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US3519201A - Seal means for blood separator and the like - Google Patents

Seal means for blood separator and the like
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US3519201A
US3519201AUS727192AUS3519201DAUS3519201AUS 3519201 AUS3519201 AUS 3519201AUS 727192 AUS727192 AUS 727192AUS 3519201D AUS3519201D AUS 3519201DAUS 3519201 AUS3519201 AUS 3519201A
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channel
blood
seal
rotating element
channel means
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US727192A
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Robert J Eisel
William B Greenough
Robert M Kellogg
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US Department of Health and Human Services
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July 7, 197() R 1 EISEL ET AL SQ SEAL MEANS FOR BLOOD SEPARATOR AND THE LIKE Filed May '7, 1968 2 Sheets-Sheet l IOO /f// @o l MMM/m4 m8x /OZ 4,0 /gl v50 E G4 e Tl aff/45445470131,:152m 4e e@ l0 14 04989/14123/ es 16 e 0 z "LG @all l w La A w--fx july 7, fg@ R- J ElsEL ET AL 3,59,
SEAL MEANS FOR BLOOD SEPARATOR AND THE LIKE Filed May '7, 1968 2 Sheets-Sheet 2 United States Patent O 3,519,201 SEAL MEANS FOR BLOOD SEPARATOR AND THE LIKE Robert J. Eisel, Kensington, and William B. Greenough III, Baltimore, Md., and Robert M. Kellogg, Endwell, N.Y., assignors to the United States of America as represented by the Secretary, Department of Health, Education, and Welfare Filed May 7, 1968, Ser. No. 727,192 Int. Cl. B04b 11/00;A61m 5/00 U.S. Cl. 233-21 10 Claims ABSTRACT F THE DISCLOSURE Sealing means for use with a face seal having one fixed element and one rotating element particularly for use with a continuous blood flow separator. Saline under pressure is forced into groove means between the channel means at the interface of the seal means to preclude seepage of the materials in the channel means across the interface. According to a preferred arrangement the most sensitive material, such as packed red blood cells, is removed through the most direct pathway to preclude damage thereto. Preferably, the rotating element is formed of ceramic and the fixed element is formed of stainless steel.
This invention relates to a sealing means for use with a face seal having one fixed element and one rotating element. More specifically, this invention is directed to a modi-tied and improved sealing means for use with a continuous flow blood separator of the type described in detail in copending application Ser. No. 570,792 filed Aug. 8, 1966, in the names of George T. Judson and Emil J. Freireich, and assigned to the same assignee as the instant application. The disclosure of the aforementioned copending application is incorporated herein by reference in its entirety.
The provision of a sealing means between fixed and rotating elements provides obvious difficulties. Such a sealing means has general applicability, for example, in centrifuge devices or separating means wherein a fluid is separated into a plurality of components by centrifugal force. With such devices the fluid must be fed into the bowl of the centrifuge and the separated components of the fluid must be removed therefrom after centrifugation. Since portions of the centrifuge are rotating at high speeds, and since the source of the fluid and the depository for the components are usually stationary, a sealing means must be interposed which is effective to prevent leakage between a stationary or xed element into which the fluid is fed and from which the components are withdrawn, and a rotating element which receives the iiuid from the xed element and feeds the same to the bowl of the separator and which receives the fractional components from the separator and feeds the same to the fixed element for withdrawal from the device. The difficulties of such an operation are believed obvious.
Such difficulties are'compounded when the fluid being separated is blood or any other material particularly sensitive to damage. Further, when the fluid is blood withdrawn directly from a donor, with certain of the fractional components being returned directly to the donor in a continuous separation system, any damage to the components has even greater significance since there is relatively little opportunity to monitor the same before they are returned to the donor. The aforementioned copending application discloses such a continuous flow blood separator and provides a face seal adapted to prevent leakage between the fixed and rotating elements of the centrifuge thereof. This face seal, while "ice generally satisfactory, has been subject to certain problerns. Particularly, it has been found that in some instances the blood or fractional components thereof have a tendency to seep across the lands separating the channels defined at the interface between the fixed and rotating elements. In addition to such seepage causing a mixture of the various materials which in itself is undesirable, the high shear to which such materials are subjected during seepage across the interface has been found to damage the materials. It is this problem with which the instant invention is primarily concerned.
Other difficulties have also been encountered with the face seal disclosed in the aforementioned copending application. One of the fractional components being separated from the blood is packed red blood cells, a material which is particularly sensitive. In the face seal of the copending application, the blood itself is fed through a central axial passageway which extends through both the fixed and rotating elements, and the fractional components are withdrawn through aligned concentric channels in the fixed and rotating elements. Removal of the packed red blood cells through one of the annular channels necessitates the passage of this material through a somewhat tortuous route. It is preferred that this particularly sensitive component of the blood be handled in the most delicate manner and the instant inventive concepts modify the face seal of the copending application to effect this result.
One further difiiculty found with the sealing means of the prior application results from the preferred material utilized in the manufacture of the rotating element. A synthetic resin, specifically polytetrafluoroethylene (Teflon), was initially utilized for the formation of the rotating element, but it has now been found that this material is subject to warping in use. Due to the necessity for extremely accurate mating of the fixed and rotating elements, even slight dimensional changes of the rotating element can reduce the effectiveness of the seal. The instant invention replaces the Teflon rotating element with an element formed of a material which is dimensionally stable under the conditions of use.
Although the instant inventive concepts are applicable to any sealing means wherein fixed and rotating elements are found, since the most important application of the sealing means is in a continuous flow blood separator of the type disclosed in the aforementioned copending application, the preferred embodiments hereof will be discussed in relation thereto.
