|Publication number||US3885735 A|
|Publication date||May 27, 1975|
|Filing date||Aug 27, 1973|
|Priority date||Nov 2, 1972|
|Also published as||DE2354368A1|
|Publication number||US 3885735 A, US 3885735A, US-A-3885735, US3885735 A, US3885735A|
|Inventors||J Eric H Westbert|
|Original Assignee||J Eric H Westbert|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (5), Referenced by (35), Classifications (15)|
|External Links: USPTO, USPTO Assignment, Espacenet|
United States Patent [191 Westbert 51 May 27, 1975 CENTRIFUGE APPARATUS  Inventor: J. Eric H. Westbert, Rodstuguvagen 14, 181 31 Lidingo, Sweden  Filed: Aug. 27, 1973  Appl. No.: 391,537
 Foreign Application Priority Data Nov. 2, 1972 Sweden 14193/72  US. Cl 233/25; 233/27  Int. Cl B04b 5/00  Field of Search 233/14 R, 23 A, 25, 26, 233/27, 1 R
 References Cited UNITED STATES PATENTS 489,202 1/1893 Peck 233/25 X 3,235,173 2/1966 Unger 233/26 X 3,347,454 10/1967 Bellamy et a1. 233/26 X 3,674,197 7/1972 Mitchell et al 3,684,161 8/1972 Unger et a1. 233/26 Primary Examiner-George H. Krizmanich  ABSTRACT A centrifuge apparatus, primarily for use in the continuous or semi-continuous separation of blood, has a disposable separation unit which is orbited on a centrifuge rotor. The separation unit has a sealed jacket which is held against rotation during the orbiting and communicates with a stationary and nonrotatable liquid inlet and outlet connector on the rotor axis. A separation vessel rotatably mounted in the jacket communicates with liquid inlet and outlet passages in the jacket and is rotationally unbalanced to orient itself relative to the rotor during the orbiting of the jacket.
14 Claims, 9 Drawing Figures FATENTEU vf3 885,735
SHEET 1 I Fig. 7 ,0 29 22 33 12 2/ 3028 2 FATE MED E IAY 2 7 i975 SHEET CENTRIFUGE APPARATUS BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to centrifugal separation ofliquid and, more particularly, to centrifuge apparatus of the type having a centrifuge rotor which carries a container for the liquid to be separated and rapidly orbits the container about the axis of rotation of the rotor, as well as inlet and outlet conduits continuously conveying liquid to and from the container while the latter is being orbited. The invention is particularly useful in connection with the separation of blood or other biological liquids and accordingly the following description will be devoted primarily to that application.
2. Prior Art In centrifuge apparatus of the aforementioned type, the continuous transfer of liquid between the orbiting container, in which the separation takes place, and the stationary accessories for conveying liquid to and from the container (such accessories may include a pump, a source of the liquid to be separated and one or more vessels for receiving and isolating separated fractions), involves difficult sealing problems, because the liquid transfer has to take place by way of a rotary seal. Such seals typically have a rotary part carried by the rotor on the axis of rotation of the latter and communicating with the container, and a stationary part sealingly engaging the rotary part and communicating with the stationary liquid conveying accessories.
Since a perfect seal between relatively rotating elements is always difficult to accomplish, known centrifuge apparatus often suffers from leakage between the rotary and the stationary parts. Outward leakage may soil the centrifuge, while inward leakage may contaminate the liquid to be separated and/or the separated fractions. Such contamination is particularly troublesome in the case of blood or other biological liquids which have to be treated under sterile conditions.
SUMMARY OF THE INVENTION A general object of the invention is to provide in a centrifuge a separation unit including all the parts which are contacted by the liquid and in which there are no rotary seals between the spaces holding or conveying liquid to be treated and/or separated fractions, on the one hand, and the exterior side of the unit, on the other hand. A more particular object is to accomplish the foregoing general object in a separation unit having relatively few and inexpensive parts and thus lending itself to use as a disposable item.
