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    • 2. 发明申请
    • SYSTEMS AND METHODS FOR CREATING PROGRAMMABLE REPLY FUNCTIONS FOR AN INSTANT MESSAGING CLIENT
    • 为即将发布的消息客户端创建可编程回复功能的系统和方法
    • US20080129469A1
    • 2008-06-05
    • US11566066
    • 2006-12-01
    • Charles SumnerAndrea L. Snow-Weaver
    • Charles SumnerAndrea L. Snow-Weaver
    • G08B1/08
    • G06Q10/107
    • A method for adding a customizable reply function to an interface in an instant messaging (IM) client, including the steps of identifying a string of characters to be associated with the reply function, choosing an action of the IM client to be associated with the reply function, selecting presentation characteristics of a representation of the reply function in the interface of the IM client, and incorporating the reply function into the interface of the IM client, where a subsequent user selection of the incorporated representation of the reply function in the IM client interface instructs the IM client to output the string of characters associated with the reply function and to perform an action associated with the reply function.
    • 一种用于向即时消息(IM)客户端中的接口添加可定制回复功能的方法,包括以下步骤:识别要与回复功能相关联的字符串,选择IM客户端与回复相关联的动作 功能,在IM客户端的接口中选择应答功能的表示的呈现特征,并将回复功能合并到IM客户端的接口中,其中随后的用户选择IM客户端中回复功能的并入表示 接口指示IM客户端输出与回复功能相关联的字符串,并执行与回复功能相关联的动作。
    • 4. 发明授权
    • Olefin plant recovery system employing catalytic distillation
    • 采用催化蒸馏的烯烃装置回收系统
    • US5679241A
    • 1997-10-21
    • US442954
    • 1995-05-17
    • Stephen J. StanleyFrancis D. McCarthyCharles SumnerGary Robert Gildert
    • Stephen J. StanleyFrancis D. McCarthyCharles SumnerGary Robert Gildert
    • C10G7/00C10G45/00C10G45/32C10G70/02
    • C10G7/00C10G45/00C10G45/32C10G70/02
    • The C.sub.2 to C.sub.5 and heavier acetylenes and dienes in a thermally cracked feed stream are hydrogenated without significantly hydrogenating the C.sub.2 and C.sub.3 olefins. Additionally, the C.sub.4 and heavier olefins may be hydrogenated. Specifically, the cracked gas feed in an olefin plant is hydrogenated in a distillation reaction column containing a hydrogenation catalyst without the necessity of separating the hydrogen out of the feed and without any significant hydrogenation of the ethylene and propylene. A combined reaction-fractionation step known as catalytic distillation hydrogenation is used to simultaneously carry out the reactions and separations while maintaining the hydrogenation conditions such that the ethylene and propylene remain substantially un-hydrogenated and essentially all of the other C.sub.2 and heavier unsaturated hydrocarbons are hydrogenated. Any unreacted hydrogen can be separated by a membrane and then reacted with separated C.sub.9 and heavier materials to produce hydrogenated pyrolysis gasoline.
    • 在热裂化的进料流中的C2至C5和较重的炔和二烯被氢化而不显着氢化C2和C3烯烃。 此外,C4和较重的烯烃可以被氢化。 具体地说,在含有氢化催化剂的蒸馏反应塔中,将烯烃装置中的裂化气进料氢化,而不需要将氢气从进料中分离出来,而乙烯和丙烯没有明显的氢化作用。 使用称为催化蒸馏氢化的组合反应分级步骤同时进行反应和分离,同时保持氢化条件,使得乙烯和丙烯保持基本上未氢化,并且基本上所有其它C2和较重不饱和烃均被氢化 。 任何未反应的氢气可以通过膜分离,然后与分离的C9和较重的材料反应,生成氢化裂解汽油。