Baxter International Inc.

Baxter Travenol Laboratories, Inc.

Omnis Surgical Inc.

Kenneth M Johnson

Ronald J Leonard

Mary A Stewart

Thomas L Drehobl

Samira E Monaghan

The present invention provides a coextruded tubing that has been optimized for usage in cryogenic freezing applications. To this end, a coextruded tubing is provided having three layers, a first layer of ethylene vinyl acetate; a second layer of polyolefin; and a third layer of polyvinyl chloride. An improved container for use in cryogenic freezing applications is also provided.

Cryogenic resistant coextruded tubing

Systems and methods for collecting blood substantially free of undesired matter assure that accurate crossmatching and typing of cellular blood components can be done prior to transfusion, even though the cellular components are collected and stored in different containers. The blood containing the undesired matter is collected in a blood collection container. The blood collection container includes a tube that is sealed for retaining samples of the collected blood for later analysis. The collected blood is conveyed out of the blood collection container for removal of undesired matter. The blood substantially free of the undesired matter is collected in a separate transfer container for storage. The distal end of the sealed tube containing the blood samples is attached to the transfer container, while the other end of the sealed tube is disconnected from the original blood collection container. This leaves the sealed tube and, with it, the retained blood sample, attached only to the transfer container, which now holds blood substantially free of undesired matter. Using the systems and methods, direct traceability can be assured between red blood cells made substantially free of white blood cells for transfusion and the donor from whom the red blood cells were obtained.

Systems and methods for removing undesired matter from blood cells

Systems and methods of collecting blood cells use a first container connected to initially collect blood. A filtration system is provided that uses two flow paths, the first being a dual purpose path that is initially used to convey plasma and platelets to a pair of transfer/storage containers. A second flow path leads to a temporary transfer container through a filtration device. The dual purpose fluid path is next used to convey blood cells, now substantially free of undesired matter, from the temporary storage container to a storage container. The filtration system is then detached from the blood collection system.

A mass transfer device (60) includes a hollow fiber bundle (10) comprising a generally cylindrical core (14) having opposed ends, a plurality of layers of hollow fiber (12) that have been wound around the core, and binding means (48a, 48b, 48c), such as double-sided pressure-sensitive tape that have been wound around the layers of hollow fiber in a plurality of longitudinally spaced locations along the core and intermediate the opposite ends of the core for providing longitudinally spaced support means for the hollow fiber bundle. The hollow fiber bundle is enclosed in a housing (62) having an inner wall (80) which defines a generally circular opening for receiving the hollow fiber bundle except that the inner wall adjust a fluid outlet manifold (74) includes an expansion volume (82) for the hollow fibers that are adjacent that fluid outlet manifold. A screen (88) is provided adjacent the fluid outlet manifold to prevent the fibers from migrating too far into the outlet and to provide a controlled expansion.

Hollow fiber bundle having transverse binding means and method of making

A heat exchanger (38) is provided which may be used in a mass transfer device (20), such asn an oxygenator or a dialyzer. The heat exchanger comprises a core (40) formed of a corrugated metal having a high thermal conductivity. Each of the corrugations of the core comprises substantially parallel side walls (70, 72). A first fluid, such as blood, is introduced onto the outside of the core. A second fluid, such as water, is introduced into the inside of the core. The first and second fluids will be in heat exchange relationship with each other and the flow of the fluids is substantially uniform resulting from the substantially parallel side walls of the corrugations. The core is formed by providing a flexible metalhose, annealing the flexible metal hose, compressing the annealed hose and expanding the compressed hose to a length that is substantially less than its original length but greater than its length during compression.

Mass transfer device having a heat-exchanger

A mass transfer device (60) includes a hollow fiber bundle (10) comprising a generally cylindrical core (14) having opposed ends, a plurality of layers of hollow fiber (12) that have been wound around the core, and binding means (48a, 48b, 48c) such as double- sided pressure-sensitive tape that have been wound around the layers of hollow fiber in a plurality of longitudinally spaced locations along the core and intermediate the opposite ends of the core for providing longitudinally spaced support means for the hollow fiber bundle. The hollow fiber bundle is enclosed in a housing (62) having an inner wall (80) which defines a generally circular opening for receiving the hollow fiber bundle except that the inner wall adjacent a fluid outlet manifold (74) includes an expansion volume (82) for the hollow fibers that are adjacent that fluid outlet manifold. A screen (88) is provided adjacent the fluid outlet manifold to prevent the fibers from migrating too far into the outlet and to provide a controlled expansion.

Mass transfer device

A bundle (12) of hollow fiber (34) is formed by winding a length of hollow fiber around a core (38) from an arm (20) that is in a plane at an acute angle with respect to the longitudinal axis of the core and is between opposite ends of the core. Relative rotation is provided between the longitudinal axis of the core and the position of the winding arm. During winding of the hollow fiber around the core, there is an increase in the ratio of (a) the angular velocity of the wind and (b) the relative rotational velocity between the longitudinal axis of the core and the position of the winding arm. In this manner, the void fraction of radially-outward annuli of the wound bundle is less than the void fraction would be if the ratio remained constant.

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Lindenhurst, IL, United States of America

Kenneth M Johnson