Method and device for preventing imbalance during the separation and isolation of blood or bone marrow components

Abstract: Centrifugal apparatus for separating components of a biological mixture such as blood, comprising a plurality of co-rotating containers (1) spaced from and distributed evenly about the centrifugal axis, a first co-rotating liquid system for containing the biological mixture, said first liquid system comprising a primary source reservoir (2) in each container (1), at least one primary receiving reservoir (3) connected to said source reservoir (2) through a respective primary conduit (4), and primary pumping means for letting at least a portion of said biological mixture flow from the primary source (2) reservoir to said primary receiving reservoir (3) during centrifuging, the apparatus further comprising a co-rotating secondary liquid system (8) for compensating the decrease in weight of each of the containers resulting from the outflow of the portion of the biological mixture from the primary source reservoir in order to keep the apparatus in balance during pumping. The density of the secondary liquid is larger than that of the heaviest component of the mixture which is to be separated.

Description: The invention is related to an apparatus and a method for separating components of a biological mixture, such as blood, by centrifuging, wherein means are provided and measures are taken, respectively, to prevent imbalance. A centrifugal apparatus as described in the preamble of claim 1 is known from US-A-4.303.193. A method as described in the preamble of claim 9 is also known from US-A-4.303.193. The invention further concerns a method and device for the separation of blood or cells of blood-forming organs, such as bone marrow, into their components and for the isolation of those components by means of centrifuging in which a source reservoir, which is connected with one or more recipient reservoirs via an outflow opening, is applied as a container for the blood or the bone marrow. Blood consists of four components which, in order of increasing specific gravity, are: blood plasma, blood platelets, white blood cells and red blood cells. For the red blood cells further distinction is made between the old cells - the gerocytes and the newly-formed cells - the neocytes. The average lifetime of a red blood cell is approximately 90 days. "New" cells will therefore still be able to live for a relatively long time, which can be of great importance in the case of blood transfusion. The specific gravity of the red blood cells increases as they get older, so that with the aid of centrifuging it is possible to achieve a certain distribution of the red blood cells according to age. White blood cells and blood placelets - together called 'buffycoat' - constitute in total approximately 1% of the volume of normal blood. Approximately 45% of the total volume is taken up by red blood cells and after centrifuging approximately 50% of the neocytes are situated in a layer thereof, which layer comprises approximately 10% of the total outgoing volume. In the prior art, both the components which constitute the buffy-coat and the neocytes are separated from one another according to a known procedure, and thereafter isolated from one another. For this purpose see, for example, European Patent No. 0026417. A difficulty in this connection is the isolation of the relatively small fractions - the white cells, the platelets and the neocytes - without much loss occurring through, for example, contamination in the adjoining surfaces. In European Patent No. 0026417 a method is described for the separation and isolation of blood components. After separation by centrifuging the layers are successively pumped out of the source reservoir and then collected. The pumping out is done by exerting a sideways pressure on the flexible source reservoir with the aid of a pressure cushion. Liquid is then pressed out of the reservoir. A description is given of how in that way blood plasma is transferred to an adjacent recipient reservoir. A device for separating and isolating blood components described in the above-discussed European Patent No. 0026417 consists of a centrifuge with one or more containers mounted at a certain radial distance from the centrifugal axle which rotate together with the centrifuge during use. Each contains a source reservoir with an outflow opening which is in the main directed at the centrifugal axle, with which the reservoir is joined via an outflow pipe with one (or more) recipient reservoir(s) as a closed system. This centrifuge is equipped with a pump mechanism with which, after they have been separated, the components are pumped out of the source reservoir to the recipient reservoir(s). In "Nature", vol. 217, page 816 et seq., a method is described with which the said disadvantage is removed, with the aid of a "continuous-flow" process. Thereby the components are both separated and isolated during centrifuging. Contamination after centrifuging does therefore not occur