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    CONTROL SYSTEM FOR A WORK UNIT
    1.
    发明申请
    CONTROL SYSTEM FOR A WORK UNIT 审中-公开
    工作单位控制系统

    公开(公告)号：WO2010019770A2

    公开(公告)日：2010-02-18

    申请号：PCT/US2009053712

    申请日：2009-08-13

    Applicant: VERMEER MFG CO ,  MASS CORY ,  GRAHAM CURT ,  HUTCHINSON MATTHEW

    Inventor： MASS CORY ,  GRAHAM CURT ,  HUTCHINSON MATTHEW

    IPC: A01B69/00 ,  A01B76/00 ,  B62D11/02 ,  B62D11/20

    CPC classification number: B62D1/12 ,  A01B33/028 ,  A01B69/007 ,  B62D11/006 ,  B62D11/04 ,  B62D51/001 ,  B62D51/04

    Abstract: The present disclosure relates to a work unit with power turning. The work unit includes a frame having a first end, a second end and left and right sides that extend between the first and second ends. A work element is carried by the frame. A left propulsion element is positioned at the left side of the frame and a right propulsion element is positioned at the right side of the frame. A drive arrangement is carried by the frame for driving the left and right propulsion elements. The work unit also includes left and right spaced-apart leverage arms that project outwards from the second end of the frame. At least one of the left and right leverage arms is operatively connected to the drive arrangement such that pressure applied by an operator to the left or right leverage arms in a left or right direction causes the drive arrangement to turn the work unit.

    Abstract translation: 本公开涉及具有动力转向的作业单元。 工作单元包括具有在第一端和第二端之间延伸的第一端，第二端以及左右两侧的框架。 工件由框架承载。 左推进元件位于框架的左侧，右推进元件位于框架的右侧。 驱动装置由用于驱动左右推进元件的框架承载。 工作单元还包括从框架的第二端向外突出的左和右间隔开的杠杆臂。 左和右杠杆臂中的至少一个可操作地连接到驱动装置，使得操作者向左或右杠杆臂施加的压力在左或右方向上使杠杆臂驱动装置转动。

    LNG REGASIFICATION CONFIGURATIONS AND METHODS
    3.
    发明申请
    LNG REGASIFICATION CONFIGURATIONS AND METHODS 审中-公开
    LNG重组配置和方法

    公开(公告)号：WO2006004723A1

    公开(公告)日：2006-01-12

    申请号：PCT/US2005/022880

    申请日：2005-06-27

    Applicant: FLUOR TECHNOLOGIES CORPORATION ,  MAK, John ,  NEUMANN, Ralph ,  GRAHAM, Curt ,  HEFFERN, Dan

    Inventor： MAK, John ,  NEUMANN, Ralph ,  GRAHAM, Curt ,  HEFFERN, Dan

    IPC: F25J3/00

    CPC classification number: F25J3/0214 ,  F25J3/0233 ,  F25J3/0238 ,  F25J3/0242 ,  F25J2200/02 ,  F25J2200/04 ,  F25J2200/72 ,  F25J2200/74 ,  F25J2205/04 ,  F25J2215/62 ,  F25J2235/60 ,  F25J2240/02 ,  F25J2245/02 ,  F25J2270/02 ,  F25J2290/10

    Abstract: LNG composition of LNG from a storage tank or other source is modified in a process in which the LNG is pumped to a first pressure and split into two portions. One portion of the pressurized LNG is then reduced in pressure and heavier components are separated from the reduced pressure LNG to thereby form a lean LNG. The lean LNG is then pumped to a higher pressure and combined with the other portion to form a leaner LNG. Preferably, separation is performed using a demethanizer, wherein part of the demethanizer overhead product is condensed to form the lean LNG, while another portion is used for column reflux. In further preferred configurations, ethane recovery is variable and in yet other configurations, propane or ethane can be delivered via a batching pipeline.

    Abstract translation: 来自储罐或其他来源的LNG的LNG组成在LNG被泵送到第一压力并分成两部分的过程中被修改。 然后将一部分加压LNG压力降低，并将较重组分从减压LNG中分离出来，从而形成贫LNG。 然后将贫LNG泵送到更高的压力并与另一部分结合以形成更贫乏的LNG。 优选地，使用脱甲烷塔进行分离，其中部分脱甲烷塔塔顶产物被冷凝以形成贫LNG，而另一部分被用于塔回流。 在进一步优选的构造中，乙烷回收是可变的，并且在其他构造中，丙烷或乙烷可以通过配料管道输送。

    APPARATUS FOR CONTROL OF A MOBILE MACHINE
    5.
    发明申请
    APPARATUS FOR CONTROL OF A MOBILE MACHINE 审中-公开
    控制移动机器的设备

    公开(公告)号：WO2007030243A1

    公开(公告)日：2007-03-15

    申请号：PCT/US2006/030448

    申请日：2006-08-03

    Applicant: VERMEER MANUFACTURING COMPANY ,  GRAHAM, Curt ,  SHKIRYAK, Peter ,  HUTCHINSON, Matthew

    Inventor： GRAHAM, Curt ,  SHKIRYAK, Peter ,  HUTCHINSON, Matthew

    IPC: E02F9/20 ,  G05G9/047

    CPC classification number: G05G9/047 ,  E02F9/2004

    Abstract: A control system(50) for use with a mobile machine (100) . The control system including a hand-grip bar (140) having right (146) and left (142) curved sections. The curved sections each define an approximate center (c) . The control system further including joysticks (122, 124) positioned at the approximate center of the curved sections . The curved sections each have a radius such that an operator can operate one or both joysticks without releasing his grip from the hand-grip bar.