`Considering the foregoing, it is a primary object of the instant invention to provide a sealing means of the type described which is free from the foregoing and other such disadvantages. A basic and important objective of this invention is the provision of a sealing means which precludes lateral seepage of blood or fractional components thereof across the interface defined between the fixed and rotating elements. In this regard, the instant inventive concepts provide means intermediate each juxtaposed pair of channels in the face seal which acts as a barrier to such seepage.
Yet another important object of the instant invention is the provision of an arrangement for a face seal wherein the most sensitive component, that is, the packed red blood cells, are passed through the most direct path to preclude any damage thereto.
Further, another important object of this invention is the provision of a face seal wherein the rotating element is formed of a material which is not subject to dimensional change or warpage during use.
Other and further objects of the instant inventive concepts will either be specifically mentioned in the following detailed description or will be obvious therefrom.
3 Such detailed description makes reference to the accompanying drawing wherein:
FIG. 1 is a vertical cross-sectional view through a centrifuge means incorporating a face seal according to the instant inventive concepts;
FIG. 2 is a bottom plan view of the fixed or stationary element of the face seal;
FIG. 3 is a transverse cross-sectional view taken substantially onlines 3--3 of FIG. 2;
FIG. 4 is a top plan view of the rotating element of the face seal; and
FIG. 5 is a transverse cross-sectional view taken substantially on lines 5-5 of FIG. 4, showing cooperating portions of the centrifuge means in dotted lines.
Like reference characters refer to like parts throughout the several views of the drawing.
Reference may be made to the aforementioned copending application which, as has been mentioned hereinabove, is incorporated herein by reference in its entirety, to provide further background on the preferred system with which the improvements of the instant application may be utilized. In such system, whole blood is withdrawn directly from a donor, separated in a centrifuge means into red blood cells, white blood cells or buffy coat and plasma, with one or more of the fractional components being returned directly to the donor from the centrifuge means. Of course, various safety devices are included in the system and the use of these devices would be equally applicable to the means of the instant invention. Additionally, platelets can be withdrawn either with the white blood cells or 'with the plasma and subsequently separated in a second centrifuge, if desired. Further, the various operating means including pumps and the like shown. in the aforementioned copending application are all applicable to use with the modified means of the instant invention.
The basic centrifuge means is designated generally by the reference numeral in FIG. l and includes a bowl or shell y12 disposed within a casing (not shown) which is utilized to rotate the bowl and its associated elements about a central axis. Theshell 12 has an upstanding cylindrical sidewall means 14 Which terminates in an outwardly and upwardly directedflange 16. Thebottom wall 18 of theshell 12 is provided with an annular depending flange 20y and acentral spindle 22 utilized for centering theshell 12 with respect to the outer casing.
The interior of thesidewalls 14 of theshell 12 serve to provide the outer boundary for the separation channel 24. Starting iat the top of theshell 12, awall portion 26 extends linearly downwardly for a predetermined distance, then merges smoothly into an inwardly and downwardlyinclined wall portion 28 which in turn merges into another linearly extendingwall portion 30.
Another portion of the centrifuge assembly or separating means 10 is the center or filler piece designated generally by thereference number 32. This filler piece is suitably suspended within theshell 12 in a manner to be more fully described hereinafter. Acentral bore 34 extends completely from thelower surface 36 of theller piece 32 to the upper surface thereof. A depression 38 is provided in theupper surface 40 of theller piece 32 and an O-ring 42 seals this depression 38 against a protrusion 44 on thecover member 46 thereby providing an enlarged cavity 48. Thisbore 34 provides the input channel for the blood and the cavity 48 permits communication between thebore 34 which is axial and radially offset passageway means 50 for carrying the blood from the seal means in a manner to be described in more `detail hereinafter. This arrangement dilfers from the construction of the separating means in the aforementioned copending application and permits the use of the axial passageway means into the seal means for packed red blood cells which are more sensitive to damage than the whole blood itself.
Theller piece 32 is cylindrically shaped for the most part and of a somewhat smaller diameter than that of theshell wall portion 30. As such, the outer orsidewall 52 of thefiller piece 32 is spaced slightly away from thewall portion 30 to thereby provide the other boundary of the separation channel 24. This channel extends with uniform thickness substantially for the height of theshell wall portion 30. Substantially opposite to theinclined portion 28 of the centrifuge shell, thesidewall 52 of the ller piece is radially curved as shown at 54. This curve merges into an inwardly extending shoulder portion 56 which again turns into an upwardly extending portion at 58 to blend into thetop surface 40.
Thefiller piece 32 is secured to thecover member 46 by bolts or the like 60 which also function to secure a holdingmember 62 in the related assembly.
Thetop cover 46 is preferably fabricated of a clear plastic material 'which permits visual observation of the separation occurring within the centrifuge. This top cover member includes aflange portion 64 which abuts against the top of theflange portion 16 of thecentrifuge shell 12 withbolts 66 securing these elements in related assembly. Gasket means (not shown) are included to preclude against leakage between these parts. Additionally, theflange portion 64 of thecover member 46 includes an angularly offsetportion 68 designed to rest upon, and be frictionally driven by, a driving means (not shown). This manner of rotating the separating means differs slightly from the construction shown in the aforementioned application and has been found to provide better overall operation.
