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    Method and Apparatus for the Continuous Controlled Discharge of Solids
    22.
    发明申请
    Method and Apparatus for the Continuous Controlled Discharge of Solids 有权
    固体连续控制放电的方法和装置

    公开(公告)号：US20080244986A1

    公开(公告)日：2008-10-09

    申请号：US11587709

    申请日：2005-04-01

    Applicant: Dieter Adelmann ,  Stefan Gerl

    Inventor： Dieter Adelmann ,  Stefan Gerl

    IPC: B01J8/00 ,  H05B3/60

    CPC classification number: B01J8/002 ,  B01J8/003 ,  B01J2208/00061 ,  B01J2208/00415 ,  B01J2208/0061 ,  B01J2208/00752 ,  B01J2219/00191 ,  B65G65/46 ,  B65G65/4881 ,  B65G69/10 ,  H05B3/0009 ,  H05B3/60

    Abstract: It is known that poorly-flowing solid materials can lead to an inhomogeneous mass flow of the solid across the discharge cross-section of a silo. If the solid in the silo is also heated or cooled the uneven mass flow can lead, for example, to local variations in temperature and/or hence to varying product properties. According to the invention, the above problem may be resolved, whereby a method and a discharge device for a solids silo and a solids silo are disclosed, permitting a controllable solids discharge evenly across the cross-section of the silo. The cross-section of the silo discharge is divided into several, preferably equivalent, partial cross-sections to which a continuously controllable discharge device is connected. The solid flow discharged from the controllable discharge devices can be collected on a continuous conveyor arranged therebelow and removed. The even solid mass discharge from the continuous discharge devices is controlled, depending on measured signals from several equivalent sensors, recording the local mass flow in the corresponding partial sections of the silo, by means of the conveyor power of the discharge device, relating to each sensor. Where electrically-conducting solids are used which are to be heated in the silo using electrodes by means of resistance heating, the control of the discharge devices is achieved with the measured current at the electrodes.

    Abstract translation: 已知的是，流动不足的固体材料可能导致固体跨过筒仓的排放横截面的质量流量不均匀。 如果筒仓中的固体也被加热或冷却，则不均匀的质量流动可能导致例如温度的局部变化和/或因此改变产品性质。 根据本发明，可以解决上述问题，由此公开了用于固体筒仓和固体仓的方法和排出装置，允许可控的固体排料均匀地跨过料仓的横截面。 筒仓放电的横截面被分成几个，优选等效的部分横截面，连续可控放电装置连接到该部分横截面。 从可控排放装置排出的固体流可以在布置在其下方的连续输送机上收集并移除。 根据来自多个等效传感器的测量信号，控制来自连续放电装置的均匀固体质量放电，借助于放电装置的输送功率，记录与仓库相关的部分部分中的局部质量流量 传感器。 在使用通过电阻加热的电极在筒仓中加热的导电固体的情况下，通过在电极处测量的电流来实现放电装置的控制。

    Device for increasing pH of an aqueous stream
    23.
    发明授权
    Device for increasing pH of an aqueous stream 失效
    用于增加含水流的pH的装置

    公开(公告)号：US07378016B2

    公开(公告)日：2008-05-27

    申请号：US11287846

    申请日：2005-11-28

    Applicant: Joseph Gordon Monteith

    Inventor： Joseph Gordon Monteith

    IPC: C02F1/68

    CPC classification number: C02F1/66 ,  B01J8/1809 ,  B01J8/1872 ,  B01J19/0086 ,  B01J2208/00548 ,  B01J2208/00592 ,  B01J2208/0061 ,  B01J2219/185 ,  B01J2219/1946 ,  C02F2103/10 ,  C02F2103/16 ,  C02F2103/22 ,  C02F2103/32 ,  C02F2209/40

    Abstract: A device is provided for increasing the pH of an acidic aqueous stream, which may result from commercial activity in petroleum, mining, metal finishing and food processing sectors, among others. A container defines an upright reactor portion with a cross-section that increases upwardly, along with inlet and outlet conduits connected to an inlet and an outlet between which the reactor portion is located. The conical portion contains a bed of substantially water-insoluble alkaline salt particulate, such as MgSO, the bed being such that, when the pH of the inflowing aqueous stream is below 7, contact between the particulate and the aqueous stream will raise the pH of the outflowing stream to a level above that of the inflowing stream.

