow of a halide containing additive comprising the halide to control a ratio of a yield of an alkylate gasoline and a yield of a middle distillate. Also a process, comprising: a. taking a sample from an effluent of an alkylation reactor in an alkylation reactor process; b. measuring a content of a halide in the sample; and c. in response to the measured content of the halide, adjusting a flow of a halide containing additive to a predetermined range that has been selected to obtain a ratio of a yield of an alkylate gasoline and a yield of a middle distillate from 0.31 to 4.0 in a product from the alkylation reactor.

    Abstract translation: 一个过程，包括：a。 从连续烷基化反应器工艺中取样; b。 测量样品中卤化物的含量; 和c。 在取样后45分钟内，调节包含卤化物的含卤化物添加剂的流动，以控制烷基化汽油的产率和中间馏分的产率。 还有一个过程，包括：a。 在烷基化反应器工艺中从烷基化反应器的流出物中取出样品; b。 测量样品中卤化物的含量; 和c。 响应于测量的卤化物含量，将含卤化物的添加剂的流量调节到预定范围内，以获得烷基化汽油的产率与中间馏分的产率之比为0.31至4.0，在 产物从烷基化反应器。

    RAPID THERMAL PROCESSING OF HEAVY HYDROCARBON FEEDSTOCKS
    128.
    发明申请
    RAPID THERMAL PROCESSING OF HEAVY HYDROCARBON FEEDSTOCKS 审中-公开
    重度热处理重油加料

    公开(公告)号：US20120279825A1

    公开(公告)日：2012-11-08

    申请号：US13552536

    申请日：2012-07-18

    Applicant: Barry Freel ,  Robert G. Graham

    Inventor： Barry Freel ,  Robert G. Graham

    IPC: C10G9/00

    CPC classification number: C10B55/04 ,  C10G9/32 ,  C10G31/06 ,  C10G2300/201 ,  C10G2300/208 ,  C10G2300/302 ,  C10G2300/304 ,  C10G2300/308

    Abstract: The present invention is directed to the upgrading of heavy hydrocarbon feedstock that utilizes a short residence pyrolytic reactor operating under conditions that cracks and chemically upgrades the feedstock. The method for upgrading a heavy hydrocarbon feedstock comprises introducing a particulate heat carrier into an upflow reactor, introducing the heavy hydrocarbon feedstock into the upflow reactor at a location above that of the particulate heat carrier so that a loading ratio of the particulate heat carrier to feedstock is from about 15:1 to about 200:1, allowing the heavy hydrocarbon feedstock to interact with the heat carrier with a residence time of less than about 1 second, to produce a product stream, separating the product stream from the particulate heat carrier, regenerating the particulate heat carrier, and collecting a gaseous and liquid product from the product stream.

    Abstract translation: 本发明涉及使用在裂化和化学升级原料的条件下运行的短停留热解反应器的重质烃原料的升级。 用于升级重质烃原料的方法包括将颗粒状热载体引入向上流动的反应器中，将重质烃原料引入到高于微粒热载体的位置的上游反应器中，使得颗粒状热载体与原料的负载比 为约15:1至约200:1，允许重质烃原料与热载体相互作用，停留时间小于约1秒，以产生产物流，将产物流与颗粒状热载体分离， 再生颗粒状热载体，并从产物流中收集气态和液态产物。

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