A short vertical wall portion 70 extends downwardly from theange portion 64 of thetop cover 46 to mate contiguously with theWall portion 26 of thecentrifuge shell 12, thereby properly positioning the cover on the shell. At the end of the vertical wall portion 70, there is a horizontally or radially inwardly steppedportion 72 which merges with the top of another short vertical 'wall portion 74. At the bottom of thewall portion 74, there is another radially inwardly stepped portion 76 which merges with the top of a furthervertical wall portion 78. The bottom of thisvertical wall portion 78 merges with thebottom surface 80` of thecover member 46 which rests on thetop surface 40 of theller piece 32.
The `attachment of thefiller piece 32 to thecover member 46 is arranged such that thebottom surface 36 of thefiller piece 32 is spaced slightly from the bottominner surface 82 of theshell 12 to provide achannel 84 through which the whole blood flowing through thebore 34 can spread outwardly to the separation channel 24 and then climb upwardly therealong as the centrifuge is operated.
The seal means of the instant invention is designated generally by the reference numeral and includes a lower orrotating element 102 and an upper orstationary element 104. The lower orrotating element 102 fits within a rst stepped recess orportion 106 on the top of thecover member 46. A second stepped recess orportion 108 is also provided in the top of thecover member 46 with the steppedportion 108 being somewhat smaller than the steppedportion 106. The steppedportion 108 contains a plurality of spaced grooves concentrically arranged around the central axis thereof with O-rings having a rectangular cross-sectional configuration being mounted within each of these grooves. All of the O-rings have been designated generally by thereference numeral 110, but it will be appreciated that the size or diameter of such O-rings continually increases. Since the bottom of therotating element 102 abuts against the top of the various O-rings 110, the overall effect of such arrangement is to set olf a series of channels or annular spaces between the steppedportion 108 and the bottom of therotating element 102. The smallest or innermost O-ring 110 defines therewithin a circular opening or channel means designated 112, with such channel means being axially aligned with the central or rotational axis of the centrifuge means 10. Between this innermost O-ring and the next adjacent O-ring, a first annular channel means 114 is formed. Between the second O-ring and the next adjacent O-ring, a secondannular channel 116 is formed. Finally, between said next adjacent O-ring and the outermost O-ring, a third or outer annular channel means 118 is formed. Each of these channel means serves to receive either the whole blood or the one of the fractional components as will be explained in more detail hereinafter.
To more fully understand the nature of the separation or fractionation which occurs within the centrifuge means 10, it can be seen that the separation channel 24, preferably having an optimum radial dimension of approximately l mm., extends upwardly with uniform thickness until it reaches theinclined wall portion 28 of thecentrifuge shell 12. At this point, the separation channel 24 merges into an enlarged separation space 120. When whole blood enters the centrifuge means it travels downwardly through thecentral bore 34, then outwardly in theseparation channel 84 and upwardly through the separation channel 24 to enter the space 120. Such climbing action is created by a combination of the centrifugal force generated by rotation of thecentrifugal shell 12, thefiller piece 32 and thetop cover 46 and the action of the various pumps described in more detail in the aformentioned copending application. Due to this centrifugal force, the whole blood starts to separate as it begins to climb through the separation channel 24 and due to the difference in specific gravities of the various fractions thereof. The packed red cells are the most dense of the fractions, and these are thus packed outermost within the space 120. The white cells are the next most dense and these are thus positioned adjacent the red cells and the plasma is the least dense and hence is disposed furtherest inwardly within the centrifuge. For purposes of illustration, blood is shown in thebore 34, in theseparation channel 84 and in the lower portion of the separation channel 24. The packed red cells are designated R, the white cells are designated W, and the plasma is designated P. The various fractions are fully separated in the separation space 120 and the quantity of white cells is extremely small whereby, initially, there is merely an interface between the plasma P and the packed red cells R. Proper regulation of the various pumps associated with the separation system, as explained in more detail in the aforementioned copending application, adjusts the plasmared cell interface line to space the same closer to theshell wall 26 or further away therefrom. However, after the blood has been separating for awhile, the white cells W start to build up within the centrifuge to form a buffy coat of the shape generally illustrated in FIG. 1. It will be seen that the white cell layer effectively oats between the red cells and plasma.
A firstradial channel 124 communicates at one end with the separation space 120 at the wall portion 58 to receive the layer of plasma, and thisradial channel 124 turns upwardly at 126 to communicate at its opposite end with the channel means 118 for removal of plasma P through the seal means 100. A second radial channel 128 communicates at one end with the separation space 120 at thewall portion 78 and turns upwardly as at 130 to communicate at its opposite end with the channel means 116 for removal of white blood cells W through the seal means 100. A thirdradial channel 132 communicates at one end with the separation space 120 at thewall portion 74 and turns upwardly as at 134 to lform a portion which is co-axial with the center of rotation of the centrifuge means 10 and which communicates at its opposite end with the channel means 112 for removal of the packed red blood cells R through the seal means 100. Thus, each of the individual fractions of the blood is transferred to its own particular channel means between thetop cover 46 and the seal means 100.
Although only a single channel has been shown communicating the separation space with the individual channel means defined between thetop cover 46 and the seal means 100, it will be understood that such an arrangement is illustrative and a plurality of ports or channels can be provided to carry each of the fractional components of the blood to their respective channel means. Additionally, as will be readily understood that those skilled in the art, these fractional components are withdrawn from the separating means 10 with the aid of pumps as explained in more det-ail in the aforementioned copending patent application.
