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    SOLAR ENERGY BASED COUNTINUOUS PROCESS AND REACTOR SYSTEM FOR THE PRODUCTION OF AN ALKENE BY DEHYDROGENATION OF THE CORRESPONDING ALKANE
    3.
    发明申请
    SOLAR ENERGY BASED COUNTINUOUS PROCESS AND REACTOR SYSTEM FOR THE PRODUCTION OF AN ALKENE BY DEHYDROGENATION OF THE CORRESPONDING ALKANE 审中-公开
    通过对相应的碱进行脱氢生产烷基苯基的太阳能基于反应器的反应器和反应器系统

    公开(公告)号：US20150139896A1

    公开(公告)日：2015-05-21

    申请号：US14396622

    申请日：2013-04-19

    Applicant: SAUDI BASIC INDUSTRIES CORPORATION

    Inventor： Mohamed Sabri Abdelghani ,  Mustapha Karime ,  Zeeshan Nawaz ,  Abdullah Mohammad Al-Qahtani

    IPC: C07C5/48 ,  C01B3/38 ,  C07C5/333

    CPC classification number: C07C5/48 ,  C01B3/386 ,  C01B2203/0261 ,  C01B2203/0277 ,  C01B2203/0855 ,  C01B2203/107 ,  C01B2203/1088 ,  C07C5/3337 ,  C07C2529/068 ,  C10G35/04

    Abstract: A solar energy based continuous process and reactor system for the production of an alkene by dehydrogenation of the corresponding alkane is performed in a reactor which process comprises alternatingly performing a first mode and a second mode in the same reactor, wherein the first mode is a non-oxidative dehydrogenation wherein the non-oxidative dehydrogenation is performed by contacting the alkane with a suitable dehydrogenation catalyst at a temperature of at least 500° C. to produce the corresponding alkene and hydrogen and wherein the second mode is an oxidative dehydrogenation wherein the oxidative dehydrogenation is performed by contacting the alkane with a suitable dehydrogenation catalyst and an oxidation agent at a temperature from 300 to 500° C. to produce the corresponding alkene wherein the dehydrogenation catalyst for the oxidative dehydrogenation and the non-oxidative dehydrogenation are the same, wherein the heat for the first mode is provided by a solar energy source.

    Abstract translation: 用于通过相应烷烃脱氢生产烯烃的基于太阳能的连续方法和反应器系统在反应器中进行，该反应器包括在同一反应器中交替执行第一模式和第二模式，其中第一模式是非 氧化脱氢，其中所述非氧化脱氢是通过在至少500℃的温度下使所述烷烃与合适的脱氢催化剂接触以产生相应的烯烃和氢气进行的，其中所述第二模式是氧化脱氢，其中所述氧化脱氢 是通过使烷烃与合适的脱氢催化剂和氧化剂在300-500℃的温度下接触来制备相应的烯烃，其中用于氧化脱氢和非氧化脱氢的脱氢催化剂是相同的，其中 用于第一模式的热量由太阳能源提供 。

    INTEGRATED STEAM CRACKER AND MTBE PRODUCTION UNITS
    7.
    发明申请
    INTEGRATED STEAM CRACKER AND MTBE PRODUCTION UNITS 审中-公开
    综合蒸汽破碎机和MTBE生产单位

    公开(公告)号：US20160326079A1

    公开(公告)日：2016-11-10

    申请号：US15109184

    申请日：2015-01-02

    Applicant: SAUDI BASIC INDUSTRIES CORPORATION

    Inventor： Guillermo Leal ,  Zeeshan Nawaz ,  Antonio Matarredona ,  Faisal Baksh

    IPC: C07C41/06 ,  B01J19/24 ,  C07C4/04

    CPC classification number: C07C41/06 ,  B01J19/245 ,  B01J2219/24 ,  C07C4/04 ,  C10G9/36 ,  C07C43/046

    Abstract: Described herein are methods and systems for producing methyl t-butyl ether (MTBE) by reacting an isobutene-containing stream with methanol in an MTBE production unit. In accordance with the method described herein, at least a portion of the isobutene-containing stream is obtained from a mixed C4 stream from a steam cracking unit and is not produced by passing the dehydrogenation of isobutane. Furthermore, an alkane-containing stream from the MTBE production unit is used as a feed stream for the steam cracking unit.

    Abstract translation: 本文描述了通过在MTBE生产单元中使含异丁烯的物流与甲醇反应生产甲基叔丁基醚（MTBE）的方法和系统。 根据本文所述的方法，至少一部分含异丁烯的物流由来自蒸汽裂解装置的混合C4物流获得，并且不通过使异丁烷脱氢而产生。 此外，使用来自MTBE生产单元的含烷烃的物流作为蒸汽裂解装置的进料流。

    REACTOR AND PROCESS FOR PARAFFIN DEHYDROGENATION TO OLEFINS
    8.
    发明申请
    REACTOR AND PROCESS FOR PARAFFIN DEHYDROGENATION TO OLEFINS 审中-公开
    对于烯烃脱氢的反应器和方法

    公开(公告)号：US20160068454A1

    公开(公告)日：2016-03-10

    申请号：US14783005

    申请日：2014-04-04

    Applicant: SAUDI BASIC INDUSTRIES CORPORATION

    Inventor： Zeeshan Nawaz ,  Faisal Baksh

    IPC: C07C5/333 ,  B01J8/24 ,  B01J8/18 ,  B01J8/26

    CPC classification number: C07C5/3337 ,  B01J8/0055 ,  B01J8/1836 ,  B01J8/24 ,  B01J8/26 ,  B01J23/92 ,  B01J23/96 ,  B01J38/02 ,  B01J38/30 ,  B01J2208/00168 ,  B01J2208/00203 ,  C07C5/3335 ,  C07C5/48 ,  C07C2521/04 ,  C07C2523/26 ,  C07C2523/42 ,  C10G11/05 ,  C10G11/182 ,  C10G2300/1081 ,  C10G2400/20 ,  Y02P20/584 ,  C07C11/02

    Abstract: Disclosed herein is a method and apparatus for dehydrogenation of a paraffin comprising: providing a dehydrogenation reactor comprising an integrated fluidized bed reactor and a regenerator reactor, wherein the integrated fluidized bed reactor has a first longitudinal axis and comprises an inner surface defining an interior space, wherein the regenerator reactor has a second longitudinal axis and is positioned at least partially within the interior space; activating a deactivated catalyst present in the regenerator reactor by performing a exothermic catalyst regeneration reaction to produce an activated catalyst and heat; transferring the heat to the integrated fluidized bed reactor; and dehydrogenating a paraffm present in the integrated fluidized bed reactor by performing an endothermic reaction with a catalyst, the paraffm, and at least a portion of the transferred heat to forma dehydrogenation product.

    Abstract translation: 本文公开了一种用于脱氢石蜡的方法和装置，包括：提供包含集成流化床反应器和再生器反应器的脱氢反应器，其中所述一体化流化床反应器具有第一纵向轴线并且包括限定内部空间的内表面， 其中所述再生器反应器具有第二纵向轴线并且至少部分地定位在所述内部空间内; 通过进行放热催化剂再生反应来活化再生器反应器中存在的失活的催化剂以产生活化的催化剂和加热; 将热量传递到集成流化床反应器; 并通过与催化剂，石蜡和至少一部分转移的热量进行吸热反应，使整合的流化床反应器中存在的石蜡脱氢形成脱氢产物。

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