Method and apparatus for filtering suspensions of medical and biological fluids or the like

• US 6,497,821 B1
• Filed: 05/17/1999
• Issued: 12/24/2002
• Est. Priority Date: 09/25/1996
• Status: Expired due to Term

• Current Assignee: Baxter International Inc.
• Original Assignee: Baxter International Inc.
• Inventors: Sternberg, Shmuel, Prince, Paul R., Pekkarinen, Michael O., Bellamy, David Jr.
• Primary Examiner(s): Drodge, Joseph W.
• Application Number:
  US09/312,883
• Time in Patent Office: 1,317 Days
• Field of Search: 210/321.69, 210/500.22, 210/500.38, 210/500.39, 210/500.4, 210/500.26, 210/636, 210/637, 210/644, 210/645, 210/650, 210/651, 210/767, 210/782, 210/321.6, 210/321.78, 210/321.87, 210/780, 210/781, 210/321.67, 210/321.68, 210/506, 210/137, 210/138, 216/2, 216/56
• US Class Current: 210/651
• CPC Class Codes: A61M 1/262 rotating
• CPC Class Codes: A61M 1/265 inducing Taylor vortices
• CPC Class Codes: A61M 1/34 Filtering material out of the blood by passing it through a membrane, i.e. hemofiltration or diafiltration
• CPC Class Codes: A61M 1/3403 Regulation parameters
• CPC Class Codes: A61M 1/341 by measuring the filtrate rate or volume
• CPC Class Codes: A61M 2202/0035 fluid leaving the cross-flow filter without having passed through the filtering element
• CPC Class Codes: A61M 2202/0042 filtrate, i.e. the fluid passing through the filter
• CPC Class Codes: A61M 2202/0429 Red blood cells; Erythrocytes
• CPC Class Codes: A61M 2202/0439 White blood cells; Leucocytes lymphocytes A61M2202/0407
• CPC Class Codes: A61M 2205/3334 Measuring or controlling the flow rate
• CPC Class Codes: B01D 2321/20 By influencing the flow
• CPC Class Codes: B01D 2321/2025 Tangential inlet
• CPC Class Codes: B01D 2321/2058 by vibration of the membrane, e.g. with an actuator
• CPC Class Codes: B01D 2321/2066 Pulsated flow
• CPC Class Codes: B01D 39/1692 Other shaped material, e.g. perforated or porous sheets
• CPC Class Codes: B01D 61/147 Microfiltration
• CPC Class Codes: B01D 61/22 Controlling or regulating
• CPC Class Codes: B01D 63/16 Rotary, reciprocated or vibrated modules
• CPC Class Codes: B01D 65/08 Prevention of membrane fouling or of concentration polarisation
• CPC Class Codes: B01D 69/02 characterised by their properties

Abstract

A method and apparatus for filtering suspensions of medical and biological fluids, one aspect of which is separating a suspension comprising at least two types of particles which are differently sized or shaped and in which the first type of particle may be deformable at a relatively lower force and/or faster rate than the second type of particle. A filter member is provided having substantially precisely dimensioned pore sizes, with the pores being dimensioned to allow passage of the first type of suspended particle without distortion or only minimal distortion and passage of the second type of particle only with substantial distortion. Because the filter membrane has precisely dimensioned pores, with spacing between the pores being maintained despite the smaller interval between the pores, the porosity of the membrane may be much greater than nominal pore size membranes, allowing faster filtration rates and/or smaller membranes for a given filtration rate, while reducing the exposure time of the cells within the shear environment, and consequently reducing particle damage. Various methods for preventing clogging of the membrane are also disclosed.

Claims

1. A method for separating red blood cells in whole blood from white blood cells comprising:

providing a filter membrane having substantially precisely dimensioned pores, said pores being dimensioned to correspond substantially to the shape of a cross section of said red blood cells to allow passage of substantially undeformed red blood cells through said pores while precluding passage of undeformed white blood cells; and

contacting the whole blood and said membrane such that said white cells are in contact with said membrane for a time less than that needed to deform said white blood cells to a size and shape capable of passing through said membrane.

