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    FLUID BED REACTORS AND ASSOCIATED METHODS
    81.
    发明申请
    FLUID BED REACTORS AND ASSOCIATED METHODS 有权
    流体床反应器及相关方法

    公开(公告)号：US20100034709A1

    公开(公告)日：2010-02-11

    申请号：US12437190

    申请日：2009-05-07

    Applicant: David Fame

    Inventor： David Fame

    IPC: B01J8/28 ,  F27B15/08

    CPC classification number: B01J8/10 ,  B01J8/125 ,  B01J8/28 ,  B01J8/382 ,  B01J2208/00371 ,  B01J2219/185 ,  F26B3/08 ,  F26B17/005 ,  Y10S210/912

    Abstract: In one embodiment of the present invention a fluid bed reactor is provided, comprising:a housing, at least one tray disposed within the housing, at least one motor operatively connected to the at least one tray, wherein the motor rotates the at least one tray; and at least one wiper associated with at the at least one tray which directs product on a top surface of a respective tray down through at least one radial slot in each respective tray as each respective tray is rotated by the motor. At least one of the trays is at least partially perforated material which a gas to flow up out of the top surface of the tray, at least partially fluidizing product on the top surface of the tray.

    Abstract translation: 在本发明的一个实施例中，提供了一种流化床反应器，包括：外壳，设置在壳体内的至少一个托盘，至少一个马达，其可操作地连接到所述至少一个托盘，其中所述马达使所述至少一个托盘 ; 以及至少一个与所述至少一个托盘相关联的擦拭器，所述至少一个托盘在每个相应的托盘由所述马达旋转时将产品在相应托盘的顶表面上向下引导通过每个相应托盘中的至少一个径向槽。 托盘中的至少一个是至少部分穿孔的材料，其中气体从托盘的顶表面向上流出，至少部分地使托盘顶表面上的产品流态化。

    Reaction apparatus for producing trichlorosilane and method for producing trichlorosilane
    83.
    发明申请
    Reaction apparatus for producing trichlorosilane and method for producing trichlorosilane 有权
    用于制备三氯硅烷的反应装置和三氯硅烷的制备方法

    公开(公告)号：US20090123359A1

    公开(公告)日：2009-05-14

    申请号：US12289209

    申请日：2008-10-22

    Applicant: Chikara Inaba

    Inventor： Chikara Inaba

    IPC: B01J8/02 ,  C01B33/107

    CPC classification number: C01B33/10736 ,  B01J8/1827 ,  B01J8/34 ,  B01J8/382 ,  B01J19/30 ,  B01J2208/00867 ,  B01J2219/30207 ,  B01J2219/30215 ,  B01J2219/30408 ,  B01J2219/312

    Abstract: A reaction apparatus for producing trichlorosilane in which metal silicon powder M is reacted with hydrogen chloride gas, thus generating trichlorosilane, includes: an apparatus body into which the metal silicon powder is supplied; and an ejection port for ejecting the hydrogen chloride gas into the apparatus body from the bottom part of the apparatus body, wherein a plurality of holed pieces having a through hole penetrating in the thickness direction and a plurality of pellets interposed between these holed pieces are stacked in a mixed state on the upper side of the ejection port.

    Abstract translation: 一种制造三氯硅烷的反应装置，其中金属硅粉末M与氯化氢气体反应，从而产生三氯硅烷，包括：提供金属硅粉末的装置体; 以及用于从装置主体的底部将氯化氢气体喷射到装置主体中的排出口，其中多个具有沿厚度方向贯穿的通孔的孔和多个在这些孔之间插入的颗粒被堆叠 在喷射口的上侧处于混合状态。

    Apparatus for treating flue gas using single-stage gas dispersing tray
    85.
    发明申请
    Apparatus for treating flue gas using single-stage gas dispersing tray 审中-公开
    使用单级气体分散盘处理烟气的设备

