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    • 111. 发明申请
    • FLUID SEPARATION DEVICES, SYSTEMS AND/OR METHODS USING A FLUID PRESSURE DRIVEN AND/OR BALANCED CONFIGURATION
    • 使用流体压力驱动和/或平衡配置的流体分离装置,系统和/或方法
    • WO02062482A2
    • 2002-08-15
    • PCT/US0146940
    • 2001-11-02
    • GAMBRO INC
    • HLAVINKA DENNIS JFELT THOMAS J
    • A61M1/02A61M1/36A61M1/38B04B5/04B04B7/08B04B9/08B04B
    • B04B5/0442A61M1/0231A61M1/3693A61M1/3696A61M1/38B04B5/0428B04B7/08B04B9/08B04B2005/045B04B2005/0464B04B2009/143
    • A centrifugal fluid separation system is disclosed for centrifugally separating a composite fluid into components thereof. This centrifugal separation system includes at least a centrifugal rotor which has a composite fluid containment area, several fluid flow channels and at least two separated component collection areas defined therein. A composite fluid to be separated is delivered to the fluid containment area from which it travels through an inlet channel to a substantially circumferential fluid separation channel where under centrifugal forces the composite fluid is separated into components which each then travel to distinct first and second separated fluid outlet channels, and thence on to exit therefrom into the respective collection areas. The first and second fluid outlet channels also have respective first and second heights which are related to each other so as to provide a balanced fluid pressure relationship for the respective separated component fluids flowing therethrough. Such a pressure balance controls the interface of the separated fluid components within the circumferential separation channel. The preferred fluid pressure balance relationship is rho 2g2h2 = rho 3g3h3 wherein the first height of the first outlet channel is h2, and the second height of the second outlet channel is h3, wherein g2 and g3 are gravitational or centrifugal acceleration values and rho 2 and rho 3 represent the respective densities of the separated fluids in the first and second outlet channels. A similar, continuously forward flow drive relationship involves also the height h1 of the inlet channel and the density rho 1 of the fluid therein such that rho 1g1h1 > rho 2g2h2 or rho 1g1h1 > rho 3g3h3. The preferred centrifugal drive motor used here produces a rotating magnetic field, which co-acts with a magnetically reactive material disposed in the rotor to rotate the rotor with the rotating magnetic field. A loopless, sealless continuous flow centrifuge is thus available herefrom. Adisposable bag and tubing system is also disclosed for use with preferably reusable rotor devices.
    • 公开了用于将复合流体离心分离成其组分的离心流体分离系统。 该离心分离系统至少包括具有复合流体容纳区域,若干流体流动通道和限定在其中的至少两个分离的部件收集区域的离心转子。 要分离的复合流体被输送到流体容纳区域,从该入口通道行进通过入口通道到基本上圆周的流体分离通道,在离心力作用下,复合流体被分离成各自分成不同的第一和第二分离流体 出口通道,然后从那里退出到相应的收集区域。 第一和第二流体出口通道还具有彼此相关的相应的第一和第二高度,以便为流过其中的各个分离的组分流体提供平衡的流体压力关系。 这种压力平衡控制在圆周分离通道内的分离的流体组分的界面。 优选的流体压力平衡关系为rho 2g2h2 = rho 3g3h3,其中第一出口通道的第一高度为h2,第二出口通道的第二高度为h3,其中g2和g3为重力或离心加速度值,rho 2和 rho 3表示第一和第二出口通道中分离的流体的相应密度。 类似的,连续向前的流动驱动关系还涉及入口通道的高度h1和其中流体的密度rho 1,使得r 1g1h1> rho 2g2h2或rho1g1h1> rho3g3h3。 这里使用的优选的离心驱动马达产生旋转磁场,其与设置在转子中的磁反应性材料共同作用,以使转子与旋转磁场一起旋转。 因此,可以使用无孔,无密封的连续流离心机。 还公开了可用于优选可重复使用的转子装置的相关袋和管系统。
    • 117. 发明专利
    • DE60035474T2
    • 2008-03-13
    • DE60035474
    • 2000-12-22
    • GAMBRO INC
    • BAINBRIDGE MARLENEFELT THOMAS
    • A61M1/38A61M1/30A61M1/34A61M1/36
    • A method and apparatus for controlling a fluid separation system in response to fluid pressure changes in a fluid flow, said method comprising the steps of sensing a fluid pressure; comparing the fluid pressure to a threshold value, and if the fluid pressure is below the threshold value, then pausing fluid flow for a selected period. During the selected period, either the fluid pressure sensed automatically resolves or the method further comprises a step of setting a full alarm condition. The method and apparatus may further include interpreting a particular quantity of fluid pressure comparisons where the fluid pressure is below the threshold value occurring within a particular time period, and then, signaling an alarm. Threshold values may be calculated by the method or apparatus according to a formula such as the following: Threshold Value = Config + 75 - 0.3309 * Qin/(1-Hin) - 0.3026 * Qn/(1-Hn) ; where, Config = a configuration pre-selected pressure value Qin = fluid flow rate in the inlet tubing line; Hin = Hematocrit in the inlet tubing line; Qn = fluid flow rate in the needle; and Hn = Hematocrit in the needle.