2. A method for separating red blood cells in whole blood from white blood cells comprising:

providing a filter membrane having substantially precisely dimensioned pores, said pores being dimensioned to correspond substantially to the shape of a cross section of said red blood cells to allow passage of substantially undeformed red blood cells through said pores while precluding passage of undeformed white blood cells; and

contacting the whole blood and said membrane with a force less than that needed to deform said white blood cells to a size and shape capable of passing through said membrane.

3. An apparatus for separating red blood cells in whole blood from white blood cells comprising:

a filter membrane having substantially precisely dimensioned pores, said pores being dimensioned to correspond substantially to the shape of a cross section of said red blood cells to allow passage of substantially undeformed red blood cells through said pores while precluding passage of undeformed white blood cells; and

means for contacting the whole blood in said membrane such that said white cells are in contact with said membrane for a time less than that needed to deform said white blood cells to a size and shape capable of passing through said membrane.

4. An apparatus for separating red blood cells in whole blood from white blood cells comprising:

a filter membrane having substantially precisely dimensioned pores, said pores being dimensioned to correspond substantially to the shape of a cross section of said red blood cells to allow passage of substantially undeformed red blood cells through said pores while precluding passage of undeformed white blood cells; and

means for contacting the whole blood and said membrane with a force less than that needed to deform said white blood cells to a size and shape capable of passing through said membrane.

5. A method for separating a suspension comprising at least first and second types of particles of different shape, the first type of particle being deformable at a relatively lower force than the second type of particle, said method comprising:

providing a filter membrane having pores with substantially precisely dimensioned shapes and sizes, said pore shapes and sizes being dimensioned to correspond substantially to the shape of said first particle to allow passage of said first type of particle and to block passage of said second type of particle; and

contacting the suspension and said membrane with a force sufficient to allow any required deformation of said first type of particle for passage through said pores and insufficient to allow deformation of said second type of particle for passage through said pores, so as to allow passage of said first type of particle through said pores and to block passage of said second type of particle through said pores.

7. The method of claim 5 or 6 further comprising removing said second type of particle from said membrane to prevent clogging of said pores.

8. The method of claim 7 in which the step of contacting said suspension and said membrane includes providing relative movement between said suspension and said membrane.

9. The method of claim 8 in which said relative movement includes movement generally parallel to said membrane.

10. The method of claim 8 in which said relative movement includes movement generally perpendicular to membrane.

11. The method of claim 5 or 6 including varying the contact pressure between the suspension and said membrane to enhance passage of said first type of particle through said pores.

12. The method of claim 11 in which the contact pressure between the suspension and said membrane is increased for a time sufficient to allow any required deformation and passage of said first type of particle through said pores and insufficient to allow deformation of said second type of particle for passage through said pores.

13. The method of claim 5 or 6 including varying the contact pressure between the suspension and said membrane to enhance removal of said second type of particle from entrance to said pores.

14. The method of claim 5 or 6 in which said first and second particles are red blood cells and white blood cells, respectively, and said pores are substantially rectangularly shaped, having a width of approximately 1.0 to 3.5 microns and a length of 6 to 14 microns.

6. A method for separating a suspension comprising at least first and second types of particles of different shape, the first type of particle being deformable at a relatively faster rate than the second type of particle, the method comprising:

providing a filter membrane having pores with substantially precisely dimensioned shapes and sizes, said pore shapes and sizes being dimensioned to correspond substantially to the shape of said first particle to allow passage of said first type of particle and to block passage of said second type of particle; and

contacting the suspension and said membrane such that said first type of particles are in contact with said membrane for a time sufficient to allow any required deformation and passage of said first type of particle through said pores and such that said second type of particle are in contact with said membrane for a time insufficient to allow deformation of said second type of particle for passage through said pores so as to allow passage of said first type of particle through said pores and to block passage of said second type of particle through said pores.

15. An apparatus for separating a suspension comprising at least first and second types of particles of different shape, said first type of particle being deformable at a relatively faster rate than said second type of particle, said apparatus comprising:

a filter membrane having pores with substantially precisely dimensioned shapes and sizes, said pore shapes and sizes being dimensioned to correspond substantially to the shape of said first particle to allow passage of said first type of particle and to block passage of said second type of particle; and

means for contacting the suspension and said membrane for a time sufficient to allow any required deformation of said first type of particle for passage through said pores and insufficient to allow deformation of said second type of particle for passage through said pores so as to allow passage of said first type of particle through said pores and to block passage of said second type of particle through said pores.