To understand the nature and construction of the seal means 100, attention is directed particularly to FIGS. 2-5 which show in further detail therotating element 102 and the fixedelement 104. Therotating element 102 is preferably formed of a ceramic material which has been found to ibe dimensionally stable under the conditions of use. As mentioned previously, it was found that Teiion had a tendency to warp from the heat of the blood and the operation of the device causing a reduction in the effectiveness of the seal. Manufacture of therotating element 102 from ceramic material precludes this disadvantage. Therotating element 102 has acircular base portion 140 with a atbottom surface 142. The size of this base portion corresponds substantially to the size of the steppedportion 106 in thecover member 46 and, as mentioned previously, when therotating element 102 is positioned within thetop cover 46, thebottom surface 142 abuts against the top of the O-rings 110. To prevent relative rotation between therotating element 102 and thecover member 46, asmall notch 144 can be provided in the periphery of thebase portion 140, if desired. Thisnotch 144 may mate With a guide pin 146 positioned at one edge of the steppedrecess 106 in thetop cover 46. Further means of securing therotating element 102 to thetop cover 46 comprises thepressure plate 62 which includes an inwardly directed ange 148 which seats over thebase portion 140 of therotating element 102 as shown in FIG. 1. Thebolts 60 function to secure this element to thefiller piece 32 through thetop cover 46 thereby securing the entire assembly together. Alternatively, separate bolts may be utilized to secure thecover member 46 to thefiller piece 32 and to secure thepressure plate 62 to thecover member 46. Further, thepressure plate 62 may merely function to assist in securing therotating element 102 in position, with its primary function being as a handle to facilitate removal of the centrifuge means 10 from the casing (not shown) in which it is mounted in the assembly. To this end, an outstanding peripheral flange 150 may be provided on the pressure plate or handle 62.
Therotating element 102 also includes an upstandingcylindrical body portion 152 integral with thebase portion 140, but having a cross-sectional diameter somewhat smaller than that of thebase portion 140. Thetop surface 154 of therotating element 102 is planar according to the instant inventive concepts, although, if desired, mating portions of the channel means and groove means defined in the fixedelement 104 and to be described in more detail hereinafter, may be provided in thetop surface 154. However, it has been found that a better seal is provided if this element has a planar top surface.
At the center of therotating element 102, acentral bore 156 is provided which functions as a passageway means for withdrawing packed red blood cells from the channel means 112 through therotating element 102. The upper portion of this passageway means 156 and the lower portion of an aligned passageway means in the fixedelement 104 to be described in more detail hereinafter together define a channel means for the red blood cells at the interface between these elements.
In addition to the central bore or passageway means 156 a plurality of additional bores or passageway means 158 are arranged concentrically about thecentral bore 156 in communication with the channel means 114 and in communication with the channel means for the whole blood to lbe provided at the interface between the rotating and fixed elements as described in more detail hereinafter. Additional concentrically arranged bores or passageway means 160 are provided in communication with the channel means 116 for carrying white blood cells through therotating element 102 and still further concentrically arranged bores or passageway means 162 are provided to communicate with the channel means 118 for carrying plasma through therotating element 102. Thebores 158, 160 and 162, as will be seen from the drawing, are arranged on concentric circles of increasing diameter. These circles correspond to the mean diameters of the channel means provided at the interface between the fixed and rotating elements as will be explained in further detail hereinafter.
As mentioned previously, the fixedelement 102 is formed of ceramic and thus, is not subject to dimensional change or instability during use.
As will be seen, there is a series of annular lands formed by thetop surface 154 of therotating element 102. These lands act as boundaries between the various passageway means, and as will be explained in further detail hereinafter, cooperate with certain groove means in the fixedelement 104 to preclude cross-over or seepage between the various channel means carrying the whole blood and fractional components thereof.
By referring now more particularly to FIGS. 2 and 3, the exact nature of the upper or fixed seal means 104 will be better understood. This element is preferably formed of stainless steel and has a fiatlower surface 164 Which is preferably lapped to a fiatness of 3 light waves or less and which rests on theupper surface 154 of therotating element 102, thisupper surface 154 also preferably being lapped to a iiatness of 3 light waves or less. Acentral bore 166 is defined in the fixedelement 104 and is aligned with thecentral bore 156 of therotating element 102 to receive the packed red blood cells therefrom and pass the same totubing 167 for removal from the separating means 10. This use of a continuous central bore through the seal means 100 to carry the packed red blood cells functions to provide a more direct pathway for the red blood cells which, as mentioned, previously, are particularly sensitive. Concentrically arranged annular channel means 168, 170 and 172 are designed to mate with the openings at the tops of the passageway means 158, 160 and 162 in therotating element 102. Bores or passageway means 174, 176 and 178 communicate with the channel means 168, 170 and 172 respectively at one end and withflexible tubing 180, 182 and 184 at their opposite ends. In this manner, whole blood is passed, from a source of the same, in a continuous blood separator, from the donor, through thetubing 180 to bore 174, the channel means 168, the passageway means 158, the channel means 114, the bore 50 and the cavity 48 to the separating means. White blood cells pass from the separating means through the channel means 116, the passageway means 160, the channel means 170, the passageway means 176 and thetubing 182 to any desired location. The plasma, when received from the separating means 10, passes through the channel means 118, the passageway mean 162, the channel means 172, the passageway means 178 and thetubing 184 to any desired location, generally back to the donor in a continuous blood separator.
Finally, an annular channel means 190 is provided in the fixedelement 104 to define a saline-receiving channel to cool the seal means 100 and to provide an air barrier to protect the blood and other fractional components in the remainder of the seal means 100 against the entrance of air.Tubing 192 communicates through abore 194 with this outer channel means for introduction, generally by gravity, of saline to the channel means 190 andtubing 196 communicates with the channel means 190 through abore 198 for slow removal of saline therefrom. A clamp or the like (not shown) may be utilized on thetubing 196 to regulate removal of saline from the channel means 190.