    Abstract translation: 提供了一种用于增加酸性含水流的pH值的装置，其可能由石油，采矿，金属加工和食品加工部门等的商业活动引起。 容器限定具有向上增加的横截面的直立反应器部分，以及连接到反应器部分所位于的入口和出口之间的入口和出口导管。 锥形部分包含基本上不溶于水的碱性盐颗粒如MgSO 4的床，床的流动使得当流入的水流的pH低于7时，颗粒和水流之间的接触将提高pH 流出的流量高于流入物流的水平。

    Method for the Continuous Production of Crosslinked Particulate Gel-Type Polymers
    24.
    发明申请
    Method for the Continuous Production of Crosslinked Particulate Gel-Type Polymers 审中-公开
    连续生产交联颗粒凝胶型聚合物的方法

    公开(公告)号：US20080004408A1

    公开(公告)日：2008-01-03

    申请号：US11662824

    申请日：2005-09-21

    Applicant: Uwe Stueven ,  Matthias Weismantel ,  Rudiger Funk ,  Annemarie Hillebrecht ,  Dominicus Esbroeck ,  Karl Possemiers ,  Ronny Kaey

    Inventor： Uwe Stueven ,  Matthias Weismantel ,  Rudiger Funk ,  Annemarie Hillebrecht ,  Dominicus Esbroeck ,  Karl Possemiers ,  Ronny Kaey

    IPC: C08F2/01

    CPC classification number: B01J19/0066 ,  B01J8/10 ,  B01J2208/0061 ,  C08F2/01 ,  C08F6/008 ,  C08F6/10 ,  C08F220/06 ,  C08F220/56

    Abstract: Disclosed is a method for the continuous production of crosslinked, particulate, gel-type polymers by copolymerizing a) water-soluble, monoethylenically unsaturated monomers, b) 0.001 to 5 molar percent of monomers containing at least two polymerizable groups, the percentage being relative to the monomers (a), in a mixer. The substances that are added at the beginning of the kneader are conveyed in an axial direction towards the end of the mixer. The inventive method is characterized in that at least one of the following conditions is met: i) the filling level in the kneader mixer is at least 71 percent; ii) the water-soluble, monoethylenically unsaturated monomers contain up to 150 ppm of a semicyclic ether of a hydroquinone; iii) the temperature in the polymerization zone exceeds 65° C.; iv) the kneader has a remixing rate of less than 0.33.

    Abstract translation: 公开了通过共聚a）水溶性单烯属不饱和单体，b）0.001至5摩尔％的含有至少两个可聚合基团的单体，其相对于 单体（a），在混合器中。 在捏合机开始时添加的物质沿轴向方向输送到混合器的末端。 本发明的方法的特征在于满足以下条件中的至少一个：i）捏合机混合器中的填充水平为至少71％; ii）水溶性单烯属不饱和单体含有高达150ppm的氢醌的半环醚; iii）聚合区域的温度超过65℃。 iv）捏合机的再混合率小于0.33。

    Catalyst withdrawal apparatus and method for regulating catalyst inventory in a fluid catalyst cracking unit
    25.
    发明申请
    Catalyst withdrawal apparatus and method for regulating catalyst inventory in a fluid catalyst cracking unit 有权
    用于调节流体催化裂化装置中催化剂存量的催化剂抽出装置和方法

    公开(公告)号：US20070020154A1

    公开(公告)日：2007-01-25

    申请号：US11184125

    申请日：2005-07-19

    Applicant: Martin Evans

    Inventor： Martin Evans

    IPC: F27B15/00 ,  B32B27/12

    CPC classification number: B01J8/003 ,  B01J8/0035 ,  B01J8/0055 ,  B01J8/20 ,  B01J2208/00176 ,  B01J2208/00185 ,  B01J2208/00203 ,  B01J2208/00212 ,  B01J2208/00371 ,  B01J2208/00539 ,  B01J2208/00548 ,  B01J2208/0061 ,  B01J2208/00619 ,  B01J2208/00734 ,  B01J2208/00761 ,  B01J2208/00769 ,  B01J2219/00207 ,  B01J2219/0022 ,  B01J2219/00236 ,  C10G11/18 ,  C10G11/187 ,  C10G2300/70

