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    • 4. 发明申请
    • DROPLET COUNTING AND MEASURING DEVICE
    • 倒角计数和测量装置
    • US20120154787A1
    • 2012-06-21
    • US13393641
    • 2010-09-03
    • Michael Brady
    • Michael Brady
    • G01P3/36G01N15/14
    • G01N15/1459
    • The present invention is a device to measure the characteristics of droplets within a stream of liquid droplets used in spraying. It comprises: a light source (45) supplying light across the stream of droplets; detection (means 2) to detect change in the light level caused by a passing droplet, the detection means generating a signal according to the change in light; and processing means (59) to analyse the characteristics of the droplets in the stream based on the signal produced by the detection means. The light passes through a slit (3A) in a panel (53) disposed between the droplet stream and the detection means (52), so that the change in level of light detected by the detection means is proportional to the diameter of the droplet. Preferably two or more intersecting light beams (68,69) are used to provide comparative data about passing droplets.
    • 本发明是用于测量在喷雾中使用的液滴流内的液滴的特性的装置。 它包括:一个光源(45),用于在液滴流上提供光; 检测(装置2),检测由通过的液滴引起的光级的变化,检测装置根据光的变化产生信号; 以及基于由检测装置产生的信号来分析流中的液滴的特性的处理装置(59)。 光通过设置在液滴流和检测装置(52)之间的面板(53)中的狭缝(3A),使得由检测装置检测的光的变化与液滴的直径成比例。 优选地,使用两个或更多个相交光束(68,69)来提供关于通过液滴的比较数据。
    • 6. 发明授权
    • Biomass conversion process
    • 生物质转换过程
    • US08003835B2
    • 2011-08-23
    • US12606804
    • 2009-10-27
    • Steve YanikRobert BartekPaul O'ConnorDennis StamiresMichael Brady
    • Steve YanikRobert BartekPaul O'ConnorDennis StamiresMichael Brady
    • C07C1/00F27B15/08
    • C10G1/08C10B49/22C10B53/02C10B57/02C10G1/006C10G3/42C10G3/57Y02E50/14Y02E50/32Y02P20/145Y02P30/20
    • A method for converting solid biomass into hydrocarbons includes contacting the solid biomass with a catalyst in a first riser operated at a temperature in the range of from about 50° C. to about 200° C. to thereby produce a first biomass-catalyst mixture and a first product comprising hydrocarbons; a) separating the first product from the first biomass-catalyst mixture; c) charging the first biomass-catalyst mixture to a second riser operated at a temperature in the range of from about 200° C. to about 400° C. to thereby produce a second biomass-catalyst mixture and a second product comprising hydrocarbons; d) separating the second product from the second biomass-catalyst mixture; e) charging the second biomass-catalyst mixture to a third riser operated at a temperature greater than about 450° C. to thereby produce a spent catalyst and a third product comprising hydrocarbons; and f) separating the third effluent from the spent catalyst.
    • 将固体生物质转化为烃的方法包括使固体生物质与在约50℃至约200℃的温度下操作的第一提升管中的催化剂接触,从而产生第一生物质 - 催化剂混合物, 包含烃的第一产物; a)将第一产物与第一生物质 - 催化剂混合物分离; c)将第一生物质 - 催化剂混合物装载到在约200℃至约400℃的温度范围内操作的第二提升管,从而产生第二生物质 - 催化剂混合物和包含烃的第二产物; d)将第二产物与第二生物质 - 催化剂混合物分离; e)将第二生物质 - 催化剂混合物装入在大于约450℃的温度下操作的第三提升管,从而产生废催化剂和包含烃的第三产物; 和f)将第三流出物与废催化剂分离。