there. This described process, however, also has disadvantages: the necessary supply and drain pipes with their accompanying channels and rotating seals lead to a costly and complex construction. Another disadvantage is that in one centrifugal process there can only be worked with one reservoir, which leads to a low processing capacity. Summary of the Invention According to the invention a method and an apparatus as claimed in the accompanying claims is provided, in which a source reservoir is centrifuged and fractional components thereof are pumped out into a co-rotating receiving reservoir during centrifuging and in which imbalance is prevented by means of a co-rotating compensating system. This method according to the invention makes the pumping out of components during centrifuging possible in a simple way without the said disadvantages occurring, and has for that purpose the characteristic that after a certain centrifuging time, pumping takes place during centrifuging with the aid of a pump mechanism which rotates with the centrifuge, and that the entire liquid system: the recipient reservoir(s), the source reservoir and the joining pipe(s) rotate together, whilst the centrifuge is kept in balance by the compensating system that forms part of the rotor. Because of the fact that the compensating system rotates together with the centrifuge, the costly pipes and rotating seals have become unnecessary. Imbalance of the centrifuge can, for example, be avoided by either situating the recipient reservior(s) at approximately the same place with relation to the centrifuge axis as the source reservoir, or by ensuring in another way, for example via a separate - also co-rotating - liquid system, such that in the place of the source reservoir the weight of liquid which flows out of it is compensated. When a high rotational speed of the centrifuge is necessary for obtaining and maintaining a well defined separation surface between the layers during pumping, the difficulty arises with this method that a vacuum can be formed in the joining pipe between the source and the recipient reservoir, due to which further pumping out of the components may be impeded. This difficulty can, according to a further characteristic of the method according to the invention, be overcome by ensuring that during centrifuging the liquid in the system is subjected to an extra pressure. Such a pressure is obtained according to one way of implementing the method by introducing extra liquid into a system of flexible reservoirs which can only expand to a limited degree. The limitation of the expansion can be effected for example if both reservoirs are situated in a closed container. When extra liquid is then brought into the system the reservoirs will expand with their flexible walls and fill the container completely, after which the desired extra pressure in the system occurs with only a small excess of liquid. Plastic disposable reservoirs, for example, could be used as reservoirs. The extra fluid can, for example, be introduced into the system from an extra reservoir which is in fluid pressure communication via a delivery pipe with the recipient reservoir, and which, in relation to the expansion possibilities of the system, is filled with sufficient liquid, and from whereout, if a vacuum occurs in the system, liquid can be drawn into the system. Such an extra pressure can also be created by externally increasing the pressure on the system, or on part of it. Of course, in order to obtain the desired effect, it is necessary that at least a part of the system, for example a reservoir, has a flexible wall, from where the extra pressure to the system can be given. The said methods are especially applied when separating blood into its components and when separating bone marrow cells. The said components of blood are: blood plasma, red blood cells, blood platelets and white blood cells, with specific gravities of 1,03; 1,10; 1,05 and 1,07 g/ml. The white blood cells can be divided again into mononuclears and granulocytes. The demand for the different components with a high purity is high. In order to avoid undesired immunological reactions with patients as a result of transfusion and transplantations, one desires namely to administer a patient with only those components which are necessary. As only approximately one percent volume of blood exists of blood platelets and white blood cells together, and the blood platelets, the mononuclear white cells and the granulocytes must each be isolated out of this mixture, a method according to which contamination of a component with cells of another component is avoided to a great degree is difficult to achieve, whilst the need therefore is nevertheless great. Besides the greater purity of the isolated components the advantages of the methods according to the invention are that the yield, or quantity of the component which can be extracted out of a certain quantity of the source mixture is considerably higher than according to the known methods, and that more units can be processed