    Abstract: A catalyst withdrawal apparatus and method for regulating catalyst inventory in a fluid catalytic cracking catalyst (FCC) unit is provided. In one embodiment, a catalyst withdrawal apparatus for removing catalyst from a FCC unit includes a pressure vessel having a metering device coupled to a fill port. A heat dissipater is located adjacent the metering device and is adapted to cool catalyst entering the pressure vessel. A sensor is coupled to the pressure vessel arranged to provide a metric indicative of catalyst entering the pressure vessel through the metering device. In another embodiment, a method for regulating catalyst inventory in a FCC unit includes the steps of determining a change of catalyst present in a FCC unit, withdrawing catalyst from the FCC unit into an isolatable storage vessel coupled to the FCC unit, measuring the amount of catalyst disposed in the storage vessel, and removing the measured catalyst from the storage vessel.

    Abstract translation: 提供了一种用于调节流化催化裂化催化剂（FCC）单元中催化剂存量的催化剂提取装置和方法。 在一个实施方案中，用于从FCC单元除去催化剂的催化剂提取装置包括具有连接到填充口的计量装置的压力容器。 散热器位于计量装置附近并适于冷却进入压力容器的催化剂。 传感器耦合到压力容器，所述压力容器被布置成提供指示通过计量装置进入压力容器的催化剂的量度。 在另一个实施方案中，一种用于调节FCC单元中催化剂库存的方法包括以下步骤：确定FCC单元中存在的催化剂的变化，将催化剂从FCC单元回收到耦合到FCC单元的可分离存储容器中， 催化剂，并将其从储存容器中除去。

    Combined thermal and catalytic treatment of heavy petroleum in a slurry phase counterflow reactor
    28.
    发明授权
    Combined thermal and catalytic treatment of heavy petroleum in a slurry phase counterflow reactor 有权
    在淤浆相逆流反应器中对重石油进行联合热处理和催化处理

    公开(公告)号：US06755962B2

    公开(公告)日：2004-06-29

    申请号：US09852107

    申请日：2001-05-09

    Applicant: Dwijen K. Banerjee

    Inventor： Dwijen K. Banerjee

    IPC: C10G4700

    CPC classification number: C10G65/10 ,  B01J8/0035 ,  B01J8/22 ,  B01J8/228 ,  B01J2208/00256 ,  B01J2208/00274 ,  B01J2208/00283 ,  B01J2208/00539 ,  B01J2208/0061 ,  B01J2208/0084 ,  C10G47/22

    Abstract: A slurry phase reactor is designed to treat extra heavy petroleum crude in a combination of thermal-zone and catalytic-zone in a counterflow system where liquid feed is added to the top and hydrogen at the bottom. Feed enters the gas-phase thermal zone, where it passes to a liquid-phase thermal zone. In the liquid-phase thermal zone, the hydrocarbon is thermally cracked and the unreacted liquid is further passed to a catalytic-zone below in communication with the thermal-zone. Catalyst can be added or removed as required in a continuous mode without shutting down the system. The heat generated inside the catalytic cracking zone is distributed to the entire reactor as the gaseous product flows upward. Feed is brought to the reaction conditions by the heat recovered from the gas-phase zone. Reaction temperature could be controlled by feed temperature.

    Abstract translation: 浆料相反应器被设计成在反向流动系统中处理热区域和催化区域的组合中的额外重质石油原油，其中液体进料添加到顶部，底部加氢。 进料进入气相热区，在那里它进入液相热区。 在液相热区中，烃被热裂化，并且未反应的液体进一步传递到与热区连通的下游催化区。 可以根据需要在连续模式下添加或除去催化剂，而无需关闭系统。 当气体产物向上流动时，催化裂化区内产生的热分布到整个反应器中。 通过从气相区回收的热量将进料送入反应条件。 反应温度可以通过进料温度控制。

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