These and other objects are realized in a separation unit having a jacket or housing which is nonrotatably connected with a connector member through a torsionally rigid but flexible body including conduits for conveying liquid between the connector member and the jacket. A separation vessel rotatably mounted in the jacket communicates with the conduits and includes orientation means. In use of the separation unit, the jacket is rotatably mounted on a centrifuge rotor and orbited about the axis of rotation of the rotor but held against rotation by the flexible body and the connector member which is secured to a stationary part of the centrifuge on or near the axis of rotation of the rotor. The orientation means, which preferably include an unbalancing mass, maintain the separation vessel in a fixed angular position relative to the centrifuge rotor so that the heaviest liquid fraction is permitted to settle in the radially outermost portion of the separation vessel while the lighter fraction or fractions are permitted to settle radially inwardly of the heaviest fraction.
The invention will be fully understood from the following detailed description of exemplary embodiments with reference to the accompanying diagrammatic drawings.
ON THE DRAWINGS FIG. 1 is a view in longitudinal section ofa centrifuge constructed in accordance with a first embodiment of the invention and includes a diagrammatic representation of accessories for feeding liquid to and receiving liquid from the centrifuge;
FIG. 2 is an enlarged fragmentary view in longitudinal section of a portion of the centrifuge shown in FIG.
FIGS. 3A and 3B are diagrammatic cross-sectional views of the rotor of the centrifuge shown in FIG. 1;
FIG. 4 is a view in longitudinal section of a separation unit constructed in accordance with a second embodiment of the invention;
FIGS. 5 and 6 are cross-sectional views on lines V-V and Vl-VI, respectively, in FIG. 4;
FIG. 7 is a diagrammatic view, partly in vertical section, of a centrifuge apparatus provided with the separation unit shown in FlG. 3 and accessories for feeding liquid to and from the separation unit;
FIG. 8 is a view in longitudinal section showing a modification of the lower portion of the separation unit of FIG. 4.
AS SHOWN ON THE DRAWINGS The centrifuge 10 shown in somewhat diagrammatic form in FIGS. 1 and 2 comprises a base plate 11 on which a hollow, generally cylindrical centrifuge rotor 12 is supported for rotation about a horizontal axis 13 in antifriction bearings 14. A drive unit including an electric motor 15 and a belt transmission 16 as well as control apparatus and a brake mechanism (not shown) is capable of rotating the rotor 12 at high speed and of rapidly reducing the rotational speed.
Disposed within the rotor 12 and radially displaceable therein along guides 17 to selected radial positions in a separation unit 18. Antifriction bearings 19 support the separation unit 18 for rotation relative to the rotor 12 and the guides 17 about an axis 20 parallel to but spaced from the rotor axis 13. Thus, during the rotation of the rotor 12 the separation unit 18 and, accordingly, the axis 20 are orbited about the rotor axis 13.
The separation unit 18, which may be constructed as a disposable item and discarded after a single use, includes a generally cylindrical housing or jacket 21, a separation vessel 22, which is also generally cylindrical and which is enclosed in the jacket 21 and freely rotatable relative to the latter about the aforementioned axis 20, and two flexible but torsionally rigid conduits 23 and 24 which are constantly in open communication with the separation vessel 22 adjacent opposite ends of the latter and extend from opposite ends of the jacket 21 to stationary brackets 25 disposed on the base plate 11 and holding a portion of each conduit relatively fixed on the rotor axis 13 and without rotation.
The end portions 26 and 27 of the conduits 23 and 24 adjacent the jacket 21 are rigid and fixedly secured to the latter and project coaxially with the jacket into recesses 28 and 29 in the end walls of the separation vessel 22 to form an axle or spindle on which the separation vessel is rotatable about the axis 20. As best seen from FIG. 2, the aforementioned end portions 26 and 27 are each formed by a short length of a metal tube sealingly secured to the end wall of the jacket 21 and sealingly connected with a length of flexible plastic tubing 23A surrounded by a densely coiled helical spring 233 of steel wire.