at the same time in a centrifuge with more source reservoirs, as a result of which more blood can be separated per unit of time. When separating and isolating blood components it appears to be important, in order not to disturb the dividing surfaces during pumping between the layer containing the blood platelets and the white blood cells on the one hand, and the layers containing the blood plasma and the red blood cells on the other hand, to centrifuge at a high rotational speed; for example with a centrifuge with an arm length of 26 cm, at more than 500 revolutions per minute (rpm). At approximately 800 rpm the problem of the vacuum in the joining pipe began to occur and it was necessary to increase the pressure in the system. At 2000 rpm the necessary extra pressure appeared to be 6 atm., which was achieved by introducing more liquid - a physiological salt solution - into the system. The apparatus according to the invention consists of a centrifuge with one or more containers at a certain radial distance to the centrifuge axis which rotate in use together with the centrifuge, and which each either serve as a source reservoir, or contain a source reservoir, whereby the source reservoir has an outflow opening which at least in the main is directed radially and which is joined as a closed fluid system with a recipient reservoir by a tube which is in the main radially directed, and with a co-rotating pumping mechanism for pumping liquid out of the source reservoir to the recipient reservoir(s). The containers are each situated for example at the end of an arm which extends radially from the rotation axis. From the source reservoir runs a tube, in which a flow of the liquid to the recipient reservoir(s) is brought about by the co-rotating pump mechanism. In order to ensure that the centrifuge remains in balance during pumping one must ensure that the mass at the end of the arm of the centrifuge always remains the same. For this purpose liquid is continually introduced into a container during pumping. A suitable solution is obtained with a device of which the pump mechanism consists of a second co-rotating liquid system (II) with a flexible recipient reservoir which fills a container together with the, also flexible, source reservoir of the first liquid system (I), and which contains a liquid in its source reservoir which is situated outside the container with a density which is just a little larger than that of the liquid which must be centrifuged. When this heavier liquid is pressed into the container by the centrifugal force in the recipient reservoir (II), because of the fact that the reservoirs are closed in, an equal amount of fluid is pressed out of the source reservoir (I) of the first system. The total mass at the end of an arm thus remains approximately constant. The two systems indicated here with I and II are joined together in such a way that source reservoir (I) and recipient reservoir (II) and situated in one container and source reservoir (II) and recipient reservoir (I) are situated in another container. A co-rotating pump can in principle be situated anywhere in the centrifuge, for example also in the container of the reservoirs. Thus a conical shaped "cap", which is movable in a radial direction and which rests on the the source reservoir, can serve as a "pump", if the specific gravity of that cap lies between that of the two components which are to be separated. The recipient reservoir then lies against the radially inward side of the cap. As a component flows out the source reservoir into the recipient reservoir, the cap is pushed outwards in a radial direction and it will function as a pump. A simple solution for the balancing problem is achieved if, in the device according to the invention, a container contains both the source reservoir and the corresponding recipient reservoir(s). The total quantity of liquid in the container does not then change. For centrifuging at a high rotational speed, in order to avoid the forming of a vacuum in the system, a device according to the invention is equipped with a source reservoir and recipient reservoir(s), both with flexible walls, which are situated in a container which contains them completely and which they approximately fill when in use, whereby an extra reservoir, which is filled with a liquid when in use, is coupled in fluid pressure communication with the system with an open join in the section between the container and the centrifuge axle. The make-up fluid in the reservoir which is preferably a saline solution having a density greater than the various components of the fluid mixture, may be adapted to flow into the source reservoir for displacing the lighter separated components therefrom, or may be adapted to flow into a separate pressure vessel or balloon which contacts the source reservoir and applies pressure thereto to express the separated components thereof. Various designs can be chosen as pump mechanisms. According to one preferred design the device contains a usual type of peristaltic pump, which