SYSTEM TO FACILITATE ONLINE SHOPPING
    34.
    发明申请
    SYSTEM TO FACILITATE ONLINE SHOPPING 审中-公开
    制定在线购物体系

    公开(公告)号:US20090299875A1

    公开(公告)日:2009-12-03

    申请号:US12129701

    申请日:2008-05-30

    IPC分类号: G06Q30/00

    CPC分类号: G06Q30/06 G06Q30/0601

    摘要: A system for facilitating online shopping that includes one or more content providers of a first domain, one or more online merchants of a second domain, and a framework. Web pages may be aggregated from the content providers. Descriptions of products for sale may be aggregated from the online merchants. The products for sale may be matched with the web pages based on relevancy. A list of descriptions of products that are relevant to each web page may be provided. A shopping cart list may be maintained by the framework. The shopping cart list may facilitate payment for the products for sale selected from different web pages.

    摘要翻译: 一种用于促进在线购物的系统,其包括第一域的一个或多个内容提供商,第二域的一个或多个在线商家和框架。 可以从内容提供商聚合网页。 可以从在线商家汇总出售产品的描述。 出售的产品可能会根据相关性与网页匹配。 可以提供与每个网页相关的产品的描述的列表。 框架可以维护购物车列表。 购物车列表可以促进从不同网页选择的销售产品的支付。

    11,12-Cyclic thiocarbamate macrolide antibacterial agents
    35.
    发明申请
    11,12-Cyclic thiocarbamate macrolide antibacterial agents 审中-公开
    11,12-环硫代氨基甲酸酯大环内酯类抗菌剂

    公开(公告)号:US20050250713A1

    公开(公告)日:2005-11-10

    申请号:US11114502

    申请日:2005-04-26

    CPC分类号: C07H17/08

    摘要: The present invention is directed to novel macrolide antibacterial agents and processes for preparing them. The present invention is further directed to pharmaceutical compositions containing the novel macrolide antibacterial agents disclosed herein and their use in the treatment and prevention of bacterial infections.

    摘要翻译: 本发明涉及新型大环内酯类抗菌剂及其制备方法。 本发明进一步涉及含有本文所公开的新型大环内酯抗菌剂及其在治疗和预防细菌感染中的用途的药物组合物。

    Process for producing an alkylene oxide by olefin epoxidation
    39.
    发明授权
    Process for producing an alkylene oxide by olefin epoxidation 有权
    通过烯烃环氧化制备烯化氧的方法

    公开(公告)号:US08859791B2

    公开(公告)日:2014-10-14

    申请号:US13878659

    申请日:2011-10-11

    IPC分类号: C07D301/12 C07D303/04

    CPC分类号: C07D301/12 C07D303/04

    摘要: A process for producing an alkylene oxide by olefin epoxidation, wherein said process comprises the steps of: (1) in a first olefin epoxidation condition, in the presence of a first solid catalyst, a first mixed stream containing a solvent, an olefin and H2O2 is subjected to an epoxidation in one or more fixed bed reactors and/or one or more moving bed reactors until the conversion of H2O2 reaches 50%-95%, then, optionally, the resulting reaction mixture obtained in the step (1) is subjected to a separation to obtain a first stream free of H2O2 and a second stream containing the unreacted H2O2, and the olefin is introduced to the second stream to produce a second mixed stream, or optionally, the olefin is introduced to the reaction mixture obtained in the step (1) to produce a second mixed stream; (2) in a second olefin epoxidation condition, the reaction mixture obtained in the step (1) or the second mixed stream obtained in the step (1) and a second solid catalyst are introduced to one or more slurry bed reactors to conduct an epoxidation until the total conversion of H2O2 reaches 98% or more, with a proviso that said process for producing the alkylene oxide by olefin epoxidation has an selectivity for the alkylene oxide of 90% or more.The process of the present invention combines the slurry bed reactor with the fixed bed reactor and/or the moving bed reactor so as to overcome the disadvantages of the low conversion of H2O2 in the case that only the fixed bed reactor and/or the moving bed reactor are used, and the low selectivity for the target alkylene oxide in the case that only the slurry bed reactor is used.

    摘要翻译: 一种通过烯烃环氧化生产烯化氧的方法,其中所述方法包括以下步骤:(1)在第一烯烃环氧化条件下,在第一固体催化剂存在下,将含有溶剂,烯烃和H 2 O 2的第一混合物流 在一个或多个固定床反应器和/或一个或多个移动床反应器中进行环氧化,直到H 2 O 2的转化率达到50%-95%,然后,任选地,将在步骤(1)中获得的所得反应混合物 以分离以获得不含H 2 O 2的第一物流和含有未反应的H 2 O 2的第二物流,并将烯烃引入第二物流以产生第二混合物流,或任选地将烯烃引入到 步骤(1)以产生第二混合流; (2)在第二烯烃环氧化条件下,将步骤(1)中获得的反应混合物或步骤(1)中获得的第二混合物流和第二固体催化剂引入一个或多个淤浆床反应器中进行环氧化 直到H 2 O 2的总转化率达到98%以上,条件是通过烯烃环氧化生产环氧烷烃的方法对环氧烷烃的选择性为90%以上。 本发明的方法将淤浆床反应器与固定床反应器和/或移动床反应器结合,以克服在只有固定床反应器和/或移动床的情况下H 2 O 2转化率低的缺点 使用反应器,在仅使用浆料床反应器的情况下对目标烯化氧的选择性低。