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    • 3. 发明申请
    • EXTENDED LENGTH STRAND TAKE UP DEVICE
    • 延长的长度使用设备
    • US20060151761A1
    • 2006-07-13
    • US10924492
    • 2004-08-24
    • James Stevens
    • James Stevens
    • B21F9/00
    • B25B25/00F16B7/06Y10T403/32221
    • An extended length strand take up device comprises at least two tension rods disposed in parallel spaced relationship to one another, and a first connecting body slidably mounted on the tension rods for connecting the extended length strand take up device to a guy wire, and a second a first connecting body slidably mounted on the tension rods for connecting the extended length strand take up device to a ground anchor. The first and second connecting bodies each include at least two side load tubes interconnected by a central web, each side load tube being slidably disposed on a respective one of said tension rods. A stop member at each end of said tension rods retains the first and second connecting bodies on the tension rods.
    • 延长长度的卷取装置包括彼此平行间隔设置的至少两个张力杆,以及可滑动地安装在张力杆上的第一连接体,用于将延长长度的绳索卷绕装置连接到家具线,第二连接体 第一连接体可滑动地安装在张力杆上,用于将延伸长度的绳索卷绕装置连接到地锚上。 第一和第二连接体各自包括通过中心腹板互连的至少两个侧向负载管,每个侧面负载管可滑动地设置在所述张力杆的相应一个上。 所述张力杆的每一端处的止动构件将第一和第二连接体保持在张力杆上。
    • 10. 发明申请
    • Apparatus and method for hydrogen generation
    • 用于氢气生成的装置和方法
    • US20050229489A1
    • 2005-10-20
    • US10827187
    • 2004-04-19
    • Farshad BavarianJames Stevens
    • Farshad BavarianJames Stevens
    • C01B3/24C01B3/38C01B3/50C01B3/56
    • C01B3/56C01B3/38C01B3/508C01B2203/0227C01B2203/0233C01B2203/0283C01B2203/0425C01B2203/0475C01B2203/1241C01B2203/127
    • Apparatus and method for converting hydrocarbon fuels to hydrogen-rich reformate that incorporate a carbon dioxide fixing mechanism into the initial hydrocarbon conversion process. The mechanism utilizes a carbon dioxide fixing material within the reforming catalyst bed to remove carbon dioxide from the reformate product. The bed optionally contains a water gas shift catalyst. The removal of carbon dioxide from the product stream shifts the reforming reaction and shift reaction equilibria toward production of higher concentrations of hydrogen with only small amounts of carbon oxides produced. The carbon oxide-depleted reformate is directed to a purification bed comprising a hydrogen fixing material that removes hydrogen from the reformate stream to provide fixed hydrogen and a hydrogen-depleted reformate that flows out of the purification bed. The purification bed is heated to release fixed hydrogen from the hydrogen fixing material to provide a highly pure hydrogen gas.
    • 将碳氢化合物燃料转化为富含氢的重整产物的装置和方法,其将二氧化碳固定机构并入初始烃转化过程。 该机构利用重整催化剂床内的二氧化碳固定材料从重整产品中除去二氧化碳。 该床任选地含有水煤气变换催化剂。 从产物流中除去二氧化碳使重整反应和转化反应平衡转向生产较高浓度的氢气,只产生少量的碳氧化物。 不含氧化碳的重整产品涉及一种净化床,该纯化床包含从重整产品流中除去氢气以提供固定氢气的氢固定材料,以及从净化床流出的贫氢重整产品。 净化床被加热以从氢固定材料释放固定的氢气以提供高纯度的氢气。