The separation vessel 22 is rotationally unbalanced with respect to its axis of rotation, which is defined by the axis 20. To this end, an axially extending unbalance weight 30 is attached to the cylindrical wall of the separation vessel. As a consequence, as the separation unit 18 is being orbited about the rotor axis 13, the separation vessel 22 will maintain a constant orientation, that is, a fixed angular or rotational position, relative to an imaginary line intersecting the axes 13 and 20. This is illustrated in FIGS. 3A and 3B which are diagrammatic cross-sectional representations of the rotor 12 and the separation unit 18 with the latter in two different angular positions. As seen from these figures, the separation vessel 22 does not rotate relative to the rotating line 31 joining the rotor axis 13 and the orbiting axis 20. In other words, the separation vessel does not rotate relative to the rotor 12, and hence-every point on the separation vessel is always at a constant distance from the stationary rotor axis 13. The jacket 21, on the other hand, is continuously rotated relative to the rotor 12 about the orbiting axis 20 but does not change its orientation relative to the base plate 11 and the brackets 25. This is also seen from FIGS. 3A and 313 where the little circle 32 represents presents an arbitrarily chosen point on the circumference of the jacket.
As seen from FIG. 1, the two end recesses 28 and 29 are constantly in open communication with the interior of the separation vessel 22 at locations which are on opposite sides thereof. More particularly, the end recess 28 communicates with the separation vessel at a location adjacent the unbalance weight 30, that is, at a location where the contents of the separation vessel are subjected to the greatest centrifugal force during the orbital motion of the separation unit, while the end recess 29 communicates with the separation vessel at a location where the contents are subjected to the smallest centrifugal force.
The jacket 21 and the separation vessel 22 define between them an annular space 33 which extends throughout the length of the separation vessel 22 and communicates with the interior of the latter by way of the small clearances between the end walls of the separation vessel 22 and the spindle tubes 26 and 27; in FIG. 2 the clearance is greatly exaggerated for illustrative purposes. Thus, liquid fed into the separation vessel 22 through one of the flexible conduits 23 and 24 may enter and completely fill the space 33 but since the connections between the jacket 21 and the conduits 26, 27 as well as the jacket itself are sealed, there is no possibility for the liquid to escape from the separation unit 18 except through the conduits.
The operation of the centrifuge with the separation unit 18 will now be explained, assuming that it is being used for plasmapheresis in vivo. Plasmapheresis in vivo means that blood is taken from a live donor and separated into plasma and red blood cells (other components of the blood are disregarded here) whereupon the red blood cells are resuspended in isotonic saline and returned therewith to the donor while the plasma is collected in a separate container.
The auxiliary equipment necessary for plasmapheresis in vivo is diagrammatically shown in FIG. 1 and includes a flexible container 34 holding sterile isotonic saline (0.9 percent salt solution), a flexible container 35 holding an anticoagulant solution labeled ACD, a needle 36 through which blood is drawn from the donor and through which the saline with the red blood cells suspended therein is returned to the donor, a pump 37 connected to the containers 34 and 35 and the needle 36 as well as to one end of the separation unit 18. A third flexible container 38 holding a sterile solution, herein referred to as the priming solution, is connected to the other end of the separation unit.
The internal structure of the pump 37 forms no part of the invention and will not, therefore, be described. The function of the pump, however, will become apparent as the description proceeds. The pumps 37 and the container 38 are connected respectively to the conduit 23 and the conduit 24 by way of flexible conduits 39 having sterile couplings.
The centrifuge rotor 12 is first started and the pump 37 is so operated as to draw the sterile priming solution from the container 38 into the separation vessel 22. The centrifugal force causes the priming solution to enter the annular space 33 and expel all air from the separation unit up to the point of the needle 36.