    公开(公告)号：US20070134141A1

    公开(公告)日：2007-06-14

    申请号：US11385383

    申请日：2006-03-21

    Applicant: Seung Park ,  Ki Kim ,  Hi An ,  Kwang Park ,  Hee Uhm

    Inventor： Seung Park ,  Ki Kim ,  Hi An ,  Kwang Park ,  Hee Uhm

    IPC: B01J8/08

    CPC classification number: B01J19/26 ,  B01D53/18 ,  B01D53/504 ,  B01J4/002 ,  B01J8/1818 ,  B01J8/1827 ,  B01J8/22 ,  B01J8/28 ,  B01J8/382 ,  B01J8/386 ,  B01J8/44 ,  B01J2208/00132 ,  B01J2208/00867 ,  B01J2219/1923 ,  B01J2219/1941

    Abstract: An apparatus for treating flue gas using a single-stage gas dispersing tray, which removes sulfur dioxide from the flue gas exhausted from a thermal power plant. Oxidation air is injected into the lower portion of an absorption slurry riser so as to decrease the density of a gas-liquid (slurry) mixture rising through the absorption slurry riser, and a difference of densities of absorption slurry between the inside and the outside of an overflow weir serve as a driving force for circulating the absorption slurry positioned on and under the gas dispersing tray so as to maximize the amount of the circulating absorption slurry. Thereby, the apparatus has a high SO2 removal efficiency even at a low operating pH and a low absorber pressure drop.

    Abstract translation: 一种用于使用单级气体分散盘处理烟道气的装置，其从从火力发电厂排出的烟道气中除去二氧化硫。 将氧化空气注入到吸收浆料提升管的下部，以便降低通过吸收浆料提升管升高的气液（浆料）混合物的密度，以及内部和外部之间的吸收浆料的密度差 溢流堰作为使位于气体分散塔上和下方的吸收浆液循环的驱动力，以使循环吸收浆料的量最大化。 因此，即使在低操作pH和低吸收剂压降下，该装置也具有高的SO 2去除效率。

    Installation for gas-phase polymerisation
    86.
    发明申请
    Installation for gas-phase polymerisation 审中-公开
    气相聚合安装

    公开(公告)号：US20070015886A1

    公开(公告)日：2007-01-18

    申请号：US11485324

    申请日：2006-07-13

    Applicant: Paul Diepen ,  Stanislaus Mutsers

    Inventor： Paul Diepen ,  Stanislaus Mutsers

    IPC: C08F2/00

    CPC classification number: B01J8/36 ,  B01J8/382 ,  B01J2208/00274 ,  B01J2208/00362 ,  B01J2208/00628 ,  B01J2208/00867 ,  B01J2219/182 ,  C08F10/00 ,  C08F2/01 ,  C08F2/34

    Abstract: Installation for the gas-phase polymerisation of at least one olefinic monomer, comprising a horizontal stirred reactor (1) consisting of an undivided space, provided with a number of gas feeds (13a-13) in the bottom section of the reactor (1) and a number of liquid feeds (7a-7) in the top section of the reactor (1) and at least two gas outlets (9, 11) at the top of the reactor (1), the installation being provided with means (43, 45) to regulate the discharge capacities of the gas outlets.

    Abstract translation: 用于至少一种烯烃单体的气相聚合的安装，包括由不连续空间组成的水平搅拌反应器（1），其在反应器（1）的底部设有多个气体进料（13a-13） ）和反应器（1）的顶部中的多个液体进料（7a--7）和在反应器（1）的顶部的至少两个气体出口（9,11），所述装置设置有装置 （43,45）来调节气体出口的放电容量。

    Continuous slurry polymerization volatile removal
    87.
    发明授权
    Continuous slurry polymerization volatile removal 有权

