PROCESS AND APPARATUS FOR FLUID CATALYTIC CRACKING
    81.
    发明申请
    PROCESS AND APPARATUS FOR FLUID CATALYTIC CRACKING 审中-公开
    流体催化裂化的工艺和装置

    公开(公告)号:US20140364300A1

    公开(公告)日:2014-12-11

    申请号:US14465268

    申请日:2014-08-21

    Applicant: UOP LLC

    Inventor: Paolo Palmas

    Abstract: One exemplary embodiment can be a process for fluid catalytic cracking. The process can include sending a first catalyst from a first riser reactor and a second catalyst from a second riser reactor to a regeneration vessel having a first stage and a second stage. The first catalyst may be sent to the first stage and the second catalyst may be sent to the second stage of the regeneration vessel. Generally, the first stage is positioned above the second stage.

    Abstract translation: 一个示例性实施方案可以是流化催化裂化的方法。 该方法可以包括将第一催化剂从第一提升管反应器和第二催化剂从第二提升管反应器送到具有第一阶段和第二阶段的再生容器。 可将第一催化剂送至第一阶段,第二催化剂可送至再生容器的第二阶段。 通常,第一阶段位于第二阶段之上。

    Gas-liquid-solid three-phase suspension bed reactor for fischer-tropsch synthesis and its applications
    84.
    发明授权
    Gas-liquid-solid three-phase suspension bed reactor for fischer-tropsch synthesis and its applications 有权
    用于费托合成的气液固相三相悬浮床反应器及其应用

    公开(公告)号:US08506895B2

    公开(公告)日:2013-08-13

    申请号:US12527355

    申请日:2007-10-12

    Abstract: A Fischer-Tropsch synthesis three-phase suspension bed reactor (“suspension bed” also called “slurry bed”) and its supplemental systems, may include: 1) structure and dimension design of F-T synthesis reactor, 2) a gas distributor located at the bottom of the reactor, 3) structure and arrangement of a heat exchanger members inside the reactor, 4) a liquid-solid filtration separation device inside reactor, 5) a flow guidance device inside reactor, 6) a condensate flux and separation member located in the gas phase space at the top of reactor, 7) a pressure stabilizer, a cleaning system for the separation device; an online cleaning system for the gas distributor; an ancillary system for slurry deposition and a pre-condensate and mist separation system located at the outlet of upper reactor. This reactor is suitable for industrial scale application of Fischer-Tropsch synthesis.

    Abstract translation: 费 - 托合成三相悬浮床反应器(“悬浮床”也称为“浆料床”)及其补充系统可包括:1)FT合成反应器的结构和尺寸设计,2)位于 反应器底部,3)反应器内部的热交换器部件的结构和布置; 4)反应器内部的液固过滤分离装置; 5)反应器内的流动引导装置,6)位于 反应器顶部的气相空间,7)压力稳定器,分离装置的清洗系统; 用于气体分配器的在线清洁系统; 用于浆料沉积的辅助系统和位于上反应器出口处的预冷凝和雾化分离系统。 该反应器适用于费 - 托合成的工业规模应用。

    Moving bed reactor for solar thermochemical fuel production
    85.
    发明授权
    Moving bed reactor for solar thermochemical fuel production 有权
    太阳能热化学燃料生产移动床反应堆

    公开(公告)号:US08420032B1

    公开(公告)日:2013-04-16

    申请号:US13220321

    申请日:2011-08-29

    Applicant: Ivan Ermanoski

    Inventor: Ivan Ermanoski

    Abstract: Reactors and methods for solar thermochemical reactions are disclosed. Embodiments of reactors include at least two distinct reactor chambers between which there is at least a pressure differential. In embodiments, reactive particles are exchanged between chambers during a reaction cycle to thermally reduce the particles at first conditions and oxidize the particles at second conditions to produce chemical work from heat. In embodiments, chambers of a reactor are coupled to a heat exchanger to pre-heat the reactive particles prior to direct exposure to thermal energy with heat transferred from reduced reactive particles as the particles are oppositely conveyed between the thermal reduction chamber and the fuel production chamber. In an embodiment, particle conveyance is in part provided by an elevator which may further function as a heat exchanger.

