Hollow fiber plasmapheresis process

• US 4,668,399 A
• Filed: 12/16/1982
• Issued: 05/26/1987
• Est. Priority Date: 02/16/1982
• Status: Expired due to Fees

• Current Assignee: E. I. du Pont de Nemours and Company (Corteva, Inc.)
• Original Assignee: E. I. du Pont de Nemours and Company (Corteva, Inc.)
• Inventors: Duggins, Ray B.
• Primary Examiner(s): Sadowski, David
• Application Number:
  US06/450,221
• Time in Patent Office: 1,622 Days
• Field of Search: 210/636, 210/637, 210/649, 210/650, 210/651, 210/654
• US Class Current: 210/637
• 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 1/3496 Plasmapheresis; Leucopheresis; Lymphopheresis A61M1/3472 takes precedence
• CPC Class Codes: A61M 1/3603 in the same direction
• CPC Class Codes: A61M 1/3604 in opposite directions
• CPC Class Codes: A61M 1/3623 Means for actively controlling temperature of blood
• CPC Class Codes: A61M 2205/3306 Optical measuring means
• CPC Class Codes: A61M 2205/3331 Pressure; Flow
• CPC Class Codes: A61M 2205/3334 Measuring or controlling the flow rate
• CPC Class Codes: A61M 60/109 incorporated within extracorporeal blood circuits or systems
• CPC Class Codes: A61M 60/113 in other functional devices, e.g. dialysers or heart-lung machines
• CPC Class Codes: A61M 60/279 Peristaltic pumps, e.g. roller pumps
• CPC Class Codes: A61M 60/37 Haemodialysis, haemofiltration or diafiltration
• CPC Class Codes: A61M 60/438 the force acting on the blood contacting member being mechanical
• CPC Class Codes: A61M 60/853 the valve being formed by a flexible tube element which is clamped for restricting the flow
• CPC Class Codes: B01D 2321/2066 Pulsated flow
• CPC Class Codes: B01D 2321/2083 By reversing the flow
• CPC Class Codes: B01D 61/147 Microfiltration
• CPC Class Codes: B01D 63/02 Hollow fibre modules
• CPC Class Codes: B01D 65/08 Prevention of membrane fouling or of concentration polarisation

Abstract

Hollow fiber plasmapheresis module and process, said module comprising hollow fibers having cell-retaining pores and an effective length (L) to lumen diameter (D) ratio L/D not greater than 16,400 cm^-1 D (L and D being in centimeters) within a housing having a blood inlet for conducting blood to the fibers, an outlet for conducting exit (plasma-depleted) blood from the fibers, and a plasma outlet for conducting plasma out of the module.

Claims

1. Improved method for plasmapheresis carried out in a system with a bundle consisting of a plurality of blood wettable porous membrane hollow fibers all of which are in parallel bundle alignment and have a substantially uniform membrane pore diameter and open inlet ends and open outlet ends, each fiber having a lumen diameter (D) no greater than 0.050 cm, the pore diameter being within the range 0.1 to 1.0 μ

m, comprising;

(a) conducting blood in a forward direction into and through the fibers while maintaining a mean positive transmembrane pressure difference across the membranes from inlets to outlets of the hollow fibers;

(b) terminating the forward conducting of blood;

(c) conducting blood through the hollow fibers in the reverse direction;

(d) collecting plasma-depleted blood from the outlets of the hollow fibers;

(e) collecting plasma which has passed through the pores of the membranes; and

(f) repeating in sequence steps (a), (b) and (c) to collect additional plasma-depleted blood and plasma, the effective length, that is, the portion of each fiber, between the ends, through which plasma passes, of the hollow fibers being such that the L/D ratio is no greater than 16,400 cm^-1 D (L and D being in centimeters) and the velocity of the blood in step (a) being such that the shear rate is 200 to 2500 sec^-1, the improved method providing a plasma flux of at least 0.042 mL/min/cm² and an outlet plasma-depleted blood hematocrit of at least 65%.

2. Method of claim 1 wherein the lumen diameter (D) is 0.015 to 0.050 cm and the pore size of the porous membrane is within the range 0.4 to 0.6 μ

m.

3. Method of claim 2 wherein the shear rate is 1000 to 2500 sec^-1.

4. Method of claim 2 wherein the L/D ratio is not greater than about 540.

5. Method of claim 2 wherein the L/D ratio is about 100 to about 350.

6. Method of claim 1 wherein the fibers are blood wettable polypropylene fibers.

7. Method of claim 1 which includes as an additional feature:

conducting blood in an external circuit from a region near the inlets or outlets of the fibers to a region near, respectively, the outlets or inlets of the fibers.

8. Method of claim 1 wherein the volume of blood conducted in step (a) is different from the volume of blood conducted in step (c).

9. Method of claim 8 wherein the volume of blood conducted in step (a) is greater than the volume of blood conducted in step (c).

10. Method of claim 1 wherein the volume of blood conducted in either step (a) or step (c) is at least 5% of the total volume of blood in the system.

11. Method of claim 1 wherein the transmembrane pressure difference across part of the membrane hollow fibers is negative for part of the distance that the blood is conducted across the membrane hollow fibers.

12. Method of claim 11 wherein the arithmetic product of:

(a) the time-average of the transmembrane pressure while it is positive in a portion of the membrane hollow fibers and (b) the time in that portion of the membrane hollow fiber, is numerically greater, indenpendently of sign, than such product when the transmembrane pressure is negative.