rotates together with the centrifuge, and whose drive shaft is situated in the extension of the rotating shaft of the centrifuge, mechanically coupled to it, e.g., by a clutch, which coupling can be disconnected during centrifuging. The coupling with the centrifuge shaft is for example via the pump housing. The clutch can be disconnected by disengaging the drive shaft during centrifuging with the aid of a pressure plate which is fixed at a stationary point, for example the lid of the centrifuge. The pump housing will then rotate around its now stationary drive shaft and the pump will therefore pump. Other designs of the pump mechanism are also possible. For example the pump mechanism can be a barrel (II) on or near the centrifuge shaft which rotates together with the centrifuge, and which is filled with a liquid with a larger density than that of the heaviest component of the mixture which is to be separated. This barrel is joined via a pipe with a flexible recipient reservoir (II), discussed above, which is situated together with the flexible source reservoir (I) of the mixture in a closed container at the end of the centrifuge arm. During centrifuging this liquid will then flow to the recipient reservoir (I) in this container. As this reservoir is filled, the source reservoir (I) is compressed and liquid will be pushed out of it to a recipient reservoir (I) on or near the centrifuge shaft. In order to avoid the centrifuge getting out of balance a liquid must be chosen as pumping liquid with a density which is just a little larger than that of the heaviest component of the mixture. Different mechanical elements and configurations are employed in several aspects of the invention to control the rate of pumping during centrifuging, so as to isolate precise components of the fluid being treated. The method according to the invention aims firstly at being able to "treat" as much blood as possible in one centrifugal processing run, with as large a quantity as possible per quantity of blood of each component of a certain high purity, and secondly at keeping the duration of one centrifugal processing run as short as possible. In order to achieve the first thing it is important, among other things, that an optimum use is made of the space which a centrifuge offers for the placement of source reservoirs. The invention is based on the insight, that is is possible to achieve a pump mechanism which does not take up any space in the sense mentioned. The method can for that purpose have the characteristic that the pumping-out is effected by reducing the volume of the source reservoir by pressing in the radially outer wall of this reservoir. This can be achieved in two ways. The first means of achieving this is that the pressing-in is effected by allowing the source reservoir to move radially outward under influence of the centrifugal force, with its outer wall against an elevation in the floor of the container, and the second means of achieving it is that the pressing-in is effected by moving an elevation in the floor of the container radially inward, and pressing-into the outside wall of the source reservoir. In order to further achieve a shortest possible duration of one centrifugal processing run it is important that pumping out is always done at as high a speed as possible. As the buffy-coat layer is a relatively thin layer, there is an upper limit to the speed at which it can be pumped out. Once the upper limit is exceeded the buffy coat layer will, on reaching the outflow opening, be "broken" and red blood cells will also be pumped out together with the buffy coat. In order to achieve an optimum pumping-out process as far as duration is concerned the method according to the invention can have a further characteristic that the speed with which the reservoir is pressed-in is relatively high when pumping out a relatively voluminous component, and relatively low when pumping out a component which is of relatively little voluminousness. For the execution of this method such a device can have the characteristic that the side walls of the source reservoir converge in an approximately funnel-like shape to the outflow opening and that a mechanism is present to reduce the volume of the reservoir from the radially outer side of the reservoir with an adjustable speed. The funnel shape at the radially inner end serves to be able to efficiently isolate the components. If only a small amount of a layer has remained behind in the reservoir, the funnel shape ensures that as the layer approaches the outlet it becomes so thick, that it can be pumped out without being mixed with a following layer. This is especially true for the buffy-coat layer, which has but a very small thickness in total. The mechanism to adjust the speed with which the reservoir is compressed serves to obtain an optimum speed, that is to say to adjust the rate of outflow from the reservoir for each layer according to the layer thickness. The funnel shape can be effected by constructing the radially inner end of the otherwise flexible