    Abstract translation: 一种与移动机器（100）一起使用的控制系统（50）。 该控制系统包括具有右（146）和左（142）弯曲部分的手柄杆（140）。 弯曲部分每个限定近似中心（c）。 控制系统还包括位于弯曲部分的大致中心处的操纵杆（122,124）。 弯曲部分各自具有半径，使得操作者可以操作一个或两个操纵杆，而不会将其从手柄杆释放。

    CONFIGURATIONS AND METHODS FOR IMPROVED ACID GAS REMOVAL
    7.
    发明申请
    CONFIGURATIONS AND METHODS FOR IMPROVED ACID GAS REMOVAL 审中-公开
    改善酸性气体去除的配置和方法

    公开(公告)号：WO2003089115A1

    公开(公告)日：2003-10-30

    申请号：PCT/US2002/012050

    申请日：2002-04-15

    Applicant: FLUOR CORPORATION ,  MAK, John ,  GRAHAM, Curt ,  NIELSEN, Richard

    Inventor： MAK, John ,  GRAHAM, Curt ,  NIELSEN, Richard

    IPC: B01D53/14

    CPC classification number: B01D53/1493 ,  B01D53/1475 ,  Y02C10/06

    Abstract: A plant includes an absorber (103) that operates in a gas phase supercritical region and removes an acid gas from a feed stream (9) at high recovery of the feed stream (10) while producing a high purity acid gas stream (36). Particularly preferred plants include gas purification plants that receive a feed gas with at least 5 mol % carbon dioxide at a pressure of at least 3000 psi.

    Abstract translation: 植物包括在气相超临界区域中操作并在高回收率的进料流（10）中从进料流（9）中除去酸性气体同时产生高纯酸性气流（36）的吸收器（103）。 特别优选的设备包括气体净化设备，其在至少3000psi的压力下接收具有至少5mol％二氧化碳的进料气体。

    LNG REGASIFICATION CONFIGURATIONS AND METHODS
    9.
    发明申请
    LNG REGASIFICATION CONFIGURATIONS AND METHODS 审中-公开
    LNG注册配置和方法

    公开(公告)号：WO2006004723B1

    公开(公告)日：2006-08-17

    申请号：PCT/US2005022880

    申请日：2005-06-27

    Applicant: FLUOR TECH CORP ,  MAK JOHN ,  NEUMANN RALPH ,  GRAHAM CURT ,  HEFFERN DAN

    Inventor： MAK JOHN ,  NEUMANN RALPH ,  GRAHAM CURT ,  HEFFERN DAN

    IPC: F25J3/00 ,  F17C9/02

    CPC classification number: F25J3/0214 ,  F25J3/0233 ,  F25J3/0238 ,  F25J3/0242 ,  F25J2200/02 ,  F25J2200/04 ,  F25J2200/72 ,  F25J2200/74 ,  F25J2205/04 ,  F25J2215/62 ,  F25J2235/60 ,  F25J2240/02 ,  F25J2245/02 ,  F25J2270/02 ,  F25J2290/10

    Abstract: LNG composition of LNG from a storage tank or other source is modified in a process in which the LNG is pumped to a first pressure and split into two portions. One portion of the pressurized LNG is then reduced in pressure and heavier components are separated from the reduced pressure LNG to thereby form a lean LNG. The lean LNG is then pumped to a higher pressure and combined with the other portion to form a leaner LNG. Preferably, separation is performed using a demethanizer, wherein part of the demethanizer overhead product is condensed to form the lean LNG, while another portion is used for column reflux. In further preferred configurations, ethane recovery is variable and in yet other configurations, propane or ethane can be delivered via a batching pipeline.

    Abstract translation: 在LNG被泵送到第一压力并分成两部分的过程中，来自储罐或其它源的LNG的LNG组成被改变。 加压LNG的一部分然后在压力下减小，较重的部件与减压LNG分离，从而形成贫LNG。 然后将贫LNG泵送到更高的压力并与其它部分组合以形成较稀的LNG。 优选地，使用脱甲烷塔进行分离，其中部分脱甲烷塔顶产物被冷凝以形成贫LNG，而另一部分用于塔回流。 在进一步优选的构造中，乙烷回收是可变的，并且在其它构型中，丙烷或乙烷可以经由配料管道输送。

    CONFIGURATIONS AND METHODS FOR LNG REGASIFICATION AND BTU CONTROL
    10.
    发明申请
    CONFIGURATIONS AND METHODS FOR LNG REGASIFICATION AND BTU CONTROL 审中-公开

    公开(公告)号：WO2006066015A3

    公开(公告)日：2006-06-22

    申请号：PCT/US2005/045455

    申请日：2005-12-13

    Applicant: FLUOR TECHNOLOGIES CORPORATION ,  MAK, John ,  GRAHAM, Curt

    Inventor： MAK, John ,  GRAHAM, Curt

    IPC: B01D53/14 ,  F25J1/00

    Abstract: LNG is pumped to supercritical pressure and vaporized, preferably in an offshore location to thereby form a natural gas stream with an intermediate temperature. A first portion of that stream is then processed in an onshore location to remove at least some non-methane components to thereby form a lean LNG, which is then combined with a second portion of that stream to form a sales gas having desired chemical composition. The intermediate temperature and the split ratio of the gas stream in first and second portion are a function of the concentration of the non-methane components in the LNG.

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