The needle 36 is then inserted into a vein of the donor and the pump 37 is so operated as to continuously draw blood from the donor, to add anticoagulant solution from the container 35 to the flowing blood and to pump the thus anticoagulated blood into the separation vessel 22. The priming solution in the separation vessel accordingly is gradually forced back to the container 38. In the separation vessel, the centrifugal force separates the incoming blood into a heavier red cell fraction, which is collected in the portion of the separation vessel which is radially outermost with respect to the rotor axis 13 (the upper portion in FIGS. 1, 2 and 3A, 3B) and a lighter plasma fraction which is collected in the radially innermost portion of the separation vessel.
As the separation of the continuously incoming blood proceeds, the separation vessel 22 becomes almost completely filled with a concentrate of red blood cells. At that time the pump 37 is so operated as to draw the cell concentrate from the separation vessel and return it to the donor after the cells have been suspended in saline supplied from the container 341. When practically all blood cells in the separation vessel and the conduits 23 and 39 have been drawn away and replaced by plasma from the container 38, the pump is again as operated as to draw blood from the donor and feed it with anticoagulant solution to the separation vessel whereupon the above-described procedure is repeated. The separation of the blood from the donor thus is accomplished in a semi-continuous fashion and is continued until a sufficient volume of plasma has been collected in the container 38.
As is seen from the foregoing description, there are no rotary seals where the liquid in the closed separation system may become contaminated. The only places where the liquid may leave the desired flow path are the small clearances between the walls of the separation vessel 22 and the tubes 26 and 27, but since the space outside of these clearances is completely filled with the priming solution, the tendency of the blood cells or the plasma to escape through the clearances is practically eliminated and, besides, the minimal escape that might take place causes no harm. The priming solution, which has a density nearly the same as the combined density of the filled separation vessel, also aids in relieving the tubes 26 and 27 from radial forces from the separation vessel 22. The latter practically floats in the priming solution and the tubes 26 and 27 only have to resist relatively small radial forces.
FIGS. 4 to 7 show another embodiment of the centrifuge and the separation unit, generally designated 40 and 41, respectively. Referring first to FIG. 7, the centrifuge 40 includes, in addition to the separation unit, a base plate 42, a cover 43, an electric motor 44 having an upwardly directed shaft 45, and a rotor 46 carried by the motor shaft for rotation about a vertical axis 47.
Adjacent its periphery, the rotor 46 carries a frustoconical socket 48 which is freely rotatable relative to the rotor about an axis 49 intersecting the vertical rotor axis 47 and forming an acute angle a therewith. The socket 48 serves to receive and hold the frusto-conical jacket 50 of the separation unit 41 which includes a connector member 51 nonrotatably held by the top of the cover 43 and a flexible but torsionally rigid, slender body 52 which provides a nonrotatable mechanical connection as well as a fluid flow connection between the jacket and the connector member. Rotation of the rotor 46 thus will cause the jacket 50 to orbit about the rotor axis 47 with the axis 49 generating a cone having its apex on the rotor axis. A counterweight 53 on the rotor balances the latter with respect to its axis 47.
Accessories for feeding liquid to and withdrawing liquid from the separation unit 41 through the connector member 51 include a pump 54 and conduits 55.
Referring to FIG. 4, the jacket 50 comprises a frustoconical cup 56 of circular cross-section and a cover 57 secured to and closing the wide end of the cup. A neck 58 integral with the cover projects axially outwardly from the jacket and serves as an attachment for one end of the flexible body 52, which comprises a pair of flexible conduit sections 59, another pair of similar flexible conduit sections 60, and a wire 61. The wire 61 is torsionally rigid and nonrotatably secured to the neck 58 and the connector member 51 to prevent relative rotation of the jacket and the connector member. The four flexible conduit sections 59, 60 are helically wound about the wire 61, and the conduit sections 59 are in constant open communication with a common passage 62 in the neck 58 and another common passage 63 in the connector member 51. Similarly, the conduit sections 60 are in constant open communication with a common passage 64 in the neck and a common passage 65 in the connector member.