reservoir of a stiff material. In a preferred design of the device according to the invention there is a funnel shaped stiff cap fitted over the inner end of the reservoir. The cap has an opening, and its jacket is open from its outer to its inner end over a width which is at least equal to the diameter of the inflow pipe. The opening in the jacket serves to enable the cap to be placed on the reservoir together with its permanently joined outflow pipe. Such a cap is preferably conical. A design of an apparatus suitable for the method in which the source reservoir moves radially outwards, has the characteristic that the outside wall of the container has an elevation on its inside side which when at rest lies against the radially outside wall of the source reservoir, which is situated in a mainly cartridge-shaped housing containing the side walls of the reservoir, which is movable by sliding in a radial direction along the inside of the side walls of the container. The cartridge around the reservoir serves to make it possible that the reservoir can move in the container. Housing and cap are preferably joined to one another, for example by means of a screw closure. In order to make better use of the space which a centrifuge has to offer to reservoirs for the blood which is to be separated, the walls of the housing converge, according to the a further preferred design of the device, radially from the outside to the inside, while the side walls of the container also converge towards the inside approximately parallel to those of the housing, and a wall or part of a wall of the container is removable over a width corresponding to the width or the diameter of the source reservoir. Such containers can be arranged as sectors of a flat disk, with the centrifuge shaft at its center. In order to create room for the recipient reservoirs, the containers of the source reservoirs are preferably executed in a conical shape. The recipient reservoir(s) can then be placed per source reservoir on the outer wall of the cone. In a construction with a converging housing in a converging container the housing must be guided when it moves in a radial direction. In a design of a device this happens by supporting devices, which consist of a radially directed rod which is fixed at one end to the inward portion of the container, and at the other end is joined in a sliding manner to the inside end of the housing and to guiding surfaces on the back inside face of the outer circumference of the container which extend approximately radially inwards, with a distance between them corresponding to the distance between the housing walls at the outer side of the housing and running inward to at least above the elevation. In order to regulate the rate at which fluid is pumped, and thus the rate at which the outside wall of the source reservoir is compressed, a design of the mechanism which serves for that purpose is characterized by the fact that the outside face of the reservoir extends over the adjoining surface of the elevation in a ring shaped part, and that under this part and around the elevation two or more inflatable rings are situated, lying over each other as viewed in a radial direction, and equipped with valves with independently regulatable flow openings. This design makes two pump speeds possible. When the first layer - the plasma - is pumped out the speed can be high. The valve in the first air-filled ring can be adjusted in such a way that the outflow is high, whilst the other valve is closed. When the buffy-coat has advanced to the outflow opening the speed must be reduced. At that moment, the valve which until then was open must be closed and the other, narrower, valve is opened. The result is a lower pumping rate. Opening and closing of the valves can for example be controlled electronically with the aid of sensors. If, instead of using the centrifugal force which moves the source reservoir radially outward, use is made of a body which presses into the outer face of the reservoir from outside, the outside wall for example is equipped with an opening, through which an elevation, of which the inner face coincides with the outer side of the container when at rest, can be moved inwards in a radial direction. Brief Description of Drawings Fig. 1 is a view from above of a horizontal cross section through a device illustrative of one aspect of the invention; Fig. 2 is a side view of the device of fig. 1; Fig. 3 shows in detail the situation in the container after centrifuging for some time, and before pumping begins; Fig. 4 shows the situation during pumping; Fig. 5, viewed from above and perpendicular to the centrifugal axis, is a cross section through a centrifuge, in which two different design examples of centrifugal units are schematically drawn; Fig. 6 shows in more detail the same cross section of one of the centrifugal units shown in fig. 5; Fig. 7 shows a similar detailed cross section through the other centrifugal unit drawn in fig. 5, in which however the pump mechanism is another than that