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    METHOD AND APPARATUS FOR DETERMINING BEAM DIRECTION
    1.
    发明申请
    METHOD AND APPARATUS FOR DETERMINING BEAM DIRECTION 审中-公开

    公开(公告)号：WO2018127120A1

    公开(公告)日：2018-07-12

    申请号：PCT/CN2018/071532

    申请日：2018-01-05

    Applicant: CHOU, Chie-Ming ,  CHENG, Yu-Hsin

    Inventor： CHOU, Chie-Ming ,  CHENG, Yu-Hsin

    IPC: H04W16/28

    Abstract: A method for a user equipment (UE) to synchronize with a first transmit-receive point (TRP) is disclosed. The method includes receiving, by the UE, beam information of the first TRP from a second TRP(789); detecting, by the UE, a synchronization signal in a beam from the first TRP based on the beam information; transmitting, by the UE, a physical random access channel (PRACH) preamble to the first TRP to synchronize with the first TRP(790); where the first TRP operates in a first frequency, and the second TRP operates in a second frequency lower than the first frequency.

    METHODS FOR ENHANCING THE EFFICIENCY OF RHENIUM-PROMOTED EPOXIDATION CATALYSTS AND EPOXIDATION METHODS UTILIZING THESE
    6.
    发明申请
    METHODS FOR ENHANCING THE EFFICIENCY OF RHENIUM-PROMOTED EPOXIDATION CATALYSTS AND EPOXIDATION METHODS UTILIZING THESE 审中-公开
    提高铑促进环氧化催化剂效率的方法和利用这些催化剂的环氧化方法

    公开(公告)号：WO2010123675A1

    公开(公告)日：2010-10-28

    申请号：PCT/US2010/029948

    申请日：2010-04-05

    Applicant: DOW TECHNOLOGY INVESTMENTS LLC ,  LIU, Albert Cheng-Yu ,  ZHANG, Liping

    Inventor： LIU, Albert Cheng-Yu ,  ZHANG, Liping

    IPC: C07D301/10

    CPC classification number: C07D301/10

    Abstract: A method for enhancing the efficiency of a rhenium-promoted epoxidation catalyst is provided. Advantageously, the method may be carried out in situ, i.e., within the epoxidation process, and in fact, may be carried out during production of the desired epoxide. As such, a method for the epoxidation of alkylenes incorporating the efficiency-enhancing method is also provided, as is a method for using the alkylene oxides so produced for the production of 1,2-diols, 1,2-carbonates, 1,2-diol ethers, or alkanolamines.

    Abstract translation: 提供了提高铼促进的环氧化催化剂的效率的方法。 有利地，该方法可以在原位进行，即在环氧化方法中进行，实际上可以在制备期望的环氧化物期间进行。 因此，还提供了包含效率增强方法的亚烷基环氧化方法，以及如此制备用于生产1,2-二醇，1,2-碳酸酯，1,2- - 二醇醚或链烷醇胺。

    CONFINEMENT OF FOAM DELIVERED BY A PROXIMITY HEAD
    7.
    发明申请
    CONFINEMENT OF FOAM DELIVERED BY A PROXIMITY HEAD 审中-公开
    通过近接头提供的泡沫的约束

    公开(公告)号：WO2010062918A2

    公开(公告)日：2010-06-03

    申请号：PCT/US2009/065812

    申请日：2009-11-24

    Applicant: LAM RESEARCH CORPORATION ,  KHOLODENKO, Arnold ,  LIN, Cheng-Yu, Sean ,  GINZBURG, Leon ,  MANDELBOYM, Mark ,  TOMASCH, Gregory, A. ,  HUSAIN, Anwar

    Inventor： KHOLODENKO, Arnold ,  LIN, Cheng-Yu, Sean ,  GINZBURG, Leon ,  MANDELBOYM, Mark ,  TOMASCH, Gregory, A. ,  HUSAIN, Anwar

    IPC: H01L21/302

    CPC classification number: H01L21/6704 ,  B08B3/003 ,  C11D11/0047 ,  C11D11/0058 ,  H01L21/67051 ,  H01L21/67057 ,  H01L21/6719 ,  H01L21/6776

    Abstract: In an example embodiment, a linear wet system includes a carrier and a proximity head in a chamber. The proximity head includes three sections in a linear arrangement. The first section suctions liquid from the upper surface of a semiconductor wafer as the wafer is transported by the carrier under the proximity head. The second section is configured to cause a film (or meniscus) of cleaning foam which is a non-Newtonian fluid to flow onto the upper surface of the wafer. The third section is configured to cause a film of rinsing fluid to flow onto the upper surface of the wafer as the wafer is carried under the proximity head. The third section is defined partially around the second section and up to the first section, so that the third section and the first section create a confinement of the cleaning foam with respect to the chamber.