A mojor feature of the instant inventive concepts is the provision of groove means 200 in the lands separating the various channel means in the fixedelement 104. These groove means 200 communicate through a passageway means 202 with atube 204. Saline under pressure is fed through thetube 204 to the groove means 200. The pressure of the saline in these groove means is at least as great as the pressure of the blood or the fractional components thereof in the various channel means. With a continuous flow blood separator of the type shown in the aforementioned copending application, the blood could be under arterial pressure whereby the pressure of the saline in the groove means 200 is at least this great. Preferably, saline is forced into the groove means 200 at a pressure in excess of arterial pressure. Arterial pressure is generally considered to be about 200 mrn. of mercury and the pres sure behind the saline in the groove means 200 is preferably from about 10-12 p.s.i. at a iiow rate of about 20 ml./hr. Thus, a portion of the saline is caused to iiow laterally from earh of the groove means arross the interface toward juxtaposed channel means to assist in precluding seepage of the blood and components across the interface which, as mentioned previously, may damage the various materials in the channel means and may cause mixing of the same. Leakage of the saline from the outer groove means 200 around the periphery of the seal means will not cause any difficulty and will merely fiow downwardly into the separating means 10.
Reference may be made to the aforementioned copending application wherein a pivotally carried arm means is shown which cooperates with the seal means to press downwardly on the fixedelement 104 during use. This arm means (not shown herein) may be readily raised to remove the centrifuge assembly when desired.
It is believed that the operation of the separating means will be readily understood from the foregoing detailed descirption. It can be seen that there is herein provided an improved construction of such separating means, and particularly the seal means thereof, which satisfies all of the objectives of the instant invention and others, including many advantages of great practical utility and commercial importance. Since many embodiments may be made of the instant inventive concepts, and since many modifications may be made of the embodiments herein before shown and described, it is to be understood that all matter is to be interpreted merely as illustrative and not in a limiting sense.
Accordingly, what is claimed is:
1. In a blood separator of the type wherein means are provided for separating blood from a source of the` same into a plurality of fractional components, said blood separator having seal means associated with the separating means, said seal means including a fixed element and a rotating element having portions which abuttingly engage each other to define an interface therebetween, portions of said seal means defining spaced channel means at said interface for receiving in different channel means either blood to be separated from said source or fractional components of the separated blood from said separating means, and separate passageway means communicating with said seal means for bringing said blood to one of said channel means from said source through said fixed element, for feeding said blood from said one channel means to said separating means through said rotating element, for bringing said fractional components of said blood from said separating means to others of said channel means through said rotating element, and for withdrawing said fractional components from said other channel means through said fixed element, the improvement which comprises:
(a) portions of said seal means defining groove means at said interface between said pair of juxtaposed channel means, and
(b) means for feeding saline solution into each of said groove means at a pressure at least as great as the pressure of said blood and fractional components thereof in said juxtaposed channel means.
2. The improvement of claim 1 wherein said blood separator includes means for continuously withdrawing blood from a donor and means for continuously returning at least one of said fractional components thereof to the donor after separation, said saline feeding means forcing saline into each of said groove means at a pressure at least equal to arterial pressure.
3. The improvement of claim 2 wherein said saline feeding means forces saline into each of said groove means at a pressure in excess of arterial pressure.
4. The improvement of claim 1 wherein said saline feeding means forces saline into each of said groove means at a pressure suicient to cause a portion of said saline to flow laterally from each of said groove means across said interface toward juxtaposed channel means.
5. The improvement of claim 1 wherein said channel means includes a central channel means coincident with the axis of rotation of said seal means and at least two circular channel means concentric with said central channel means, said circular channel means being radially spaced from said central channel means and from each other, said groove means being provided at least between said central channel means and the rst concentric circular channel means and between each additional pair of juxtaposed circular channel means.
6. The improvement of claim S wherein one of said fractional components includes packed red blood cells, said passageway means including an axial passageway means in said rotating element communicating the portion of said separating means containing said packed red blood cells with said central channel means and an axial passageway means in said fixed element communicating with said central channel means for withdrawing said red blood cells from said seal means.
7. The improvement of claim 1 further including portions of said seal means defining an outer channel means at said interface for receiving saline solution to cool said seal means and to provide an air barrier to protect said blood and said fractional components in the remainder of said channel means, means for feeding saline solution to said outer channel means, and means for slowly removing said saline solution from said outer channel means.
8. The improvement of claim 1 wherein said xed and rotating elements each have a planar face portion, said planar face portions abutting each other and together deining said interface, and all of said channel means and all of said groove means being delined in said planar face portion of said xed element.
9. The improvement of claim 8 wherein said rotating element is formed of ceramic.
10'. The improvement of claim 9 wherein said xed element is formed of stainless steel.
References Cited UNITED STATES PATENTS 2,822,126 2/1958 `Cohn 233-1 2,876,769 3/1959 Cordova 23-2585 3,145,713 8/1964 Latham 128-214 3,195,809 7/1965 Pickels et al. 233-21 3,231,184 1/1966 Podbielniak 233-21 X 3,292,937 12/1966 Nunley 277-59 3,443,747 5/1969 Jacobson et al. 233-22 DALTON L. TRULUCK, Primary Examiner U.S. Cl. X.R.
