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    Methods and equipment for hydrothermal processing and disposal of highly toxic substances, waste and metal powders
    16.
    发明授权
    Methods and equipment for hydrothermal processing and disposal of highly toxic substances, waste and metal powders 有权
    水热处理和处置高毒性物质，废物和金属粉末的方法和设备

    公开(公告)号：US09352178B2

    公开(公告)日：2016-05-31

    申请号：US14650478

    申请日：2013-12-06

    Applicant: HYDROTHERMA SWISS ECOLOGICAL TECHNOLOGIES SA

    Inventor： Valeriy Surovtsev

    IPC: A62D3/20 ,  B01J19/24 ,  B01J3/00 ,  B01J4/00 ,  B01J4/02 ,  A62D101/02

    CPC classification number: A62D3/20 ,  A62D2101/02 ,  B01J3/008 ,  B01J4/002 ,  B01J4/02 ,  B01J19/24 ,  B01J2219/00029 ,  B01J2219/00031 ,  B01J2219/00038 ,  B01J2219/00051 ,  B01J2219/00123 ,  B01J2219/00135 ,  B01J2219/00155 ,  B01J2219/24 ,  Y02P20/544

    Abstract: A method of hydrothermal processing of highly toxic substances, wastes and metal powders, comprises a batch processing cycle of at least following steps i. to viii: i. preparing a batch of highly toxic waste, substances and metal powders for processing; ii. applying precision dozing to the batch to obtain a mixture of the batch with water and at least one additional reagent in preset proportions; iii. feeding the mixture into a reactor; iv. spraying the mixture inside the reactor with a mechanical spray nozzle; v. supplying an additional oxidizing agent inside the reactor; vi. adjusting a temperature inside the reactor to above 374.2° C.; vii. adjusting a pressure inside the reactor to above 21.8 MPa, thereby driving the water into supercritical condition and initiating a supercritical hydrothermal oxidation process; and viii. keeping the mixture in the reactor for a preset amount of time, and at the same time. The method further comprises removing a produced steam and hydrogen mixture from the reactor via a steam-gas unit and droplet separator into a wastewater condenser unit and a gas drainage pipe, and venting suspended solids through a bottom part of the reactor into a solids collector unit. The method then provides the steps of repeating the batch processing cycle after it has terminated; and monitoring and controlling the temperature and pressure inside the reactor via an Automatic Process Control System (APCS) during all steps.

    Abstract translation: 对高毒性物质，废物和金属粉末进行水热处理的方法包括至少以下步骤i的批处理循环。 到viii：i。 制备一批高毒性废物，物质和金属粉末进行加工; ii。 对批料施加精密打瞌睡以获得预定比例的批次与水和至少一种另外的试剂的混合物; iii。 将混合物进料到反应器中; iv。 用机械喷嘴将反应器内的混合物喷雾; v。在反应器内部供应另外的氧化剂; vi。 将反应器内的温度调节到374.2℃以上。 vii。 将反应器内的压力调节到21.8MPa以上，从而将水驱动到超临界状态，开始超临界水热氧化工艺; 和viii。 将混合物保持在反应器中预定的时间量，同时。 所述方法还包括通过蒸汽 - 气体单元和液滴分离器将产生的蒸汽和氢气混合物从反应器中移出到废水冷凝器单元和排气管中，并将悬浮固体通过反应器的底部排放到固体收集器单元 。 该方法然后提供在终止后重复批处理循环的步骤; 并在所有步骤中通过自动过程控制系统（APCS）监视和控制反应堆内的温度和压力。

    Microfluidic test carrier for apportioning a liquid quantity into subquantities
    17.
    发明授权
    Microfluidic test carrier for apportioning a liquid quantity into subquantities 有权
    用于将液体量分配到子量的微流体测试载体

    公开(公告)号：US09186671B2

    公开(公告)日：2015-11-17

    申请号：US13871720

    申请日：2013-04-26

    Applicant: Roche Diagnostics Operations, Inc.

    Inventor： Manfred Augstein ,  Christoph Boehm ,  Susanne Wuerl

    IPC: B01L3/00 ,  B01J4/02

    CPC classification number: B01L3/50273 ,  B01L3/502723 ,  B01L3/502738 ,  B01L2200/027 ,  B01L2200/0605 ,  B01L2200/0642 ,  B01L2200/0684 ,  B01L2200/141 ,  B01L2300/0806 ,  B01L2300/0851 ,  B01L2300/087 ,  B01L2400/0409 ,  B01L2400/0688

    Abstract: A microfluidic test carrier having a substrate, covering layer, and capillary structure formed in the substrate is provided. The capillary structure is enclosed by the substrate and covering layer and comprises a receiving chamber, sample chamber and connection channel between the receiving and sample chambers. The receiving chamber has two boundary surfaces and a side wall, wherein one boundary surface forms the bottom and the other forms the cover. The receiving chamber has a surrounding venting channel and dam between the receiving chamber and venting channel. The dam and venting channel form a capillary stop configured as a geometric valve, through which air from the receiving chamber can escape into the venting channel. The connecting channel between the venting channel outflow and sample chamber inflow controls fluid transport from the receiving chamber into the sample chamber. The capillary stop is configured to prevent autonomous fluid transport from the receiving chamber.

    Abstract translation: 提供了一种在基板上形成的具有基板，覆盖层和毛细结构的微流体测试载体。 毛细管结构由衬底和覆盖层包围，并包括接收室，样品室和接收室和样品室之间的连接通道。 接收室具有两个边界面和侧壁，其中一个边界表面形成底部，另一个形成盖。 接收室具有周围的通风通道，并且在接收室和通风通道之间具有阻塞。 大坝和排气通道形成一个被设计为几何阀的毛细管阻塞，来自接收室的空气可以通过该几何阀排出到通风通道中。 排气通道出口和样品室流入之间的连接通道控制从接收室进入样品室的流体输送。 毛细管止动件被构造成防止自主流体从接收室输送。

    Mobile fluid catalytic cracking injection system
    19.
    发明申请
    Mobile fluid catalytic cracking injection system 有权
    流动催化裂化注射系统

    公开(公告)号：US20050103684A1

    公开(公告)日：2005-05-19

    申请号：US10717249

    申请日：2003-11-19

    Applicant: Martin Evans

    Inventor： Martin Evans

    IPC: B01J20060101 ,  B01J4/02 ,  B01J8/00 ,  C10G11/00 ,  C10G11/18 ,  F02M25/10 ,  F02M25/12

    CPC classification number: B01J8/0015 ,  B01J2208/00752 ,  C10G11/18 ,  C10G2300/4062 ,  F02M25/10 ,  F02M25/12

    Abstract: A mobile fluid cracking catalyst injection system and a method of controlling a fluid catalyst cracking process is provided. In one embodiment, a mobile fluid catalyst cracking system includes a transportable platform, a catalyst reservoir coupled to the platform and a flow control device coupled to an outlet of the reservoir and adapted to control the flow of catalyst from the reservoir to a fluid catalyst cracking unit (FCCU).

    Abstract translation: 提供了一种移动流体裂化催化剂注入系统和一种控制流体催化剂裂解过程的方法。 在一个实施例中，移动流体催化剂裂解系统包括可移动平台，耦合到平台的催化剂储存器和耦合到储存器的出口的流量控制装置，并且适于控制催化剂从储存器到流体催化剂裂解的流动 单位（FCCU）。

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