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    • 65. 发明申请
    • SYSTEM, METHOD, AND COMPUTER PRODUCT FOR EXON ARRAY ANALYSIS
    • 用于外部阵列分析的系统,方法和计算机产品
    • US20060275805A1
    • 2006-12-07
    • US11421941
    • 2006-06-02
    • Alan WilliamsCharles SugnetJames Gorrell
    • Alan WilliamsCharles SugnetJames Gorrell
    • C12Q1/68G06F19/00
    • G06F19/20
    • In one embodiment, a method for analyzing data generated by probe arrays is described that comprises receiving user selections of two or more data files and an identification of one or more subsets of intensity values acquired from a biological probe array. The method includes iteratively opening each data file, identifying the selected subset of intensity values associated with each open data file, determining parameters for processing, storing the parameters and the identified intensity values, and closing the open data file prior to the subsequent iteration. The method then includes processing the stored intensity values using the parameters to identify one or more biological events.
    • 在一个实施例中,描述了一种用于分析由探针阵列产生的数据的方法,其包括接收两个或多个数据文件的用户选择以及从生物探针阵列获取的一个或多个强度值子集的识别。 该方法包括迭代地打开每个数据文件,识别与每个打开的数据文件相关联的所选择的强度值子集,确定用于处理,存储参数和识别的强度值的参数,以及在随后的迭代之前关闭打开的数据文件。 该方法然后包括使用参数来处理存储的强度值以识别一个或多个生物事件。
    • 68. 发明授权
    • Gas making
    • 制气
    • US4417905A
    • 1983-11-29
    • US173718
    • 1980-07-30
    • Reginald G. S. BanksAlan Williams
    • Reginald G. S. BanksAlan Williams
    • C10L3/06B01J23/755B01J37/03C10G11/20C01B2/14
    • C01B3/40B01J23/755B01J37/03C10G11/02C01B2203/0233C01B2203/1058Y02P20/52
    • Methane-containing gases are produced by passing a hydrocarbon feedstock having a boiling point of not greater than 350.degree. C. and steam over a catalyst at an elevated pressure and at a temperature of from 350.degree. C. to 550.degree. C. at the inlet of the catalyst and an exit of temperature of at least 450.degree. C., the catalyst comprising a reduced catalyst precursor which is resistant to deactivation by polymer formation or by sintering, the catalyst precursor containing (1) from 0 to not more than 0.43% K and from 0 to not more than 0.1% Na, (2) the combined weights of Na+ K does not exceed 0.011 gm atoms/100 gm of catalyst precursor, (3) the ratio of Na:K falls within the area defined by ABCDEO in FIG. 1 of the drawings, and (3) at combined Na+ K weights of from 0 to 0.05% the water loss is not more than 11.2%.
    • 含甲烷的气体是通过使沸点不高于350℃的烃原料和在催化剂上的蒸汽在升高的压力下和在350℃至550℃的温度下在入口 催化剂的出口温度为至少450℃,催化剂包含还原催化剂前体,其通过聚合物形成或通过烧结而失活,所述催化剂前体含有(1)0至不大于0.43% K,从0到不大于0.1%的Na,(2)Na + K的组合重量不超过0.011gm原子/ 100g催化剂前体,(3)Na:K的比例落在ABCDEO 在图中。 1),(3)组合Na + K重量为0〜0.05%,失水量不超过11​​.2%。