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US3747843A (en)*1971-04-091973-07-24Damon CorpContinuous flow zonal rotor
US3904109A (en)*1973-12-141975-09-09Gene E UnderwoodMultiple density separator
FR2308380A1 (en)*1975-04-251976-11-19Us Energy PROCESS AND CONTROL SYSTEM FOR A CONTINUOUS FLOW CENTRIFUGE FOR THE SEPARATION OF BLOOD FRACTIONS
FR2350885A1 (en)*1976-05-141977-12-09Baxter Travenol Lab CENTRIFUGAL SEPARATOR OF THE DISPOSABLE TYPE TO FRACTION THE BLOOD
FR2392663A1 (en)*1976-10-061978-12-29Haemonetics Corp
FR2395785A1 (en)*1977-06-271979-01-26Ibm DEVICE FOR THE CONTINUOUS RECOVERY OF FRACTIONS OF A LIQUID MIXTURE SUBJECT TO CENTRIFUGATION
US4151844A (en)*1977-11-111979-05-01Baxter Travenol Laboratories, Inc.Method and apparatus for separating whole blood into its components and for automatically collecting one component
EP0026333A1 (en)*1979-09-281981-04-08Gambro Dialysatoren K.G.Transferring means for use in a device for separating of liquids, especially whole blood
US4446015A (en)*1981-11-301984-05-01E. I. Du Pont De Nemours And CompanyField flow fractionation channel
US4446014A (en)*1981-11-301984-05-01Dilks Jr Charles HSedimentation field flow fractionation channel and method
US4448679A (en)*1981-11-301984-05-15E. I. Du Pont De Nemours And CompanyApparatus and method for sedimentation field flow fractionation
EP0125675A3 (en)*1983-05-161987-01-14E.I. Du Pont De Nemours And CompanyRotating seal for continuous flow centrifuge
WO1987001307A1 (en)*1985-09-101987-03-12Vereniging Het Nederlands Kanker InstituutMethod and device for the separation and isolation of blood or bone marrow components
WO1988005332A1 (en)*1987-01-131988-07-28Mclaughlin, William, F.Continuous centrifugation system and method for directly deriving intermediate density material from a suspension
US4767397A (en)*1987-03-091988-08-30Damon CorporationApparatus for liquid separation
US4776964A (en)*1984-08-241988-10-11William F. McLaughlinClosed hemapheresis system and method
US4781215A (en)*1983-08-091988-11-01Mayhall Jr Riley HPackage wrapping machine system
US4810240A (en)*1986-11-051989-03-07Frau S.P.A.Centrifugal separator of liquids with rotating seals on the fixed upper head
US4851126A (en)*1987-11-251989-07-25Baxter International Inc.Apparatus and methods for generating platelet concentrate
US4944883A (en)*1987-01-131990-07-31Schoendorfer Donald WContinuous centrifugation system and method for directly deriving intermediate density material from a suspension
US4965846A (en)*1986-08-111990-10-23Baxter International Inc.Pivot pin bearing/seal with loose eyelet especially suited for disposable continuous flow blood filtration system cartridges
US5053127A (en)*1987-01-131991-10-01William F. McLaughlinContinuous centrifugation system and method for directly deriving intermediate density material from a suspension
US5100372A (en)*1990-03-021992-03-31Haemonetics CorporationCore for blood processing apparatus
US5133729A (en)*1990-08-171992-07-28Smith & Nephew Dyonics Inc.Motor driven hand piece for a surgical tool
US5360542A (en)*1991-12-231994-11-01Baxter International Inc.Centrifuge with separable bowl and spool elements providing access to the separation chamber
US5362291A (en)*1991-12-231994-11-08Baxter International Inc.Centrifugal processing system with direct access drawer
US5370802A (en)*1987-01-301994-12-06Baxter International Inc.Enhanced yield platelet collection systems and methods
US5427695A (en)*1993-07-261995-06-27Baxter International Inc.Systems and methods for on line collecting and resuspending cellular-rich blood products like platelet concentrate
US5549834A (en)*1991-12-231996-08-27Baxter International Inc.Systems and methods for reducing the number of leukocytes in cellular products like platelets harvested for therapeutic purposes
US5573678A (en)*1987-01-301996-11-12Baxter International Inc.Blood processing systems and methods for collecting mono nuclear cells
US5628915A (en)*1987-01-301997-05-13Baxter International Inc.Enhanced yield blood processing systems and methods establishing controlled vortex flow conditions
US5632893A (en)*1987-01-301997-05-27Baxter Internatinoal Inc.Enhanced yield blood processing systems with angled interface control surface
US5641414A (en)*1987-01-301997-06-24Baxter International Inc.Blood processing systems and methods which restrict in flow of whole blood to increase platelet yields
US5690835A (en)*1991-12-231997-11-25Baxter International Inc.Systems and methods for on line collection of cellular blood components that assure donor comfort
US5961842A (en)*1995-06-071999-10-05Baxter International Inc.Systems and methods for collecting mononuclear cells employing control of packed red blood cell hematocrit
US5980760A (en)*1997-07-011999-11-09Baxter International Inc.System and methods for harvesting mononuclear cells by recirculation of packed red blood cells
US5993370A (en)*1987-01-301999-11-30Baxter International Inc.Enhanced yield collection systems and methods for obtaining concentrated platelets from platelet-rich plasma
US6007725A (en)*1991-12-231999-12-28Baxter International Inc.Systems and methods for on line collection of cellular blood components that assure donor comfort
US6027657A (en)*1997-07-012000-02-22Baxter International Inc.Systems and methods for collecting diluted mononuclear cells
US6315706B1 (en)*1996-02-262001-11-13Gambro, Inc.Method for separating cells, especially platelets, and bag assembly therefor