A rigid tube 66, which is secured to the neck 58 and communicates with the passage 62, extends into the cup 56 coaxially with the axis 49 and is rotatably received in a tube 67 in a separation vessel 68 to support the latter for free rotation relative to the jacket 50 about the axes 49. The separation vessel 68 is of the same general shape as the jacket 50 with which it defines a narrow, closed annular space 69 completely surrounding the separation vessel 68. The end of the separation vessel 68 adjacent to the cover 57 is in constant open communication with the neck passage 64 through a passage 70 and the intervening portion of the annular space 69, and the opposite end is in constant open communication with the tube 66 through a passage 71 and the adjacent end portion of the tube 67.
An unbalance weight 72 on the separation vessel 68 serves to keep it in a fixed rotational position relative to the rotor 46 as the separation unit 41 is being orbited, while the wire 61 prevents rotation of the jacket 50 relative to the connector member 51 and, accordingly, the cover 43. As seen from FIG. 4, where a phantom line 73 represents the vertical interface between separated fractions of different densities at an arbitrarily chosen time during a separation process, the unbalance weight 72 is located such that the passage 70 is kept nearer the vertical rotor axis 47 than the passage 71.
The separation unit 41 operates in a manner generally similar to the separation unit 18 of FIG. 1. Assuming that plasmapheresis is to be carried out, sterile priming solution is first fed into the orbiting separation unit through the passage 62 and the conduit sections 59. The priming solution first fills the separation vessel 68, then the annular space 69, the passage 64, the conduit sections 60 and the passage 65.
Blood is then continuously fed into the separation vessel 68 the same way as the priming solution which is thus gradually expelled from the separation vessel through the passages 70 and 64. Red blood cells are concentrated in the radially outermost portion of the separation vessel, to the right of the interface 73, while plasma is collected in the radially innermost portion and expelled therefrom the same way as the priming solution at a rate corresponding to the accumulation of the red cells.
When the separation vessel is almost completely filled with the red cell concentrate, that is, when the interface 73 is near the passage 70, the direction of flow is reversed and plasma (or saline) is returned to the separation vessel to expel the red cell concentrate from the separation unit through the passage 71, the tubes 67 and 66, the passage 62, the conduit sections 59 and the passage 63.
As is best seen from FIG. 7, the flexible body 52 is curved only in one direction and the radius of curvature is relatively long. Accordingly, the body 52 can be made relatively short without attendant risk of fatigue failure. Unwanted oscillations of the flexible body are also practically eliminated by the helical coiling of the conduit sections 59 and 60. From FIGS. 4 to 7 it is also seen that the separation unit 41 is made of relatively few and inexpensive parts that are easy to dispose in and to remove from the centrifuge.
FIG. 8 shows a separation unit permitting a fully continuous separation of blood, for example. The separation unit 80 includes a jacket 81 generally similar to the jacket of the separation unit of FIGS. 4 to 7, and a neck 82 on it is nonrotatably connected with a connector member similar to the connector member 51 by two coaxial helical wire springs 83 and 84 which are densely coiled in opposite directions. Three connector tubes 85,86,87 communicate with neck passages 88,89,90 at one end and are adapted to be connected with flexible conduit sections (not shown).
A separation vessel 91 having the same general shape as the jacket 81 is mounted for rotation therein about an axis 92. To this end, a short metal bushing 93 is inserted between a cylindrical upper end portion 94 of the separation vessel 91 and a cylindrical internal surface ofthe neck 82, and a cylindrical lower end portion 95 is rotatably received in a corresponding blind recess in the jacket 81.