    Abstract translation: 在示例性实施例中，线性湿系统包括腔室中的载体和临近头。 临近头包括三个线性排列的部分。 当晶片由邻近头下的载体传送时，第一部分从半导体晶片的上表面抽吸液体。 第二部分构造成使非牛顿流体的清洁泡沫的膜（或弯液面）流到晶片的上表面上。 第三部分被配置成当晶片在邻近头下被携带时使漂洗流体膜流到晶片的上表面。 第三部分被部分地限定在第二部分周围并且一直到第一部分，使得第三部分和第一部分形成清洁泡沫相对于腔室的限制。

    CATALYTIC PYROLYSIS OF SOLID BIOMASS AND RELATED BIOFUELS, AROMATIC, AND OLEFIN COMPOUNDS
    9.
    发明申请
    CATALYTIC PYROLYSIS OF SOLID BIOMASS AND RELATED BIOFUELS, AROMATIC, AND OLEFIN COMPOUNDS 审中-公开
    固体生物质和相关生物燃料，芳香烃和烯烃化合物的催化热解

    公开(公告)号：WO2009111026A8

    公开(公告)日：2009-12-03

    申请号：PCT/US2009001382

    申请日：2009-03-03

    Applicant: UNIV MASSACHUSETTS ,  HUBER GEORGE W ,  VISPUTE TUSHAR ,  CARLSON TORREN ,  JAE JUNGHO ,  CHENG YU-TING ,  TOMPSETT GEOFFREY

    Inventor： HUBER GEORGE W ,  VISPUTE TUSHAR ,  CARLSON TORREN ,  JAE JUNGHO ,  CHENG YU-TING ,  TOMPSETT GEOFFREY

    IPC: C10G11/18

    CPC classification number: C10G1/002 ,  C10G1/08 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/305 ,  C10G2400/02 ,  C10G2400/20 ,  C10G2400/30 ,  Y02P30/42

    Abstract: This invention relates to compositions and methods for fluid hydrocarbon product, and more specifically, to compositions and methods for fluid hydrocarbon product via catalytic pyrolysis. Some embodiments relate to methods for the production of specific aromatic products (e.g., benzene, toluene, naphthalene, xylene, etc.) via catalytic pyrolysis. Some such methods may involve the use of a composition comprising a mixture of a solid hydrocarbonaceous material and a heterogeneous pyrolytic catalyst component. In some embodiments, the mixture may be pyrolyzed at high temperatures (e.g., between 500 °C and 1000 °C). The pyrolysis may be conducted for an amount of time at least partially sufficient for production of discrete, identifiable biofuel compounds. Some embodiments involve heating the mixture of catalyst and hydrocarbonaceous material at high rates (e.g., from about 50 °C per second to about 1000 0C per second). The methods described herein may also involve the use of specialized catalysts. For example, in some cases, zeolite catalysts may be used; optionally, the catalysts used herein may have high silica to alumina molar ratios. In some instances, the composition fed to the pyrolysis reactor may have a relatively high catalyst to hydrocarbonaceous material mass ratio (e.g., from about 5: 1 to about 20:1).

    Abstract translation: 本发明涉及用于流体烃产品的组合物和方法，更具体地说，涉及用于通过催化热解的流体烃产物的组合物和方法。 一些实施方案涉及通过催化热解生产特定芳族产物（例如苯，甲苯，萘，二甲苯等）的方法。 一些此类方法可涉及使用包含固体含烃材料和非均相热解催化剂组分的混合物的组合物。 在一些实施方案中，该混合物可以在高温下（例如在500℃和1000℃之间）热解。 热解可以进行至少部分足以产生分立的，可识别的生物燃料化合物的时间量。 一些实施方案涉及以高速率（例如，从约每秒50℃至每秒约1000℃）加热催化剂和含烃材料的混合物。 本文所述的方法还可以涉及使用专门的催化剂。 例如，在一些情况下，可以使用沸石催化剂; 任选地，本文使用的催化剂可以具有高的二氧化硅/氧化铝摩尔比。 在一些情况下，进料至热解反应器的组合物可具有相对高的催化剂与烃材料质量比（例如约5：1至约20：1）。

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