Ethylene production by steam cracking of normal paraffins
    11.
    发明授权
    Ethylene production by steam cracking of normal paraffins 有权
    乙烯生产通过蒸汽裂解正链烷烃

    公开(公告)号:US08283511B2

    公开(公告)日:2012-10-09

    申请号:US12749817

    申请日:2010-03-30

    IPC分类号: C07C7/12

    摘要: A simulated moving bed adsorptive separation process for preparing the separate feed streams charged to naphtha reforming unit and a steam cracking unit has been developed. The feed stream to the overall unit is passed into the adsorptive separation unit. The desorbent in the adsorptive separation is C12 hydrocarbons. The simulated moving bed adsorptive separation separates the components of the feed stream into a normal paraffin stream, which is charged to the steam cracking process, and non-normal hydrocarbons which are passed into a reforming zone. The desorbent is readily separated from the normal paraffin stream and from the non-normal paraffin stream and the simulated moving bed adsorption zone is operated at an A/Fn ratio of from about 0.90 to about 0.92.

    摘要翻译: 已经开发了用于制备装载到石脑油重整单元和蒸汽裂解装置的单独进料流的模拟移动床吸附分离方法。 到整个单元的进料流被送入吸附分离单元。 吸附分离中的解吸剂是C12烃。 模拟的移动床吸附分离将进料流的组分分离成正常的石蜡流,将其装入蒸汽裂解过程,并将非正常烃进入重整区。 解吸剂容易地与正链烷烃流和非正构链烷烃流分离,并且模拟移动床吸附区以约0.90至约0.92的A / Fn比操作。

    Removal of impurities from liquid hydrocarbon streams
    13.
    发明授权
    Removal of impurities from liquid hydrocarbon streams 失效
    从液态烃流中去除杂质

    公开(公告)号:US07128829B1

    公开(公告)日:2006-10-31

    申请号:US10447752

    申请日:2003-05-29

    摘要: A novel process effective for the removal of organic sulfur compounds, organic nitrogen compounds and light olefins from liquid hydrocarbons is disclosed. The process more specifically addresses the removal of these contaminants from aromatic compounds including benzene and toluene and from naphtha. The liquid hydrocarbons are contacted with a blend of at least one metal oxide and an acidic zeolite. Preferably, the metal oxide comprises nickel oxide and molybdenum oxide and the acidic zeolite is acidic stabilized zeolite Y. This blend has a significant capacity for adsorption of impurities and can be regenerated by oxidative treatment.

    摘要翻译: 公开了一种有效从液态烃中去除有机硫化合物,有机氮化合物和轻质烯烃的新方法。 该方法更具体地涉及从芳族化合物(包括苯和甲苯)和石脑油中除去这些污染物。 液体烃与至少一种金属氧化物和酸性沸石的共混物接触。 优选地,金属氧化物包括氧化镍和氧化钼,酸性沸石是酸性稳定的沸石Y.该共混物具有显着的吸附杂质的能力,可以通过氧化处理再生。

    Process for removal of oxygenates from a paraffin stream
    14.
    发明授权
    Process for removal of oxygenates from a paraffin stream 有权
    从石蜡流中除去含氧化合物的方法

    公开(公告)号:US07102044B1

    公开(公告)日:2006-09-05

    申请号:US10882887

    申请日:2004-06-30

    IPC分类号: C07C2/64

    摘要: The present invention comprises a process for removal of oxygenates from a paraffin-rich or olefin-rich paraffin stream which comprises passing a feed stream, comprising one or more C10 to C15 feed paraffins or C10 to C15 olefin-rich paraffin stream and one or more oxygenates through an adsorbent bed comprising one or more adsorbents selected from silica gel, activated alumina and sodium x zeolites to remove essentially all of said oxygenates; and recovering said paraffins. A second adsorbent bed may be employed to more thoroughly remove these oxygenates.

    摘要翻译: 本发明包括从富含链烷烃或富烯烃的石蜡流中除去含氧化合物的方法,该方法包括将含有一个或多个C 10的进料流通入C 15 通过吸附床将含有一种或多种选自硅胶,活性氧化铝和吸附剂的吸附剂的烷烃或C 10向富含C 15的富烯烃链烷烃流和一种或多种含氧化合物进料, 钠x沸石以除去基本上所有的含氧化合物; 并回收所述石蜡。 可以使用第二吸附剂床来更彻底地除去这些含氧化合物。

    Continuous alkylation of aromatics using solid catalysts; prevention of
catalyst deactivation using a pulsed feed reactor
    16.
    发明授权
    Continuous alkylation of aromatics using solid catalysts; prevention of catalyst deactivation using a pulsed feed reactor 失效
    使用固体催化剂连续烷基化芳烃; 使用脉冲进料反应器防止催化剂失活

    公开(公告)号:US5648579A

    公开(公告)日:1997-07-15

    申请号:US392006

    申请日:1995-02-21

    IPC分类号: C07C2/66 C07C15/067

    摘要: A novel continuous process for the preparation of alkylated benzenes effected by solid catalysts which become deactivated under alkylation conditions uses a single catalyst zone for both reaction and catalyst flushing to prevent deactivation. The process utilizes a pulsed flow of the linear monoolefins into the catalyst zone during a reaction cycle with benzene acting as a desorbent for catalyst deactivating agents to prevent significant catalyst deactivation. The process can be generalized to encompass many types of reactions.