The upper end portion of the separation vessel 91 has two inclined passages 96 and 97 extending from adjacent the axis 92 to diametrically opposite locations adjacent the periphery of the separation vessel. The upper end of the passage 96 is in constant open communica tion with the neck passage 88 through an annular space 98 defined between two coaxial tubes 99 and 100 secured to the separation vessel and projecting into the neck 82. The upper end of the other passage 97 is in constant open communication with the neck passage 90 through an axial passage 101 in the upper end portion 94. A passage 102 coaxial with the axis 92 has its upper end in constant open communication with the neck passage 89 through the inner tube 99. Sealing rings 103 and 104 prevent short circuit flow between the neck passages.
The separation vessel 91 defines two concentric an nular separation spaces 105 and 106 separated by an annular wall 107. At their upper ends, both separation spaces are in constant open communication with both passage 96 and passage 97, and at their lower ends they are both in constant open communication with the axial passage 102.
The separation vessel 91 is rotationally unbalanced with respect to the axis 92 such that it is held in a fixed angular position relative to the centrifuge rotor when the separation unit 81 is orbited in a centrifuge similar to that shown in FIG. 7, namely, such that the passage 96 is directed radially outwardly away from the rotor axis and the passage 97 is directed radially inwardly towards the rotor axis.
The separation unit 80 is used in a centrifuge similar to that shown in FIG. 7, and before the separation of the blood is commenced, sterile saline is fed to the orbiting separation unit through the connector tube 85. The saline first enters the separation spaces 105, 106 and then, under the influence of the centrifugal force, is forced along the bushing 93 into the annular space 108 between the separation vessel 91 and the jacket 81.
When the saline has expelled all air from the separation unit, blood is continuously fed into the separation spaces through the connector tube 85. The red blood cells are accumulated in the radially outermost portion of the separation spaces (to the left of the vertical interface 109) while plasma is accumulated in the radially innermost portion. Blood cells and plasma are continuously withdrawn through the connector tubes 86 and 87, respectively, at such a rate that the interface 109 is maintained between the locations where the separation spaces 105 and 106 communicate with the plasma withdrawing passage 97 and the red cell withdrawing passage 102.
Although the foregoing detailed description of embodiments refers only to plasmapheresis, it is to be understood that these embodiments, with no or only minor modifications, may also be used in connection with other liquid processing operations including centrifugal separation of liquid into fractions of different densities. One example is washing of freezing preserva tives from thawed red blood cells. In that case, in order that the mixing of the red blood cells with the wash liquid may be facilitated, the separation unit may include 'ture into fractions of different densities, comprising:
a. a jacket;
b. bearing means, adapted to be mounted on the centrifugc rotor remotely from said first axis, for supporting said jacket for relative rotation with respect to the rotor about a second axis;
0. flexible inlet and outlet conduits for liquid connected at one end to said jacket;
(I. an elongated flexible holder adapted at one end remote from the rotor to be held stationary by a fixed reference, and connected to said jacket for holding it against rotation about said second axis;
e. a separation vessel disposed in and rotatably supported by said jacket for relative rotation about said second axis and communicating with said conduit; and
f. orientation means acting on said vessel for maintaining it in a fixed angular position about said second axis during rotor rotation.
2. Apparatus according to claim 1 in which the jacket and the separation vessel define between them an annular space having approximately the same axial extent as the separation vessel and communicating with one of the conduits.
3. Apparatus according to claim 1 in which the orientation means comprises an unbalanced mass on the separation vessel causing rotational unbalance of the separation vessel with respect to the second axis.
4. Apparatus according to claim 1 in which theinlet and outlet conduits open into the separation vessel at locations spaced along the second axis.
5. Apparatus according to claim 1 in which said conduits have portions protruding axially in the same general direction from end of said jacket.
6. Apparatus according to claim 5 in which a rigid tube held concentric with the second axis by the jacket and extending axially into the separation vessel journals the separation vessel for rotation about the second axis and defines a section of a flow passage between one of the flexible conduit portions and a location in the separation vessel axially remote from said one end of the jacket.
