Hockey puck with centrally disposed spherical element
    43.
    发明授权
    Hockey puck with centrally disposed spherical element 失效
    曲棍球与中央布置的球形元素

    公开(公告)号:US5976042A

    公开(公告)日:1999-11-02

    申请号:US974133

    申请日:1997-11-19

    IPC分类号: A63B67/14 A63B71/02

    摘要: A hockey puck has a generally cylindrical body having an upper face, a lower face and a circumferential wall with a generally spherical puck element secured centrally within the body and being rotatable with respect to the puck body. In a preferred embodiment, the generally spherical puck element has a weight greater than that of the body and a diameter greater than the distance between the upper face and lower face. The generally spherical puck element is secured within an inner member which in turn has a ring disposed radially outwardly thereof and secured to the inner member. The puck is structurally designed to have the generally spherical puck element have translational and rotational kinetic energy while the body will have translational or translational and rotational kinetic energy. This results an enhanced ability to maintain the puck on the desired path despite roughness of the surface on which it is moving or certain types of impact with other objects.

    摘要翻译: 曲棍球盘具有通常为圆柱形的主体,其具有上表面,下表面和圆周壁,其具有大致球形的圆盘形元件,其中心地固定在主体内并且可相对于圆盘体旋转。 在优选实施例中,大致球形的圆盘形元件的重量大于主体的重量,其直径大于上表面和下表面之间的距离。 大致球形的圆盘形元件固定在内部构件中,该内部构件又具有径向向外设置并固定到内部构件的环。 冰球在结构上被设计成具有通常球形的圆盘元件具有平移和旋转的动能,而身体将具有平移或平移和旋转的动能。 这导致了增强的能力,即将其固定在所需的路径上,尽管其移动的表面的粗糙度或与其他物体的某些类型的冲击。

    Multi-stage hydrodesulfurization and hydrogenation process for
distillate hydrocarbons
    44.
    发明授权
    Multi-stage hydrodesulfurization and hydrogenation process for distillate hydrocarbons 失效
    馏分烃多级加氢脱硫和氢化方法

    公开(公告)号:US5110444A

    公开(公告)日:1992-05-05

    申请号:US562365

    申请日:1990-08-03

    IPC分类号: C10G65/08

    CPC分类号: C10G65/08

    摘要: Middle distillate petroleum streams are hydrotreated to produce a low sulfur and low aromatic product in a process employing three reaction zones in series. Hydrogen flows between the reaction zones countercurrent to the hydrocarbons. Hydrogen sulfide is removed from effluent of the first two reaction zones by hydrogen stripping. The second and third reaction zones employ a sulfur-sensitive noble metal hydrogenation catalyst. Operating pressure increases and temperature decreases from the first to third reaction zones.

    摘要翻译: 在采用三个反应区串联的过程中,将中间馏分石油气流加氢处理以产生低硫和低芳族化合物。 反应区之间的氢气与碳氢化合物逆流。 通过氢气汽提将硫化氢从前两个反应区的流出物中除去。 第二和第三反应区采用硫敏感的贵金属加氢催化剂。 工作压力升高,温度从第一到第三反应区域减少。

    Elimination of caustic prewash in the fixed bed sweetening of high
naphthenic acids hydrocarbons
    45.
    发明授权
    Elimination of caustic prewash in the fixed bed sweetening of high naphthenic acids hydrocarbons 失效
    消除苛性预洗在固定床中的高环烷酸碳氢化合物

    公开(公告)号:US5039398A

    公开(公告)日:1991-08-13

    申请号:US495245

    申请日:1990-03-19

    IPC分类号: C10G27/10

    CPC分类号: C10G27/10

    摘要: Although high naphthenic acid hydrocarbon feedstocks normally need to be washed with caustic prior to being sweetened in a fixed bed mercaptan-to-disulfide oxidation process to avoid bed plugging, the prewash can be eliminated if aqueous ammonia is used concurrent with and as a part of the sweetening process. Aqueous ammonia injected into a sour hydrocarbon stream prior to the sweetening zone not only eliminates bed plugging, but affords an aqueous phase from which naphthenic acids may be recovered easily and economically. The ammonia also can be recovered for reuse, affording a process with considerably enhanced economic return.