US6511411B1 (en)1987-01-302003-01-28Baxter International Inc.Compact enhanced yield blood processing systems
US6582349B1 (en)1997-07-012003-06-24Baxter International Inc.Blood processing system
US6656105B2 (en)1999-05-312003-12-02Gambro, Inc.Centrifuge for processing blood and blood components in ring-type blood processing bags
US6689042B2 (en)1997-02-122004-02-10Gambro, Inc.Centrifuge and container system for treatment of blood and blood components
US6736768B2 (en)2000-11-022004-05-18Gambro IncFluid separation devices, systems and/or methods using a fluid pressure driven and/or balanced approach
US6740239B2 (en)1999-10-262004-05-25Gambro, Inc.Method and apparatus for processing blood and blood components
US7279107B2 (en)2002-04-162007-10-09Gambro, Inc.Blood component processing system, apparatus, and method
WO2012137086A1 (en)*2011-04-082012-10-11Sorin Group Italia S.R.L.Disposable device for centrifugal blood separation
US9079194B2 (en)2010-07-192015-07-14Terumo Bct, Inc.Centrifuge for processing blood and blood components
US10039876B2 (en)2014-04-302018-08-07Sorin Group Italia S.R.L.System for removing undesirable elements from blood using a first wash step and a second wash step

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US3747843A (en)*1971-04-091973-07-24Damon CorpContinuous flow zonal rotor
US3904109A (en)*1973-12-141975-09-09Gene E UnderwoodMultiple density separator
FR2308380A1 (en)*1975-04-251976-11-19Us Energy PROCESS AND CONTROL SYSTEM FOR A CONTINUOUS FLOW CENTRIFUGE FOR THE SEPARATION OF BLOOD FRACTIONS
FR2350885A1 (en)*1976-05-141977-12-09Baxter Travenol Lab CENTRIFUGAL SEPARATOR OF THE DISPOSABLE TYPE TO FRACTION THE BLOOD
FR2392663A1 (en)*1976-10-061978-12-29Haemonetics Corp
FR2395785A1 (en)*1977-06-271979-01-26Ibm DEVICE FOR THE CONTINUOUS RECOVERY OF FRACTIONS OF A LIQUID MIXTURE SUBJECT TO CENTRIFUGATION
US4151844A (en)*1977-11-111979-05-01Baxter Travenol Laboratories, Inc.Method and apparatus for separating whole blood into its components and for automatically collecting one component
EP0026333A1 (en)*1979-09-281981-04-08Gambro Dialysatoren K.G.Transferring means for use in a device for separating of liquids, especially whole blood
US4350284A (en)*1979-09-281982-09-21Gambro Dialysatoren KgTransferring means for use in a device for separating liquids
US4446015A (en)*1981-11-301984-05-01E. I. Du Pont De Nemours And CompanyField flow fractionation channel
US4446014A (en)*1981-11-301984-05-01Dilks Jr Charles HSedimentation field flow fractionation channel and method
US4448679A (en)*1981-11-301984-05-15E. I. Du Pont De Nemours And CompanyApparatus and method for sedimentation field flow fractionation
EP0125675A3 (en)*1983-05-161987-01-14E.I. Du Pont De Nemours And CompanyRotating seal for continuous flow centrifuge
US4781215A (en)*1983-08-091988-11-01Mayhall Jr Riley HPackage wrapping machine system
US4776964A (en)*1984-08-241988-10-11William F. McLaughlinClosed hemapheresis system and method
US4911833A (en)*1984-08-241990-03-27William F. McLaughlinClosed hemapheresis system and method
WO1987001307A1 (en)*1985-09-101987-03-12Vereniging Het Nederlands Kanker InstituutMethod and device for the separation and isolation of blood or bone marrow components
US4850952A (en)*1985-09-101989-07-25Figdor Carl GMethod and device for the separation and isolation of blood or bone marrow components
US4965846A (en)*1986-08-111990-10-23Baxter International Inc.Pivot pin bearing/seal with loose eyelet especially suited for disposable continuous flow blood filtration system cartridges
US4810240A (en)*1986-11-051989-03-07Frau S.P.A.Centrifugal separator of liquids with rotating seals on the fixed upper head
WO1988005332A1 (en)*1987-01-131988-07-28Mclaughlin, William, F.Continuous centrifugation system and method for directly deriving intermediate density material from a suspension
AU604843B2 (en)*1987-01-131991-01-03Mclaughlin, William F.Continuous centrifugation system and method for directly deriving intermediate density material from a suspension
US5053127A (en)*1987-01-131991-10-01William F. McLaughlinContinuous centrifugation system and method for directly deriving intermediate density material from a suspension
US4944883A (en)*1987-01-131990-07-31Schoendorfer Donald WContinuous centrifugation system and method for directly deriving intermediate density material from a suspension
US5632893A (en)*1987-01-301997-05-27Baxter Internatinoal Inc.Enhanced yield blood processing systems with angled interface control surface
US6511411B1 (en)1987-01-302003-01-28Baxter International Inc.Compact enhanced yield blood processing systems
US6899666B2 (en)1987-01-302005-05-31Baxter International Inc.Blood processing systems and methods
US20030102272A1 (en)*1987-01-302003-06-05Baxter International Inc.Blood processing systems and methods
US5993370A (en)*1987-01-301999-11-30Baxter International Inc.Enhanced yield collection systems and methods for obtaining concentrated platelets from platelet-rich plasma
US5807492A (en)*1987-01-301998-09-15Baxter International Inc.Blood processing systems and methods for collecting mono nuclear cell
US5370802A (en)*1987-01-301994-12-06Baxter International Inc.Enhanced yield platelet collection systems and methods
US5750039A (en)*1987-01-301998-05-12Baxter International Inc.Blood processing systems and methods for collecting mono nuclear cells
US5529691A (en)*1987-01-301996-06-25Baxter International Inc.Enhanced yield platelet collection systems and method