7. Apparatus according to claim 5 in which the flexible conduits are helically wound about the flexible holder.
8. Apparatus according to claim 5 in which the flexible holder comprises a torsionally rigid rod secured to said one end of the jacket.
9. Apparatus according to claim 1 in which during centrifuging, the locations where said conduits open into the separation vessel are disposed such that they are at different radial distances from the first axis.
10. Apparatus according to claim 9 in which the inlet and outlet conduits include a third flexible conduit communicating with one end of said jacket, one of said locations where said conduits open into the separation vessel being adjacent the end of the jacket remote from said one end of the jacket and the other two locations being adjacent said one end of the jacket and on opposite sides of the second axis.
11. Apparatus according to claim 1 including connector means connected fluidly to the other end of said conduits and mechanically to said one stationary end of 5 said holder adjacent said first axis.
12. Apparatus according to claim 1 in which said conduits have portions protruding axially in opposite directions from said jacket.
rotation of the centrifuge rotor.
UNITED STATES PATENT OFFICE CERTIFICATE OF CORRECTION PATENT NO. I 3 885 735 DATED May 27, 1975 |N\/E T (5 3 J. EIICH. Westberg it is certified that error appears in the above-identified patent and that said Letters Patent are hereby corrected as shown below:
On the cover page, correct the patentee's name to --J. Eric H.
Westberg- Signed and Build this [SEAL] Attest:
RUTH C. MASON C. IAISIIALI. DAMN AIM-fling Officf Commission" a] km": and Trademark:
thir 'tieth Day of December 1975
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US489202 *||Jan 11, 1892||Jan 3, 1893||Centrifugal ore separator|
|US3235173 *||Jul 24, 1961||Feb 15, 1966||Olof Unger Hans Peter||Agitating and/or fractioning centrifuge|
|US3347454 *||May 13, 1964||Oct 17, 1967||Baxter Laboratories Inc||Method and apparatus for the centrifugal washing of particles in a closed system|
|US3674197 *||Sep 8, 1970||Jul 4, 1972||Sorvall Inc Ivan||Washing means for flexible bags in split enclosures|
|US3684161 *||Aug 17, 1970||Aug 15, 1972||Aga Ab||Centrifuge|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US4016077 *||Aug 25, 1975||Apr 5, 1977||Gus Schreiber||Blood transfusion filters|
|US4056224 *||Feb 11, 1976||Nov 1, 1977||Baxter Travenol Laboratories, Inc.||Flow system for centrifugal liquid processing apparatus|
|US4058252 *||Oct 23, 1975||Nov 15, 1977||Melvin Williams||Automatic sample processing apparatus|
|US4082217 *||Jan 24, 1975||Apr 4, 1978||Separex Sa||Centrifuge apparatus|
|US4109852 *||Oct 21, 1977||Aug 29, 1978||Baxter Travenol Laboratories, Inc.||Centrifugal strain relief sheath for processing apparatus|
|US4109854 *||Jun 13, 1977||Aug 29, 1978||Baxter Travenol Laboratories, Inc.||Centrifugal apparatus with outer enclosure|
|US4109855 *||Oct 25, 1977||Aug 29, 1978||Baxter Travenol Laboratories, Inc.||Drive system for centrifugal processing apparatus|
|US4113173 *||Feb 11, 1976||Sep 12, 1978||Baxter Travenol Laboratories, Inc.||Centrifugal liquid processing apparatus|
|US4200434 *||Feb 24, 1978||Apr 29, 1980||Sanki Engineering Ltd.||Immunological blood test method|
|US4372484 *||Jun 6, 1979||Feb 8, 1983||Gambro Ab||Device for the separation of a liquid, especially whole blood|