16. The apparatus of claim 15 including means for varying the contact pressure between the suspension and said membrane to enhance passage of said first type of particle through said pores, while substantially inhibiting passage of said second type of particle through said pores.

17. The apparatus of claim 15 including means for varying the time of contact between the suspension and said membrane to enhance passage of said first type of particle through said pores, while substantially inhibiting passage of said second type of particle through said pores.

18. The apparatus of claim 17 in which the time of contact between the suspension and said membrane is limited to that sufficient to allow passage of said first type of particle through said pores and insufficient to allow deformation of said second type of particle for passage through said pores.

20. The apparatus of claim 15 or 19 further comprising means for removing said second type of particle from said filter membrane to prevent clogging of said pores.

21. The apparatus of claim 20 further including means for providing relative movement between said suspension and said membrane.

22. The apparatus of claim 21 wherein said membrane pores have major and minor axes and the major axes of said pores are oriented similarly on said membrane so that the membrane is alignable.

23. The apparatus of claim 22 in which said first and second particles are red blood cells and white blood cells, respectively, said pores are substantially rectangularly shaped, having a width of approximately 1.0 to 3.5 microns and a length of approximately 6 to 14 microns, and said membrane is disposed with said length of said pores being generally aligned with the direction of relative movement.

24. The apparatus of claim 22 in which said first and second particles are red blood cells and white blood cells, respectively, said pores are substantially rectangularly shaped, having a width of approximately 1.0 to 3.5 microns and a length of approximately 6 to 14 microns, and said membrane is disposed with said length of said pores being generally aligned generally normal to the direction of relative movement.

25. The apparatus of claim 21 in which said relative movement is generally parallel to the major axes of said membrane pores.

26. The apparatus of claim 21 in which said relative movement is generally perpendicular to the major axes of said membrane pores.

27. The apparatus of claim 21 including means for varying the contact pressure between the suspension and said membrane so that the contact pressure between the suspension and said membrane can be increased for a time sufficient to allow passage of said first type of particle through said pores and insufficient to allow deformation of said type of particle for passage through said pores.

28. The apparatus of claim 15 or 19 in which said first and second particles are red blood cells and white blood cells, respectively, and said pores are substantially rectangularly shaped, having a width of approximately 1.0 to 3.5 microns and a length of approximately 6 to 14 microns.

29. The apparatus of claim 15 or 19 in which said first type of particle has length and width dimensions greater than in thickness, further comprising means for providing relative movement between said suspension and said pores, and said pores having a length and width corresponding to the length and thickness of said first type of particle, said length being aligned with the direction of relative movement.

30. The apparatus of claim 15 or 19 in which said first type of particle has length and width dimensions greater than in thickness, further comprising means for providing relative movement between said suspension and said pores, and said pores having a length and width corresponding to the length and thickness of said first type of particle, said length being aligned generally normal to the direction of relative movement.

31. The apparatus of claim 15 or 19 wherein at least a portion of the filter membrane defines a curvilinear surface.

19. An apparatus for separating a suspension comprising at least first and second types of particles of different shape, said first type of particle being deformable at a relatively lower force than said second type of particle, said apparatus comprising:

a filter membrane having pores with substantially precisely dimensioned shapes and sizes, said pore shapes and sizes being dimensioned to correspond substantially to the shape of said first particle to allow passage of said first type of particle and to block passage of said second type of particle; and

means for contacting the suspension and said membrane with a force sufficient to allow any required deformation of said first type of particle for passage through said pores and insufficient to allow deformation of said second type of particle for passage through said pores so as to allow passage of said first type of particle through said pores and to block passage of said second type of particle through said pores.

32. The apparatus of claim 19 including means for varying the contact time between the suspension and said membrane to enhance passage of said first type of particle through said pores, while substantially inhibiting passage of said second type of particle through said pores.