An optical monitoring system is provided for use with a blood processing system having a yoke that rotates an umbilicus about a rotational axis at a first speed, which causes rotation of an associated centrifuge at a second speed about the rotational axis that is different from the first speed. The system includes a light source configured to illuminate a disposable flow circuit received in the centrifuge and a light detector configured to receive an image of the disposable flow circuit to detect the location of an interface between separated blood compenents within the disposable flow circuit. The monitoring system may be positioned outside of the centrifuge bucket which receives the centrifuge and is configured to be in a fully operational mode for interface detection only when a transparent portion of the centrifuge is visible to the monitoring system.

A centrifuge rotor having a curved shape is offset on a spinning rotor base and creates contiguous areas of low to high centrifugal force depending on the distances from the axis of the rotor base and a method of separating components in a fluid based upon a difference in density of the components, the method comprising the steps of providing to a rotor as described herein the fluid containing the mixed together components to be separated based upon the difference in density of the mixed together components; continuously flowing the components in the fluid to the rotor through an input tube connected to the input port while the rotor is spinning about a centrifugal axis of rotation; separating the components in the fluid into fractions based upon the difference in density of the mixed together components with the use of centrifugal force when the rotor is spinning; collecting components having i) a first density via a first tube connected to the output port at the first end on the rotor, ii) a second density via a second tube connected to the output port at the second end on the rotor, iii) a third density via a third tube connected to the output port at the junction on the rotor and iv) a fourth density via a fourth tube connected to the output port between the input port and the output port at the first end.

Centrifugation systems and methods are provided for separating blood into its constituent parts. Inner and outer walls of a centrifuge each include a projection which extends toward the other wall. A separation chamber is received in the centrifuge between the walls, with the chamber including an inlet port for flowing blood into the chamber, a plasma outlet port for flowing plasma out of the chamber, and a red cell outlet port for flowing red blood cells out of the chamber. With the chamber received in the centrifuge between the walls, the first projection extends into the path of separated blood components flowing toward the plasma outlet port and prevents cellular blood components from flowing into the plasma outlet port. The second projection extends into the path of separated blood components flowing toward the red cell outlet port and prevents plasma from flowing into the red cell outlet port.

Systems and methods are provided for separating blood into two or more separated blood components. The system includes a blood separation chamber with a single stage having five ports connected thereto. The five ports include a blood inlet port, a red blood cell outlet port, a platelet-rich plasma outlet port, a platelet-poor plasma outlet port, and a buffy coat outlet port. In the single stage, blood may be separated into a variety of components, such as red blood cells and platelet-rich plasma or red blood cells, platelet-poor plasma, and buffy coat. Depending on the components into which the blood is to be separated, flow out of one or more of the outlet ports may be prevented.

A modular cassette is provided for separating a composite fluid into at least two component parts thereof during centrifugation. The modular cassette includes: a housing defining a fluid inlet, a fluid outlet, and a chamber for fluid separation; a fluidic channel configured to provide fluid communication between at least two components of the modular cassette; a heat expanding valve including: a flow pathway including undulations configured to facilitate closing of the fluidic channel, wherein the heat expanding valve occludes one or more of the undulations of the flow pathway to close the fluidic channel; and a heating element configured to actuate the heat expanding valve.

Centrifugation systems and methods are provided for separating blood into its constituent parts. Inner and outer walls of a centrifuge each include a projection which extends toward the other wall. A separation chamber is received in the centrifuge between the walls, with the chamber including an inlet port for flowing blood into the chamber, a plasma outlet port for flowing plasma out of the chamber, and a red cell outlet port for flowing red blood cells out of the chamber. With the chamber received in the centrifuge between the walls, the first projection extends into the path of separated blood components flowing toward the plasma outlet port and prevents cellular blood components from flowing into the plasma outlet port. The second projection extends into the path of separated blood components flowing toward the red cell outlet port and prevents plasma from flowing into the red cell outlet port.

Fluid separation chambers are provided for rotation about an axis in a fluid processing system. The fluid separation chamber may be provided with first and second stages, with the first and second stages being positioned at different axial locations. In another embodiment, at least one of the stages may be provided with a non-uniform outer diameter about the rotational axis, which may define a generally spiral-shaped profile or a different profile for fractionating a fluid or fluid component. One or more of the stages may also have a varying outer diameter along the axis. The profile of the chamber may be provided by the chamber itself (in the case of rigid chambers) or by an associated fixture or centrifuge apparatus (in the case of flexible chambers).

An apparatus for separating cell suspension material into centrate and concentrate, includes a single use structure (178, 240, 250, 370, 414) releasably positioned in a cavity in a solid wall rotatable centrifuge bowl (172). The bowl and portions of single use structure rotate about an axis (174, 428). A stationary inlet feed tube (184, 430), a centrate discharge tube (212, 436) and a concentrate discharge tube (230,448) extend along the axis of the rotating single use structure. A centrate centripetal pump (208, 438) is in fluid connection with the centrate discharge tube. A concentrate centripetal pump (216, 450) is in fluid connection with the concentrate discharge tube. At least one concentrate channel (380, 454) and a concentrate centripetal pump chamber (376,452) have configurations in the structure that facilitate the flow of cell concentrate.

An apparatus for separating cell suspension material into centrate and concentrate, includes a single use structure (178, 240, 250) releasably positioned in a cavity in a solid wall rotatable centrifuge bowl (172). The bowl and portions of single use structure rotate about an axis (174). A stationary inlet feed tube (184), a centrate discharge tube (212) and a concentrate discharge tube (230) extend along the axis of the rotating single use structure. A centrate centripetal pump (208) is in fluid connection with the centrate discharge tube. A concentrate centripetal pump (216) is in fluid connection with the concentrate discharge tube. A controller (274) operates responsive to sensors (264, 270) in respective centrate and concentrate discharge lines (262, 268), to control flow rates of a concentrate pump (272) and a centrate pump (266) to produce output flows of cell concentrate and generally cell free centrate.

A centrifugal field-flow fractionation device is provided with a controller for controlling introduction of a liquid sample by a sample introduction part and rotation of the rotor by a motor. The controller rotates the rotor at a first rotational speed when introducing the liquid sample into a flow path. The first rotational speed is faster than a second rotational speed. Therefore, when a liquid sample is introduced into the flow path, high centrifugal force can be applied to the liquid sample, which can suppress the variation of the particles in the liquid sample introduced to the flow path. The controller rotates the rotor at the second rotational speed slower than the first rotational speed with the liquid sample flow in the flow path stopped. Therefore, it is possible to prevent the constant application of high centrifugal force to the liquid sample, thereby suppressing the increase in the length of time required for analysis.