shown in fig. 5; and Fig. 8 shows a cross section through a conical centrifugal unit according to fig. 7, through the middle of the unit, but now parallel to the centrifugal axis. Detailed Description In fig. 1 the container 1 contains a source reservoir 2 and a recipient reservoir 3, both made of flexible material, for example as plastic disposables, joined to each other by a pipe 4. The pipe 4 runs via a pump 6 which is mounted above the centrifuge shaft 5. In fig. 1 a centrifuge with four "arms" is shown. The drawn pipes 4', 4'' and 4''' correspond to arms other than the drawn arm. The pipe 4 is equipped with a valve or closure 7, with which the pipe can be closed off when a certain component has passed out of the mixture. The closure 7 reacts on a signal from an "eye" which may, for example, be a light source and photodetector arranged about the pipe and which detects the passage of a dividing layer between the components. An extra reservoir 8 is coupled with the pipe 4, filled with a physiological salt solution. When a vacuum begins to form in the system at a certain rotational speed, this solution will be sucked into the system. When the source reservoir 2 and recipient reservoir 3, partially as a result of the extra liquid which is brought to the system out of reservoir 8, "fill" the container, a pressure will be built up in the system such that the undesired vacuum will be compensated for. Figure 2 shows the same device in a side view. With 9 is given the arm of the centrifuge on the end of which the container, hinging around an axle 10, is mounted. With 11 is meant the drive shaft of the pump, which is mechanically coupled with the pump housing 6 and thereby with the centrifuge shaft 5. This drive shaft 11 can be be disengaged during centrifuging with the aid of a pressure piece 12. Figure 3 shows the situation in the container 1 after blood has been centrifuged for some time. The blood is separated into red blood cells 13, blood plasma 15 and therebetween, in a layer 14, the so called "buffy coat", consisting of blood platelets and white blood cells. Figure 4 shows the situation after pumping has taken place for some time after centrifuging. The plasma 15 leaves the source reservoir 1 as the first component and comes into the recipient reservoir 3. Next comes the buffy-coat. By stopping the pumping when the buffy coat is situated in the narrow pipe 4, and thus forms a relatively thick layer, it becomes possible to effect a separation between blood platelets 14'' and the rest of the white blood cells 14'. In Fig. 5, 16 is the centrifuge shaft, to which centrifuge units 17 and 18 are attached. One centrifuge contains in general one type of centrifuge unit, therefore, for example, either all units of type 1 or of type 2. For purposes of this discussion, "type 1" refers to the design of unit 18, and "type 2" refers to the design of unit 17. The centrifuge units 17 and 18 each consist of containers 19 respectively 20, with radially outer walls 21, respectively 22. In the containers 19 respectively 20 are flexible, for example plastic, source reservoirs 23 respectively 24 for the blood which is to be centrifuged. The walls of the containers 23 and 24 converge at the radial inner end in a funnel shape to the outflow openings 25 respectively 26. The outflow openings 25 respectively 26 open out into recipient reservoirs 27 respectively 28, of which a part is drawn. In order to guarantee the sterility of the contents, the source reservoir and the recipient reservoir in each unit are connected to each other via an outflow tube. With 29 and 30 the elevations are given, which move inwards, that is to say in the direction of the centrifugal axis, in relation to the respective outside walls 31 and 32 during the pumping out. The elevation 29 illustrated in the type I is permanently connected with the outside wall 21 of the container. During the pumping out, the reservoir 23, which is situated in a housing which moves together with reservoir (not drawn), moves outwardly and will extend over each side of the elevation 29. In the type 2 the elevation 30 is situated outside the outer wall 22 of the container 20. This outer wall 22 is equipped with a hole, through which the elevation 30 can be moved in the direction of the centrifugal axis 16, thereby pushing in the outer end of the reservoir 24. The means by which the elevation 30 can be moved inward are not drawn. This can be done, for example, hydraulically. The different ways of pumping out: either by pressing the elevation into the outer end of the reservoir, or by pressing the reservoir against the elevation can both be applied to either of the container types. With the use of centrifugal unit of type 1 the space available in the centrifuge can be used better than with use of units of the type 2. With type 1, 12 standard units for example can be placed in one circular disk. In Fig. 6 a same cross section as in Fig. 5 is shown in detail of a design of a centrifugal unit of type 2. The source reservoir 23 shows a wall section 33 converging