    摘要翻译: 虽然高环烷酸烃原料通常需要在固定床硫醇 - 二硫化物氧化过程中被硫化之前用苛性碱洗涤以避免堵塞,但是如果使用氨水并与其作为一部分 甜味过程。 在甜味区之前注入酸性烃流中的氨水不仅消除了床堵塞,而且提供了一种水相,可以容易且经济地回收环烷酸。 氨还可以回收再利用,提供了显着提高经济回报的过程。

    Glucose or maltose from starch
    46.
    发明授权
    Glucose or maltose from starch 失效
    来自淀粉的葡萄糖或麦芽糖

    公开(公告)号:US4594322A

    公开(公告)日:1986-06-10

    申请号:US608837

    申请日:1984-05-10

    摘要: A process for obtaining glucose from thinned starch by partially hydrolyzing the latter to give from 50% to 92% glucose followed by separation of the hydrolysis product to afford a glucose-enriched product with recycling of the glucose-depleted stream affords benefits unattainable by conventional commercial processes. Substantial reductions in process time and reversion products and a substantial increase in productivity are among some of the benefits.

    摘要翻译: 通过部分水解后者得到葡萄糖从50%至92%葡萄糖中获得葡萄糖的方法,然后分离水解产物以提供富含葡萄糖的流的葡萄糖富集产物,从而获得常规商业无法实现的益处 过程。 处理时间大幅度减少和回收产品以及生产率的大幅提高也是其中的一个好处。

    Catalyst regeneration apparatus
    47.
    发明授权
    Catalyst regeneration apparatus 失效
    催化剂再生装置

    公开(公告)号:US4285908A

    公开(公告)日:1981-08-25

    申请号:US101295

    申请日:1979-12-07

    摘要: A catalyst regeneration apparatus for the oxidation of coke from a spent catalyst, said coke being converted to CO, and for the conversion of the CO to CO.sub.2. Hot regenerated catalyst is recycled from a dense bed in the regeneration zone to mix with incoming spent catalyst in a mixer zone. The mixer zone operates in dense phase and is supplied with a relatively small amount of a fluidizing medium, preferably air. After the mixing of spent and fresh catalyst is substantially completed, a relatively large amount of a regenerating gas, preferably air, is admixed with the catalyst mixture, and some coke oxidation occurs. The balance of coke oxidation takes place in a downstream-situated regeneration zone of substantially conventional design. There is a transfer section connecting the mixer zone to the regeneration zone through which the relatively large amount of the regenerating gas is admitted. The transfer section is preferably a frustoconical surface, the horizontal cross section of smallest perimeter of which adjoins the outlet of said mixer zone, and regenerating gas addition is made at the base of the transfer section in order to provide a venturi effect which ensures good air-catalyst mixing.

    摘要翻译: 一种用于从废催化剂氧化焦炭的催化剂再生装置,所述焦炭转化为CO,并将CO转化为CO 2。 热再生催化剂从再生区中的致密床再循环,以在混合区中与进入的废催化剂混合。 混合器区域以密相工作,并且供应相对少量的流化介质,优选空气。 在废旧催化剂的混合基本上完成之后,将相当大量的再生气体,优选空气与催化剂混合物混合,并发生一些焦炭氧化。 焦炭氧化的平衡发生在基本上常规设计的位于下游的再生区中。 存在将混合器区域连接到再生区域的转移段,通过该再生区域允许相对大量的再生气体。 转印部优选为截头圆锥形表面,其最小周边的水平截面与所述混合区的出口相邻,并且在转印部分的底部形成再生气体添加,以提供确保良好空气的文丘里效应 催化剂混合。