    Abstract translation: 公开了用于太阳热化学反应的反应器和方法。 反应器的实施方案包括至少两个不同的反应室,其间至少存在压力差。 在实施方案中,反应性颗粒在反应循环期间在室之间交换以在第一条件下热还原颗粒,并在第二条件下氧化颗粒以从热产生化学作用。 在实施方案中,反应器的室联接到热交换器以在直接暴露于热能之前预热加热反应性颗粒,同时随着颗粒在热还原室和燃料产生室之间相反地输送而从降低的反应性颗粒转移的热量 。 在一个实施例中,颗粒输送部分由电梯提供,其可以进一步起到热交换器的作用。

    HYDROCARBON CONVERSION METHOD AND APPARATUS
    86.
    发明申请
    HYDROCARBON CONVERSION METHOD AND APPARATUS 审中-公开
    石油转化方法和装置

    公开(公告)号:US20130079571A1

    公开(公告)日:2013-03-28

    申请号:US13244006

    申请日:2011-09-23

    Abstract: One exemplary embodiment can be a hydrocarbon conversion method. Generally, the method includes providing a hydrocarbon stream having one or more C10-C14 hydrocarbons to a hydroprocessing zone and a donor solvent stream at least partially obtained from the hydroprocessing zone to a slurry hydrocracking zone. The hydroprocessing zone may have a vessel containing an internal riser. Usually, a hydroprocessing catalyst circulates within the vessel by at least partially rising within the internal riser.

    Abstract translation: 一个示例性实施方案可以是烃转化方法。 通常,该方法包括向加氢处理区提供具有一个或多个C 10 -C 14烃的烃流和至少部分地从加氢处理区获得的供体溶剂流至浆料加氢裂化区。 加氢处理区可以具有容纳内部提升管的容器。 通常,加氢处理催化剂在内部提升管内至少部分地升高在容器内循环。

    Fluidization device for solid fuel particles
    87.
    发明授权
    Fluidization device for solid fuel particles 有权
    固体燃料颗粒流化装置

    公开(公告)号:US08377387B2

    公开(公告)日:2013-02-19

    申请号:US12822132

    申请日:2010-06-23

    Abstract: A system includes a fluidization device including a flow passage configured to convey a flow of solid fuel particles in a downstream direction, and a body disposed within the flow passage. The body is configured to direct the flow of solid fuel particles between the body and an outer wall of the flow passage. The fluidization device also includes a carrier gas injection port positioned radially outward from the body. The carrier gas injection port is configured to provide a flow of carrier gas in the downstream direction to break up agglomerations within the flow of solid fuel particles.

    Abstract translation: 一种系统包括:流化装置,其包括构造成沿下游方向输送固体燃料颗粒流的流路,以及设置在流路内的主体。 主体构造成引导固体燃料颗粒在主体和流动通道的外壁之间的流动。 流化装置还包括从主体径向向外定位的载气注入口。 载气注入口构造成在下游方向提供载气流,以破坏固体燃料颗粒流中的团聚。

    Heat recovery system
    88.
    发明授权
    Heat recovery system 有权
    热回收系统

    公开(公告)号:US08354070B2

    公开(公告)日:2013-01-15

    申请号:US12672123

    申请日:2009-07-28

    CPC classification number: G07F17/323 G07F17/32 G07F17/3234

    Abstract: A moving disk type tube reactor for continuously pyrolyzing waste tire chips and preventing accumulation of remainders produced by pyrolysis, includes: a heating tube having at the ends thereof inflow and outflow ports for allowing high-temperature gas to flow; a first transfer tube penetrating the heating tube and having an input port for inputting the chips at one end thereof; a second transfer tube disposed parallel to the first transfer tube; a driving part disposed at the other end of the first and second transfer tubes, having a driving sprocket driven by a driving motor, and having a discharge port discharging oil vapor; a driven part disposed at one end of the transfer tubes, having a driven sprocket and a discharge port discharging pyrolyzed carbon black to the outside; a chain penetrating the transfer tubes and wound on the sprockets to circulate; and a plurality of disks along the chain.