    公开(公告)号：US07034090B2

    公开(公告)日：2006-04-25

    申请号：US10023677

    申请日：2002-02-14

    Applicant: James Austin Kendrick

    Inventor： James Austin Kendrick

    IPC: C08F2/00

    CPC classification number: B01D3/06 ,  B01J8/003 ,  B01J8/005 ,  B01J8/0055 ,  B01J8/007 ,  B01J8/382 ,  B01J19/1837 ,  B01J2208/00539 ,  B01J2208/00761 ,  B01J2208/00769 ,  B01J2208/00867 ,  B01J2219/00006 ,  B01J2219/00103 ,  B01J2219/00114 ,  C08F6/003

    Abstract: A process/apparatus is disclosed for continuously separating a liquid medium comprising diluent and unreacted monomers from a polymerization effluent comprising diluent, unreacted monomers and polymer solids, comprising a continuous discharge of the polymerization effluent from a slurry reactor through a discharge valve and transfer conduit into a first intermediate pressure flash tank with a conical bottom defined by substantially straight sides inclined at an angle to that of horizontal equal to or greater than the angle of slide of the slurry/polymer solids and an exit seal chamber of such diameter (d) and length (l) as to maintain a desired volume of concentrated polymer solids/slurry in the exit seal chamber such as to form a pressure seal while continuously discharging a plug flow of concentrated polymer solids/slurry bottom product of said first flash tank from the exit seal chamber through a seal chamber exit reducer with inclined sides defined by substantially straight sides inclined at an angle to that of horizontal equal to or greater than the angle of slide of the polymer solids which remain after removal of about 50 to 100% of the inert diluent therefrom to a second flash tank at a lower pressure.

    Continuous slurry polymerization volatile removal
    88.
    发明申请
    Continuous slurry polymerization volatile removal 审中-公开
    连续淤浆聚合挥发性去除

    公开(公告)号：US20040198928A1

    公开(公告)日：2004-10-07

    申请号：US10827777

    申请日：2004-04-20

    Inventor： James A. Kendrick ,  Thomas W. Towles ,  Scott Thomas Roger

    IPC: C08F002/00

    CPC classification number: B01D3/06 ,  B01J8/003 ,  B01J8/005 ,  B01J8/0055 ,  B01J8/007 ,  B01J8/382 ,  B01J19/0053 ,  B01J19/1837 ,  B01J2208/0007 ,  B01J2208/00539 ,  B01J2208/00761 ,  B01J2208/00769 ,  B01J2208/00867 ,  B01J2219/00006 ,  B01J2219/00033 ,  B01J2219/00103 ,  B01J2219/00114 ,  B01J2219/00162 ,  B01J2219/00164 ,  B01J2219/00191 ,  B01J2219/002 ,  B01J2219/00213 ,  B01J2219/00231 ,  B01J2219/00236 ,  B01J2219/0024 ,  C08F2/00 ,  C08F6/003 ,  C08F10/00 ,  C08F210/16 ,  C08F2/14 ,  C08F210/14

    Abstract: A process/apparatus is disclosed for continuously separating a liquid medium comprising diluent and unreacted monomers from a polymerization effluent comprising diluent, unreacted monomers and polymer solids, comprising a continuous discharge of the polymerization effluent from a slurry reactor through a discharge valve and transfer conduit into a first intermediate pressure flash tank with a conical bottom defined by substantially straight sides inclined at an angle to that of horizontal equal to or greater than the angle of slide of the slurry/polymer solids and an exit seal chamber of such diameter (d) and length (l) as to maintain a desired volume of concentrated polymer solids/slurry in the exit seal chamber such as to form a pressure seal while continuously discharging a plug flow of concentrated polymer solids/slurry bottom product of said first flash tank from the exit seal chamber through a seal chamber exit reducer with inclined sides defined by substantially straight sides inclined at an angle to that of horizontal equal to or greater than the angle of slide of the polymer solids which remain after removal of about 50 to 100% of the inert diluent therefrom to a second flash tank at a lower pressure.