    摘要翻译: 通过在烷基化条件下失活的固体催化剂制备烷基化苯的新型连续方法使用单一催化剂区域用于反应和催化剂冲洗以防止失活。 该方法在与作为催化剂失活剂的解吸剂的苯的反应循环期间利用脉冲流动的线性单烯烃进入催化剂区域,以防止显着的催化剂失活。 该过程可以被概括为包括许多类型的反应。

    Separation of an organic acid from a fermentation broth with an anionic
polymeric adsorbent
    18.
    发明授权
    Separation of an organic acid from a fermentation broth with an anionic polymeric adsorbent 失效
    用阴离子聚合物吸附剂从发酵液中分离有机酸

    公开(公告)号:US5068419A

    公开(公告)日:1991-11-26

    申请号:US349273

    申请日:1989-05-08

    IPC分类号: C07C51/47 C07C51/42

    CPC分类号: C07C51/47

    摘要: An organic acid is separated from a fermentation broth by using an adsorbent comprising a water-insoluble macroreticular or gel weakly basic anionic exchange resin possessing tertiary amine or pyridine functional groups or a strongly basic anionic exchange resin possessing quaternary amine functional groups. The resins are in sulfate form and have a cross-linked acrylic or styrene resin matrix. The organic acid is desorbed with water or dilute inorganic acid, e.g., sulfuric. The pH of the feed is maintained below the first ionization constant (pKa.sub.1) of the organic acid to obtain high selectivity.

    摘要翻译: 通过使用包含具有叔胺或吡啶官能团的水不溶性大网络或凝胶弱碱性阴离子交换树脂的吸附剂或具有季胺官能团的强碱性阴离子交换树脂,将有机酸与发酵液分离。 树脂为硫酸盐形式,并具有交联的丙烯酸或苯乙烯树脂基质。 有机酸用水或稀无机酸例如硫酸解吸。 饲料的pH保持低于有机酸的第一电离常数(pKa1),以获得高选择性。

    Adsorptive separation process for the purification of heavy normal
paraffins with non-normal hydrocarbon pre-pulse stream
    19.
    发明授权
    Adsorptive separation process for the purification of heavy normal paraffins with non-normal hydrocarbon pre-pulse stream 失效
    用非正常碳氢化合物预脉冲流净化重质正链烷烃的吸附分离方法

    公开(公告)号:US4992618A

    公开(公告)日:1991-02-12

    申请号:US391747

    申请日:1989-08-09

    CPC分类号: C07C7/13

    摘要: The separation of normal paraffins from non-normal hydrocarbons wherein the paraffins have from about 10 to about 35 carbon atoms per molecule, using a molecular sieve adsorbent having an effective channel diameter of about 5 angstroms wherein an improvement in the process comprises passing a non-normal hydrocarbon input stream into the adsorption zone at adsorption conditions to promote the selective adsorption of the straight chain hydrocarbon constituents of the feed material in contact with the adsorbent in preference to the lighter straight chain hydrocarbon constituents of the desorbent material also in contact with adsorbent.

    摘要翻译: 正链烷烃与非正常烃的分离,其中链烷烃具有约10至约35个碳原子/分子,使用具有约5埃的有效通道直径的分子筛吸附剂,其中该方法的改进包括: 正常碳氢化合物输入物流在吸附条件下进入吸附区,以促进与吸附剂接触的进料的直链烃组分的选择性吸附,优先于也与吸附剂接触的解吸剂材料的较轻的直链烃组分。

    Process for separating arabinose from a mixture of aldoses
    20.
    发明授权
    Process for separating arabinose from a mixture of aldoses 失效
    从阿糖混合物中分离阿拉伯糖的方法

    公开(公告)号:US4880919A

    公开(公告)日:1989-11-14

    申请号:US948384

    申请日:1986-12-31

    IPC分类号: C07H1/06 C13K1/00 C13K13/00

    CPC分类号: C13K13/00 C07H1/06 C13K1/00

    摘要: Arabinose is separated from mixtures of monosaccharides containing arabinose and other aldopentoses and aldohexoses by adsorption on sulfonated polystyrene divinylbenzene crosslinked ion exchange resins exchanged with calcium-ammonium cationic and desorbing the adsorbate with water. The other saccharides are removed from the adsorption process in the raffinate.

    摘要翻译: 将阿拉伯糖与含有阿拉伯糖和其他戊糖醛酸的单糖和其他己糖的混合物通过与磺化聚苯乙烯二乙烯基苯交联的离子交换树脂与阳离子铵阳离子交换并用水解吸吸附物进行吸附而分离。 其余的糖类从残液中的吸附过程中除去。