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    • 1. 发明授权
    • Modified surface for reducing the turbulences of a fluid and transportation process
    • 用于减少流体和运输过程的湍流的改性表面
    • US06193191B1
    • 2001-02-27
    • US08892268
    • 1997-07-14
    • Jean FalcimaigneThierry PalermoAlexandre Rojey
    • Jean FalcimaigneThierry PalermoAlexandre Rojey
    • B64C2110
    • F15D1/065B64C21/10Y02T50/166
    • The invention is a structure for inhibiting the turbulence phenomena of a fluid, exhibiting a surface geometry comprising at least one series of inhibition surfaces which inhibit turbulence present in a boundary layer of the fluid in proximity to the wall of the structure and which extend substantially longitudinally in the direction of flow of the fluid. The inhibition surfaces comprise at least a first series of surfaces (01) of amplitude a1 and at least a second series of surfaces (02) of amplitude a2. The second series of surfaces (02) is arranged so as to be superposed on the first series of surfaces (01), the first series of surfaces (01) allowing inhibition of at least turbulence of great amplitude and the second series of surfaces (02) allowing inhibition of at least turbulences of low amplitude. The structure has an application for forming at least part of a pipe for conveying a pressurized gas.
    • 本发明是一种用于抑制流体的湍流现象的结构,其表现出几何形状,其表面几何形状包括至少一系列抑制表面,其抑制流体边界层中邻近结构壁的紊流, 在流体的流动方向上。 抑制表面包括幅度为a1的至少第一系列表面(01)和振幅a2的至少第二系列表面(02)。 第二系列表面(02)被布置成叠置在第一系列表面(01)上,第一系列表面(01)允许抑制至少湍流的大振幅和第二系列表面(02 )允许至少抑制低振幅的湍流。 该结构具有用于形成用于输送加压气体的管道的至少一部分的应用。
    • 4. 发明申请
    • METHOD OF SEPARATING TWO DISPERSED-PHASE IMMISCIBLE LIQUIDS
    • 分离两相不稳定液体的方法
    • US20120125868A1
    • 2012-05-24
    • US13265580
    • 2010-04-21
    • Stefano FalappiThierry PalermoChristine NoikBenjamin BrocartAlain Ricordeau
    • Stefano FalappiThierry PalermoChristine NoikBenjamin BrocartAlain Ricordeau
    • B01D17/025
    • B01D17/0211B01D17/0214B01D17/047
    • Method of separating two dispersed-phase immiscible liquids. The two liquids are fed into a gravity separator where both liquids are separated by decantation. A first phase consisting of a first liquid is obtained at the bottom of the separator, a second phase consisting of the second liquid is obtained at the tap of the separator, a third phase containing the two dispersed-phase immiscible liquids and a fourth phase containing the two immiscible liquids in a dense bed are obtained. Physico-chemical properties of the liquids and of the dispersed phase are measured, and a physical separation model is defined. This model is defined considering that the separator works under stationary conditions, using a matter conservation balance for the first fluid within the dense bed, while taking account of a first phenomenon of coalescence between water drops within the third phase, and of a second phenomenon of coalescence between water drops of the fourth phase and the first phase. This model is then used to optimize implementation of the separation. Application to the separation of petroleum effluents for example.
    • 分离两种分散相不混溶液体的方法。 将两种液体进料到重力分离器中,其中两种液体通过倾析分离。 在分离器的底部获得由第一液体组成的第一相,在分离器的龙头处获得由第二液体组成的第二相,含有两个分散相不混溶液体的第三相和含有 获得致密床中的两种不混溶液体。 测量液体和分散相的物理化学性质,并定义物理分离模型。 考虑到分离器在稳定条件下工作,使用密度床内的第一流体的物质保持平衡,同时考虑到在第三阶段内的水滴之间的第一次聚结现象,以及第二现象 第四相水滴与第一相之间的聚结。 然后,该模型用于优化分离的实现。 例如应用于石油流出物的分离。
    • 6. 发明授权
    • Method and a device for separating a continuous fluid phase from a
dispersed phase
    • 方法和用于从分散相分离连续流体相的装置
    • US5252229A
    • 1993-10-12
    • US717001
    • 1991-06-18
    • Alexandre RojeyJean-Claude CollinThierry Palermo
    • Alexandre RojeyJean-Claude CollinThierry Palermo
    • B01D17/02B01D21/26
    • B01D17/0205B01D17/0217Y10S210/05
    • A method and device for separating a continuous phase from at least one dispersed phase, with the phases having different densities. A mixture of the phases to be separated is supplied into a device including at least one cylindrical chamber vertically disposed and at least one static helically-shaped member is accommodated in the chamber. At least one face of the helically-shaped member is formed by a helicoidal surface. A maximum free path of a dispersed phase particle in a radial direction prior to colliding with the helically-shaped member is less than one quarter of a peripheral diameter of the member and, preferably, less than one tenth of an internal diameter of the chamber. The method and apparatus are capable of separating an aqueous phase from an organic phase such as, a petroleum fluid, with the mixture to be separated also possibly including a gaseous phase and a solid phase.
    • 用于从至少一个分散相分离连续相的方法和装置,所述相具有不同的密度。 要分离的相的混合物被供应到包括垂直设置的至少一个圆柱形室的装置中,并且至少一个静态螺旋形构件容纳在室中。 螺旋形构件的至少一个面由螺旋形表面形成。 在与螺旋形构件碰撞之前,径向方向上的分散相颗粒的最大自由路径小于构件的周边直径的四分之一,并且优选地小于室的内径的十分之一。 该方法和装置能够将水相与有机相如石油流体分离,待分离的混合物也可能包括气相和固相。