at the inner end in a funnel shape. This wall section is held in shape by the cap 34 which lies over it. This cap 34 is equipped at its inner end with a hole 35 which when in use lies over the outflow opening 25, so that the outflow pipe 36 can pass through it. In order to be able to place the cap 34 onto a source reservoir 23 the jacket thereof must contain an opening (not drawn) extending from the hole 35 outwardly. The source reservoir 23 is supported on its side walls 37 over preferably the whole height thereof by a housing 38, which can slide from the inside outwardly along the inner wall 39 of the container 19. In the drawn example, cap 34 and housing 38 are connected to each other by a screw closure 40. The recipient reservoir consists of a tube 41, which is connected at one end to the outflow opening 25 of the reservoir 23, is wound around a spool or reel 42 which is mounted on the cap 34, and at its other end to one or more collecting chambers (not drawn) for the components. At the recipient reservoir are included a sensor 43, which detects when a following component "passes", and a valve or closure, 44. In order to be able to divide the blood in the source reservoir 23 into its components, it is first centrifuged, without the liquid being pumped out of the reservoir, while the closure 44 is closed. When the separation is completed, the closure 44 is opened. Due to the centrifugal force the reservoir 23 will then move outwardly, sliding with its housing 38 along the inside wall 39 of the container 19. The flexible outer wall of the reservoir is then dented in by the elevation 29 and at places 45 and 46 extends over the sides of that elevation in a ring shape and the fluid is pressed out of the reservoir 23. After the first component - the blood plasma - is thus pumped out, it is the turn for the buffy cont. As this has been pressed inwardly during the pumping out of the plasma, this will eventually be situated in the inmost tip of the funnel. Due to the funnel shape a reduction of the surface, and therefore an increase of the thickness of that layer has come about. Nevertheless, in order to avoid that fluid of the following component also comes out when pumping, the pumping rate must be relatively low; lower than is required when pumping out the plasma. In order to be able to regulate that rate, two inflatable rings 47 and 48 with valves 49 and 50 are situated behind each other around the elevation 29. The rings 47 and 48 and the width of the valves 49 and 50 can be given such dimensions, that as long as plasma is being pumped out, ring 47 deflates at a relatively high speed, and that when it is the turn for the buffy-coat ring 48 deflates with a lower speed. Fig. 7 shows the cross section of centrifugal unit 17 according to figure 5 in more detail, with the difference that the relative movement of the outside wall 32 in relation to the elevation 29 is now achieved by pressing the source reservoir 24 outwards against the elevation 29 instead of the other way around. An advantage of the reservoir shape according to fig. 7 is the already mentioned better degree of filling of the centrifuge. In order to still be able to pump out with the aid of the centrifugal force alone - therefore by being able to allow the source reservoir to move outwards - some special facilities are necessary. In the container with converging walls 20 in order to make maximum use of the space available, there is also a reservoir 24 with converging walls 52 which are laterally supported by a converging housing 53. This housing lies, in the starting position, with its walls against the walls of the container 20. When this housing 53 begins to move under influence of the centrifugal force it must be guided. For that purpose the guides 54 are mounted in the container 20, preferably also in the shape of a cartridge shaped body, along which the wall of the housing 53 slides. The housing is further guided in radial direction by a rod 55 fixed at the front at 56 to the container 20 and at the other end fixed in a sliding manner to the inward wall 57 of the housing 53, through which it protrudes. With 58 the inflatable rings are schematically given, corresponding with the rings 47 and 48 drawn in fig. 6. Elements 43 and 44 are the already mentioned sensor and the closure valve, respectively, in the recipient reservoir, of which the tube 41 is drawn, wound on a reel which is not drawn. In fig. 7 a situation is drawn in which the housing is situated in the most outward position. Fig. 8 is a vertical cross section, parallel to the centrifugal axis through a centrifugal unit as drawn in fig. 7, but then conically shaped. An advantage of the conical shape is that the collecting chambers of the recipient reservoir, seen in the direction of the centrifugal axis 5, can lie over the container, whereby a maximum amount of space is available for the reservoirs with the blood which is to be centrifuged. The collecting chambers 59 for the plasma and a second collecting chamber 60 for the blood platelets are drawn.