    Abstract translation: 公开了一种用于从包含稀释剂，未反应单体和聚合物固体的聚合流出物连续分离包含稀释剂和未反应单体的液体介质的方法/装置，其包括通过排放阀将淤浆反应器的聚合流出物连续排出并将传输导管 具有锥形底部的第一中间压力闪蒸罐，该锥形底部由基本上直的侧面倾斜的水平面倾斜，该水平面等于或大于浆料/聚合物固体的滑动角度以及直径（d）的出口密封室， 长度（l），以便在出口密封室中保持所需体积的浓缩的聚合物固体/浆料，以便形成压力密封，同时连续地将所述第一闪蒸罐的浓缩聚合物固体/浆料底部产物的塞流从出口 密封室通过密封室出口减速器，斜面由基本上直的侧面i定义 以等于或大于在约50至100％的惰性稀释剂从其中移除至较低压力的第二闪蒸罐后保留的聚合物固体的滑动角度等于或大于水平角的角度倾斜。

    Continuous slurry polymerization volatile removal
    90.
    发明申请
    Continuous slurry polymerization volatile removal 审中-公开
    连续淤浆聚合挥发性去除

    公开(公告)号：US20020182121A1

    公开(公告)日：2002-12-05

    申请号：US10147219

    申请日：2002-05-14

    Applicant: Exxon Chemical Patents, Inc.

    Inventor： James Austin Kendrick

    IPC: C08F002/00 ,  C08F002/01

    CPC classification number: B01J8/005 ,  B01D3/06 ,  B01J8/003 ,  B01J8/0055 ,  B01J8/007 ,  B01J8/382 ,  B01J19/1837 ,  B01J2208/0007 ,  B01J2208/00539 ,  B01J2208/00761 ,  B01J2208/00769 ,  B01J2208/00867 ,  B01J2219/00006 ,  B01J2219/00103 ,  B01J2219/00114 ,  B01J2219/00191 ,  B01J2219/002 ,  B01J2219/00213 ,  B01J2219/00231 ,  B01J2219/00236 ,  B01J2219/0024 ,  C08F6/003 ,  C08F6/24 ,  C08F10/00 ,  C08F210/16 ,  C08F2/14 ,  C08F210/14

    Abstract: A process/apparatus is disclosed for continuously separating a liquid medium comprising diluent and unreacted monomers from a polymerization effluent comprising diluent, unreacted monomers and polymer solids, comprising a continuous discharge of the polymerization effluent from a slurry reactor through a discharge valve and transfer conduit into a first intermediate pressure flash tank with a conical bottom defined by substantially straight sides inclined at an angle to that of horizontal equal to or greater than the angle of slide of the slurry/polymer solids and an exit seal chamber of such diameter (d) and length (I) as to maintain a desired volume of concentrated polymer solids/slurry in the exit seal chamber such as to form a pressure seal while continuously discharging a plug flow of concentrated polymer solids/slurry bottom product of said first flash tank from the exit seal chamber through a seal chamber exit reducer with inclined sides defined by substantially straight sides inclined at an angle to that of horizontal equal to or greater than the angle of slide of the polymer solids which remain after removal of about 50 to 100% of the inert diluent therefrom to a second flash tank at a lower pressure.

    Abstract translation: 公开了一种用于从包含稀释剂，未反应单体和聚合物固体的聚合流出物连续分离包含稀释剂和未反应单体的液体介质的方法/装置，其包括通过排放阀将淤浆反应器的聚合流出物连续排出并将传输导管 具有锥形底部的第一中间压力闪蒸罐，该锥形底部由基本上直的侧面倾斜的水平面倾斜，该水平面等于或大于浆料/聚合物固体的滑动角度以及直径（d）的出口密封室， 长度（I），以便在出口密封室中保持所需体积的浓缩聚合物固体/浆料，以形成压力密封，同时连续地将所述第一闪蒸罐的浓缩聚合物固体/浆料底部产物的塞流从出口 密封室通过密封室出口减速器，斜面由基本上直的侧面i定义 以等于或大于在约50至100％的惰性稀释剂从其中移除至较低压力的第二闪蒸罐后保留的聚合物固体的滑动角度等于或大于水平角的角度倾斜。

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