Secure global telephone number system and method of operation
    3.
    发明申请
    Secure global telephone number system and method of operation 审中-公开
    安全的全球电话号码系统和操作方法

    公开(公告)号:US20060222156A1

    公开(公告)日:2006-10-05

    申请号:US11098969

    申请日:2005-04-05

    申请人: C. Smith R. Zuniga

    发明人: C. Smith R. Zuniga

    IPC分类号: H04M3/42 H04M3/00

    摘要: Techniques for processing calls in a communications system. A method and a system for protecting a person's telecommunications identify includes associating a global phone number with at least one contact address. The person may publicize global number. Thereafter, the person receives all communications using the global number. Using global number, the disclosed subject matter confidentially transfers the communications from global number to at least one direct contact address. The method and system may further include screening out undesirable communications.

    摘要翻译: 在通信系统中处理呼叫的技术。 一种用于保护个人的电信标识的方法和系统包括将全球电话号码与至少一个联系人地址相关联。 该人可以宣传全球数字。 此后,该人员使用全球号码接收所有通信。 使用全球号码,所公开的主题保密地将通信从全球号码传送到至少一个直接联系人地址。 该方法和系统可以进一步包括筛选不期望的通信。

    Process for making high octane gasoline with reduced benzene content
    5.
    发明申请
    Process for making high octane gasoline with reduced benzene content 审中-公开
    制备具有降低苯含量的高辛烷值汽油的方法

    公开(公告)号:US20060194998A1

    公开(公告)日:2006-08-31

    申请号:US11362256

    申请日:2006-02-27

    IPC分类号: C07C2/68

    摘要: Solid phosphoric acid (SPA) olefin oligomerization process units may be converted to operation with a more environmentally favorable solid catalyst. The SPA units in which a light olefin feed is oligomerized to form gasoline boiling range hydrocarbon product, is converted unit to operation with a molecular sieve based olefin oligomerization catalyst comprising an MWW zeolite material. Besides being more environmentally favorable in use, the MWW based zeolites offer advantages in catalyst cycle life, selectivity. After loading of the catalyst, the converted unit is operated as a fixed-bed unit by passing a C2- C4 olefinic feed and a light aromatic co-feed containing benzene to a fixed bed of the MWW zeolite catalyst to effect alkylation of the benzene with the aromatic co-feed, typically at a temperature from 150 to 350° C., a pressure not greater than 7000 kpa, usually less than 4000 kPa and an olefin space velocity up to 10 WHSV.

    摘要翻译: 固体磷酸(SPA)烯烃低聚过程单元可以转化为具有更环保的固体催化剂的操作。 将轻烯烃进料低聚以形成汽油沸程烃产物的SPA单元通过包含MWW沸石材料的基于分子筛的烯烃低聚催化剂转化为操作。 除了在使用环境方面更有利,基于MWW的沸石还具有催化剂循环寿命,选择性等优点。 载入催化剂后,转化的单元通过使C 2 -C 4亚烷基烯烃进料和含有苯的轻芳族共进料作为固定床单元进行操作 到MWW沸石催化剂的固定床上,以通过芳族共进料烷基化苯,通常在150-350℃的温度下,不大于7000kpa(通常小于4000kPa)的压力和烯烃 空速可达10 WHSV。