US5641414A (en)*1987-01-301997-06-24Baxter International Inc.Blood processing systems and methods which restrict in flow of whole blood to increase platelet yields
US5573678A (en)*1987-01-301996-11-12Baxter International Inc.Blood processing systems and methods for collecting mono nuclear cells
US5628915A (en)*1987-01-301997-05-13Baxter International Inc.Enhanced yield blood processing systems and methods establishing controlled vortex flow conditions
US4767397A (en)*1987-03-091988-08-30Damon CorporationApparatus for liquid separation
US4851126A (en)*1987-11-251989-07-25Baxter International Inc.Apparatus and methods for generating platelet concentrate
US5100372A (en)*1990-03-021992-03-31Haemonetics CorporationCore for blood processing apparatus
US5133729A (en)*1990-08-171992-07-28Smith & Nephew Dyonics Inc.Motor driven hand piece for a surgical tool
US6071421A (en)*1991-12-232000-06-06Baxter International Inc.Systems and methods for obtaining a platelet suspension having a reduced number of leukocytes
US5549834A (en)*1991-12-231996-08-27Baxter International Inc.Systems and methods for reducing the number of leukocytes in cellular products like platelets harvested for therapeutic purposes
US5690835A (en)*1991-12-231997-11-25Baxter International Inc.Systems and methods for on line collection of cellular blood components that assure donor comfort
US5804079A (en)*1991-12-231998-09-08Baxter International Inc.Systems and methods for reducing the number of leukocytes in cellular products like platelets harvested for therapeutic purposes
US5362291A (en)*1991-12-231994-11-08Baxter International Inc.Centrifugal processing system with direct access drawer
US5360542A (en)*1991-12-231994-11-01Baxter International Inc.Centrifuge with separable bowl and spool elements providing access to the separation chamber
US6007725A (en)*1991-12-231999-12-28Baxter International Inc.Systems and methods for on line collection of cellular blood components that assure donor comfort
US5427695A (en)*1993-07-261995-06-27Baxter International Inc.Systems and methods for on line collecting and resuspending cellular-rich blood products like platelet concentrate
US5961842A (en)*1995-06-071999-10-05Baxter International Inc.Systems and methods for collecting mononuclear cells employing control of packed red blood cell hematocrit
US6315706B1 (en)*1996-02-262001-11-13Gambro, Inc.Method for separating cells, especially platelets, and bag assembly therefor
US6855102B2 (en)1996-02-262005-02-15Gambro IncMethod for separating cells, especially platelets, and bag assembly therefor
US6689042B2 (en)1997-02-122004-02-10Gambro, Inc.Centrifuge and container system for treatment of blood and blood components
US20030211927A1 (en)*1997-07-012003-11-13Baxter International Inc.Blood processing chamber counter-balanced with blood-free liquid
US6582349B1 (en)1997-07-012003-06-24Baxter International Inc.Blood processing system
US6027657A (en)*1997-07-012000-02-22Baxter International Inc.Systems and methods for collecting diluted mononuclear cells
US5980760A (en)*1997-07-011999-11-09Baxter International Inc.System and methods for harvesting mononuclear cells by recirculation of packed red blood cells
US6656105B2 (en)1999-05-312003-12-02Gambro, Inc.Centrifuge for processing blood and blood components in ring-type blood processing bags
US7235041B2 (en)1999-05-312007-06-26Gambro Bct, Inc.Centrifuge for processing a blood product with a bag set having a processing bag
US20060270542A1 (en)*1999-05-312006-11-30Gambro, Inc.Centrifuge for Processing Blood and Blood Components
US7097774B2 (en)1999-05-312006-08-29Gambro IncMethod for processing a blood product with a bag set having a multi-way connector
US6740239B2 (en)1999-10-262004-05-25Gambro, Inc.Method and apparatus for processing blood and blood components
US7094196B2 (en)2000-11-022006-08-22Gambro Inc.Fluid separation methods using a fluid pressure driven and/or balanced approach
US7094197B2 (en)2000-11-022006-08-22Gambro, Inc.Method for fluid separation devices using a fluid pressure balanced configuration
US20040164032A1 (en)*2000-11-022004-08-26Gambro, Inc.Fluid Separation Methods Using a Fluid Pressure Driven and/or Balanced Approach
US6773389B2 (en)2000-11-022004-08-10Gambro IncFluid separation devices, systems and/or methods using a fluid pressure driven and/or balanced configuration
US6736768B2 (en)2000-11-022004-05-18Gambro IncFluid separation devices, systems and/or methods using a fluid pressure driven and/or balanced approach
US7279107B2 (en)2002-04-162007-10-09Gambro, Inc.Blood component processing system, apparatus, and method
US7497944B2 (en)2002-04-162009-03-03Caridianbct, Inc.Blood component processing system, apparatus, and method
US7708889B2 (en)2002-04-162010-05-04Caridianbct, Inc.Blood component processing system method
US9079194B2 (en)2010-07-192015-07-14Terumo Bct, Inc.Centrifuge for processing blood and blood components
WO2012137086A1 (en)*2011-04-082012-10-11Sorin Group Italia S.R.L.Disposable device for centrifugal blood separation
US9308314B2 (en)2011-04-082016-04-12Sorin Group Italia S.R.L.Disposable device for centrifugal blood separation
US10039876B2 (en)2014-04-302018-08-07Sorin Group Italia S.R.L.System for removing undesirable elements from blood using a first wash step and a second wash step
US10293098B2 (en)2014-04-302019-05-21Sorin Group Italia S.R.L.System for removing undesirable elements from blood using a first wash step and a second wash step

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