Claims: Centrifugal apparatus for separating components of a biological mixture such as blood, comprising at least one co-rotating container spaced from the centrifugal axis, a first co-rotating liquid system for containing the biological mixture, said first liquid system comprising a primary source reservoir in said container, at least one primary receiving reservoir connected to said source reservoir through a respective primary conduit, and primary pumping means for letting at least a portion of said biological mixture flow from the primary source reservoir to said primary receiving reservoir during centrifuging, the apparatus further comprising a compensating system for compensating the decrease in weight of the container resulting from the outflow of the portion of the biological mixture from the primary source reservoir in order to keep the apparatus in balance during centrifuging, in particular pumping, wherein said compensating system comprises means for introducing mass-compensating liquid into said container during centrifuging, in particular pumping, characterized in that the centrifugal apparatus comprises a plurality of co-rotating containers which are spaced and distributed evenly about the centrifugal axis, and in that said compensating system is in its entirety arranged for co-rotation with the rotating parts of the centrifugal apparatus. Apparatus as claimed in claim 1, wherein said compensating system includes a co-rotating secondary liquid system for compensating fluid comprising at least one secondary system for compensating fluid comprising at least one secondary source reservoir and a plurality of secondary receiving reservoirs connected to said secondary source reservoir through respective secondary conduits, each said secondary receiving reservoir being located in one of said containers, and secondary pumping means for urging a portion of said compensating fluid into said secondary receving reservoir during pumping of said primary pumping means. Apparatus as claimed in claim 2, wherein said secondary receiving reservoir and said primary source reservoir are flexible and together fill up their respective container. Apparatus as claimed in claim 2 or 3, wherein said at least one secondary source reservoir is located on or near the centrifugal axis. Apparatus as claimed in claim 2, 3 or 4, wherein said at least one primary receiving reservoir is located on or near the centrifugal axis. Apparatus according to claim 5, wherein said at least one primary receiving reservoir and said at least one secondary source reservoir are situated in at least one further container. Apparatus according to claim 1 wherein each said primary source reservoir is connected to a separate primary receiving reservoir, said primary source reservoir and said primary receiving reservoir both being contained in a respective container. Apparatus according to any one of the preceding claims, wherein the containers are arranged on the ends of respective centrifuge arms. Method for separating components of a biological mixture such as blood, comprising the steps of: placing said mixture in at least one primary source reservoir of a centrifugal apparatus located in a corresponding container spaced from the centrifugal axis, said primary source reservoir being connected through a primary conduit to at least one primary receiving reservoir; centrifuging the mixture in order to create separation between components having different densities; pumping, while centrifuging, at least one separated component from said primary source reservoir to said primary receiving reservoir; and pumping, while centrifuging, liquid from a source into said container, said liquid having a density at least equal to the density of the component pumped out of said primary source reservoir, characterized in that said liquid is pumped from a co-rotating source. Method as claimed in claim 9, wherein said liquid has a density larger than that of the heaviest component of the mixture which is to be separated. Method as claimed in claim 10, wherein the liquid has a density which is a little larger than that of the heaviest component of the mixture. Method as claimed in claim 9, 10 or 11 wherein said liquid is a secondary liquid contained in a secondary liquid system and having a density which is slightly greater than the density of the biological mixture, said secondary liquid being stored in at least one secondary source reservoir and being pumped during centrifuging towards a secondary receiving reservoir in said container. Method as claimed in claim 12, wherein said secondary receiving reservoir is enlarged by filling with said secondary fluid to effect a pumping effect on said primary source reservoir by reducing its size within said container. Method as claimed in claim 9, wherein said liquid is the component pumped out and said primary receiving reservoir is located in said container.

Inventors: BONT WILLY S, FIGDOR CARL G, BONT, WILLY S., FIGDOR, CARL G.
Applicants: VER NL KANKER INST, VERENIGING HET NEDERLANDS KANKER INSTITUUT
Application year: 1986
Main classification: B04B9
IPC codes: B04B5, B04B9