|US4389206 *||Mar 16, 1981||Jun 21, 1983||Baxter Travenol Laboratories, Inc.||Centrifugal processing apparatus and rotatable processing bowl apparatus|
|US4389207 *||Mar 16, 1981||Jun 21, 1983||Baxter Travenol Laboratories, Inc.||Rotatable bowl assembly for centrifugal processing apparatus having a bonded and prewound umbilical system|
|US4416778 *||Oct 20, 1981||Nov 22, 1983||Neocyte, Inc.||Means for preparing neocyte enriched blood|
|US4459169 *||Mar 23, 1983||Jul 10, 1984||Baxter Travenol Laboratories, Inc.||Rotatable bowl assembly for centrifugal processing apparatus having a bonded and prewound umbilical system|
|US5114396 *||Jun 18, 1991||May 19, 1992||Omega Medicinteknik Ab||Method of washing blood cells and container assembly thereof|
|US6656105||Nov 30, 2001||Dec 2, 2003||Gambro, Inc.||Centrifuge for processing blood and blood components in ring-type blood processing bags|
|US6689042||Jan 22, 2002||Feb 10, 2004||Gambro, Inc.||Centrifuge and container system for treatment of blood and blood components|
|US6740239||Nov 30, 2001||May 25, 2004||Gambro, Inc.||Method and apparatus for processing blood and blood components|
|US7097774||Jul 24, 2003||Aug 29, 2006||Gambro Inc||Method for processing a blood product with a bag set having a multi-way connector|
|US7235041||Aug 1, 2006||Jun 26, 2007||Gambro Bct, Inc.||Centrifuge for processing a blood product with a bag set having a processing bag|
|US7279107||Apr 16, 2003||Oct 9, 2007||Gambro, Inc.||Blood component processing system, apparatus, and method|
|US7497944||Mar 27, 2007||Mar 3, 2009||Caridianbct, Inc.||Blood component processing system, apparatus, and method|
|US7708889||Jan 26, 2009||May 4, 2010||Caridianbct, Inc.||Blood component processing system method|
|US8257239||Sep 4, 2012||Fenwal, Inc.||Umbilicus for use in an umbilicus-driven fluid processing|
|US8460165 *||Jun 11, 2013||Fenwal, Inc.||Umbilicus for use in an umbilicus-driven fluid processing system|
|US8657730 *||Apr 25, 2013||Feb 25, 2014||Fenwal, Inc.||Umbilicus for use in an umbilicus-driven fluid processing system|
|US8727958 *||Nov 13, 2008||May 20, 2014||Miltenyi Biotech Gmbh||Apparatus and method for transferring energy and/or a substance to rotating means|
|US9079194||Jul 18, 2011||Jul 14, 2015||Terumo Bct, Inc.||Centrifuge for processing blood and blood components|
|US9383044||Feb 15, 2013||Jul 5, 2016||Fenwal, Inc.||Low cost umbilicus without overmolding|
|US20030173274 *||Feb 3, 2003||Sep 18, 2003||Frank Corbin||Blood component separation device, system, and method including filtration|
|US20060270542 *||Aug 1, 2006||Nov 30, 2006||Gambro, Inc.||Centrifuge for Processing Blood and Blood Components|
|US20090127206 *||Jan 26, 2009||May 21, 2009||Caridianbct, Inc.||Blood Component Processing System Method|
|US20100261596 *||Nov 13, 2008||Oct 14, 2010||Miltenyi Biotec Gmbh||Apparatus and method for transferring energy and/or a substance to rotating means|
|EP2397229A2 *||Jun 15, 2011||Dec 21, 2011||Fenwal, Inc.||Umbilicus for use in an umbilicus-driven fluid processing system|
|WO1983001394A1 *||Oct 20, 1982||Apr 28, 1983||Neotech L P||Method and means for preparing neocyte enriched blood|
|U.S. Classification||494/27, 494/60, 494/44, 210/789, 494/42|
|International Classification||B04B5/00, B04B5/04, B04B5/02|
|Cooperative Classification||B04B5/0442, B04B2005/0492, B04B5/02, B04B5/0407|
|European Classification||B04B5/02, B04B5/04B, B04B5/04C|