    Abstract translation: 一种移动盘式管式反应器,用于连续热解废轮胎片并防止由热解产生的残余物积聚,包括:加热管,其端部具有允许高温气体流动的流出口; 穿过加热管并具有用于在其一端输入芯片的输入端口的第一输送管; 平行于第一输送管设置的第二输送管; 驱动部,其设置在所述第一和第二输送管的另一端,具有由驱动电动机驱动的驱动链轮,并且具有排出油蒸气的排出口; 驱动部分设置在转移管的一端,具有从动链轮和排出热解炭黑的排出口到外部; 链条穿透传送管并缠绕在链轮上循环; 以及沿着链条的多个盘。

    Actuator for moving a movable body by electrowetting
    89.
    发明授权
    Actuator for moving a movable body by electrowetting 有权
    用于通过电润湿移动可移动体的致动器

    公开(公告)号:US08349150B2

    公开(公告)日:2013-01-08

    申请号:US11861633

    申请日:2007-09-26

    Inventor: Hiroto Sugahara

    CPC classification number: H02N11/006 H02N1/004

    Abstract: An actuator includes a fixed including a substrate, electrodes disposed on a surface of the substrate, and an insulating layer disposed on the surface of the substrate to cover the electrodes. The actuator includes an electrically conductive, liquid member disposed on and contacting a surface of the insulating layer, a movable body contacting the liquid member, a retaining device configured to adhere the liquid member to the movable body, a device configured to apply potential to each of the electrodes, and a controller configured to control the device. The controller controls the device to change potential applied to each of the electrodes to vary liquid repellency of the insulating layer in response to potential difference applied between each of the electrodes and the liquid member to change at least one of a contact portion between the liquid member and the insulating layer and a contact area of the liquid member contacting on the surface of the insulating layer, to move the movable body relative to the fixed body.

    Abstract translation: 致动器包括固定体,其包括基板,设置在基板的表面上的电极以及设置在基板的表面以覆盖电极的绝缘层。 所述致动器包括布置在所述绝缘层的表面上并且接触所述绝缘层的表面的导电液体部件,与所述液体部件接触的可移动体,构造成将所述液体部件粘附到所述可移动体的保持装置, 的电极,以及被配置为控制所述装置的控制器。 控制器控制装置改变施加到每个电极的电位,以响应于在每个电极和液体构件之间施加的电位差​​来改变绝缘层的拒水性,以改变液体构件之间的接触部分中的至少一个 所述绝缘层和与所述绝缘层的表面接触的所述液体构件的接触面相对于所述固定体移动。

    Compact two-stage granular moving-bed apparatus
    90.
    发明授权
    Compact two-stage granular moving-bed apparatus 有权
    紧凑型两级颗粒移动床设备

    公开(公告)号:US08343430B2

    公开(公告)日:2013-01-01

    申请号:US13087066

    申请日:2011-04-14

    Abstract: A compact two-stage granular moving-bed apparatus comprises a vessel, a flow-corrective element, and a filter material supplying part. The vessel comprises a hollow interior, a gas outlet, a first media outlet and a second media outlet. The flow-corrective element divides the hollow interior into a first channel and a second channel. The filter material supplying part has a first provider for providing a first granular material flowing through the first channel and a second provider for providing a second granular material flowing through the second channel, wherein a vertical level of each first and second provider is adjustable so that a first flow path that an exhaust gas flows through the first granular material and a second flow path that the exhaust gas flow through the second granular material is respectively capable of being controlled.

    Abstract translation: 紧凑的两级粒状移动床装置包括容器,流量校正元件和过滤材料供应部件。 容器包括中空的内部,气体出口,第一介质出口和第二介质出口。 流量校正元件将中空内部分成第一通道和第二通道。 过滤材料供应部分具有用于提供流过第一通道的第一颗粒材料的第一供应器和用于提供流过第二通道的第二颗粒材料的第二供应器,其中每个第一和第二供应商的垂直水平是可调节的,使得 废气流过第一颗粒材料的第一流动路径和分别能够控制废气流过第二颗粒材料的第二流动路径。

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