Abstract:
A frustro-conical chamber for separating particles in a fluidized bed for blood component or cell separation. The chamber is characterized by injection-directing means for directing inflowing fluid along a frustro-conical wall of the chamber. A dam adjacent the cell-injection port may be circumferentially disposed within the chamber and may have its maximum height adjacent an injection port, and the height may diminish away from the injection port. The injection directing means may comprise a shelf extending into the interior of the chamber from the injection port, thereby impeding fluid flow in the direction of an outlet port.
Abstract:
Provided is a method for producing platelets, in which damage to platelets is suppressed compared with a method in which platelets are separated using a filter from a megakaryocyte culture, and then the platelets are concentrated using a hollow fiber membrane and are further washed using the hollow fiber membrane, and purified platelets can be produced in a shorter period of time compared with the time that is taken to perform the above-described method so as to reduce damage to platelets. The method for producing purified platelets of the present invention includes a concentrating step of concentrating a megakaryocyte culture, and a centrifuging step of centrifuging platelets from an obtained concentrate.
Abstract:
A solid or screen bowl decanting-type centrifuge comprising:a rotatable bowl; a helical scroll conveyor which rotates coaxially within the bowl at a different rotational speed, the helical scroll comprising a hub carrying a plurality of flights whose radially outer edges lie close to an inner wall of the bowl such that, in use, solids are scrolled by the conveyer to solids discharge ports at one end of the bowl, with separated liquid being discharged from liquids discharge ports at the opposite end of the bowl. The conveyor hub carries a plurality of nozzles in a wash zone for supplying wash fluid to solids being scrolled by the conveyer towards the solids discharge ports. The conveyor hub also carries a blade in the region of the nozzles and intermediate adjacent flights of the conveyor for directing fluid droplets from the nozzles over said solids.
Abstract:
A solid or screen bowl decanting-type centrifuge comprising: a rotatable bowl; a helical scroll conveyor which rotates coaxially within the bowl at a different rotational speed, the helical scroll comprising a hub carrying a plurality of flights whose radially outer edges lie close to an inner wall of the bowl such that, in use, solids are scrolled by the conveyer to solids discharge ports at one end of the bowl, with separated liquid being discharged from liquids discharge ports at the opposite end of the bowl. The conveyor hub carries a plurality of nozzles in a wash zone for supplying wash fluid to solids being scrolled by the conveyer towards the solids discharge ports. The conveyor hub also carries a blade in the region of the nozzles and intermediate adjacent flights of the conveyor for directing fluid droplets from the nozzles over said solids.
Abstract:
A bio cell cleaning centrifuge having a detachable inner chamber body. The centrifuge includes a rotor detachable from a drive mechanism. Test tube holders are pivotally movably supported on the rotor for holding test tubes. A cleaning liquid distributor is detachably disposed on the rotor for supplying cleaning liquid to the respective test tubes. A bowl detachable from the drive mechanism is disposed below the test tube holders. The inner chamber body is disposed below the bowl for receiving therein supernatant liquid discharged out of the test tubes during rotation of the rotor. The inner chamber body is detachably mounted on a main case. The inner chamber body is detached after the distributor, the rotor, and the bowl are detached.
Abstract:
A solids dryer is post-connected to an invertible filter centrifuge, wherein a dehumidification and drying of the solids takes place in the invertible filter centrifuge by means of centrifugation, pressure gas compression and/or heat convection and in the solids dryer by means of heat contact and/or heat convection. The invertible filter centrifuge and the solids dryer are connected to one another to form a unit via a closure device. Sensors serve to measure the respectively prevailing degree of dehumidification and drying as well as to determine additional operating parameters. The sensors actuate a common control device which regulates the operating parameters. The control device carries out the regulation of the operating parameters automatically in such a manner that the operating times for the dehumidification and drying in the invertible filter centrifuge and in the solids dryer are coordinated with one another and at the same time the mechanical centrifugal energy and the thermal energies in invertible filter centrifuge and solids dryer are distributed in an optimum manner.
Abstract:
A liquid-solids separator, or centrifuge, of the type having a screw conveyor is provided with a series of offset conveyor flights. A spacer is positioned within the offset of the conveyor flights to form a channel therein. Rinse liquid is introduced into the channel through the central hub of the conveyor. The channel directs the rinse liquid into the heavy phase cake. An opening may be provided at various radial distances for varying the position of introduction of the rinse liquid from the channel. The amount of rinse liquid introduced through various channels formed by the series of offset conveyor flights may also be varied.
Abstract:
A centrifugal separation method for living cells is disclosed in which a cell containing solution is charged in a rotor chamber confined by a steam pressure-resistant wall. A rotor having septa is disposed in the rotor chamber. The septa are rotatable in the same direction at the same angular velocity as the rotor while at least part thereof is immersed in a solution in the rotor when cells are to be centrifuged from the cell-containing solution. After the cells are separated and adhered to the inner surface of the rotor, a supernatant in the rotor is discharged form the rotor. Then a fresh cultivating medium is introduced into the rotor, and the septa and the rotor are rotated at mutually different angular velocities while at least part of the septa is immersed in the fresh medium in the rotor. As a result, the cells are again suspended in the fresh medium.
Abstract:
Screw conveyor of solid bowl centrifuge has its flight member modified at the bowl dry beach area by welding sheet metal, for example, to trailing surfaces of the flight forming a chamber for rinse liquid driven thereinto. Leading or working surfaces of the flight are provided with a plurality of series of orifices per 360.degree. revolution thereof, each series comprising spaced orifices extending inwardly from a distal portion thereof and preferentially angled therethrough. Overflow passageways with cooperating baffles are provided. Thus, rinse liquid passes onto solids pile surfaces through orifices immediately inwardly thereof as well as through orifices submerged by the solids for passage of rinse liquid thereinto.
Abstract:
The method, and system for carrying out the steps of the method, are utilized in taking whole blood from a supply of blood withdrawn from a donor or from a previously banked supply of whole blood in a container, centrifuging the blood in a centrifuge device to separate the whole blood into its components, and then collecting the components, namely red blood cells, white blood cells, platelets and plasma. The fractionation of the whole blood in the centrifuge device takes place in first, second and third separation chambers. The first chamber has a square shape and is positioned in the centrifuge device in a diamond position. Each corner of the first separation chamber has an opening. Whole blood is pumped into one side corner opening and red blood cells are withdrawn from the other side corner opening and returned to the container for recirculation through the first chamber. White blood cells, platelets and plasma are withdrawn from the upper corner opening and passed through the second chamber wherein white blood cells are separated by centrifugal force. The plasma and platelets are then withdrawn from the second chamber and passed through the third chamber wherein the platelets are separated from the plasma by centrifugal force. The plasma exiting from the third separation chamber is passed back into the bottom corner of the first chamber to cause a flow of plasma across the flow of whole blood and red blood cells to elute white blood cells and plateletstherefrom and to wash the red blood cells. By appropriate operation of electromechanically controlled clamps associated with tubing carrying the various blood components, plasma can be siphoned off into a plasma collection receptacle located outside the centrifuge device. After the red blood cells have been recirculated several times through the first separation chamber, the red blood cells then can be directed to a red blood cell collection receptacle by operation of other electromechanically controlled clamps.