Hollow fiber cell propagation system and method

• US 5,126,238 A
• Filed: 02/15/1990
• Issued: 06/30/1992
• Est. Priority Date: 02/15/1990
• Status: Expired due to Fees

• Current Assignee: Unisyn Fibetec Corporation
• Original Assignee: Unisyn Fibertec Corporation
• Inventors: Veeramallu, Uday K., Gebhard, Timothy C.
• Primary Examiner(s): Warden, Robert J.
• Assistant Examiner(s): Beisner, William H.
• Application Number:
  US07/480,533
• Time in Patent Office: 866 Days
• Field of Search: 435/288, 435/813, 435/289, 435/290, 435/291, 435/313, 435/807, 435/284, 435/285, 435/311, 435/240.1, 435/240.2, 435/3, 435/240.242, 435/240.241, 435/41 , 435/240.23, 435/240.25, 422/82.04, 204/400, 204/409, 204/424
• US Class Current: 435/3
• CPC Class Codes: C12M 25/10 Hollow fibers or tubes hollow fiber modules in general B01D63/02
• CPC Class Codes: C12M 29/02 Percolation
• CPC Class Codes: C12M 41/32 of substances in solution
• CPC Class Codes: C12M 41/48 Automatic or computerized control automatic analysis G01N35/00
• CPC Class Codes: Y10S 435/807 Gas detection apparatus

Abstract

A unique hollow fiber bioreactor system and method for the propagation of cells and the production of various cell propagation products is described. The system and method include the use of a flow block holder which allows a dissolved oxygen probe to be calibrated at the same pressure as the media in the bioreactor system.

Claims

1. A hollow fiber cell propagation system comprising:

(i) a hollow fiber bioreactor including nutrient permeable hollow fibers positioned in an extracapillary space;

(ii) a first loop connected to a first inlet and a first outlet of said bioreactor so as to provide and change flow of fluids through lumens of said fibers, said first loop comprising;

(a) pump means for circulating fluids through said first loop;

(b) means for introducing gases into said first loop;

(c) means for determining and changing the temperature of the fluids in said first loop;

(d) means for determining the dissolved oxygen content of said fluids in said first loop upstream or downstream of said bioreactor, said dissolved oxygen determining means being positioned in flow block means with a sensing portion of said dissolved oxygen determining means positioned in said flow block means so as to be in contact with fluid flowing in said first loop, said flow block means including sterile filter means for passing calibrating gas into said flow block means so as to be in contact with said sensing portion for calibrating said dissolved oxygen determining means at a pressure equal to that of the fluid flowing in said first loop;

(e) means for determining and changing the flow rate of said fluids through said first loop;

(f) means for determining and changing pH of said fluids in said first loop;

(g) means for introducing fluids comprising reagents and basal medium containing nutrient into said first loop; and

(iii) a second loop connected to a second inlet and a second outlet of said bioreactor so as to provide and change flow of fluids through said extracapillary space.

2. A hollow fiber cell propagation system as defined by claim 1 in which said means for introducing fluids provides for introduction of said basal medium and reagents into said first loop at a rate determined by a preselected nutrient utilization rate in said bioreactor.

3. A hollow fiber cell propagation system as defined by claim 1 in which said second loop (iii) comprises means for simultaneous introduction of fluids into and removal of product from said extracapillary space at determined rates.

4. A hollow fiber cell propagation system as defined by claim 1 in which said nutrient permeable hollow fibers are formed of a synthetic polymer.

5. A hollow fiber cell propagation system as defined by claim 4 in which said synthetic polymer is formed from a polymethylmethacrylate, a polysulfone or a cellulose derivative.

6. A hollow fiber cell propagation system as defined by claim 1 in which said means (ii)(c) for determining and changing the temperature of said fluids comprises a resistance temperature probe positioned in a resistance temperature probe flow block means that is included as a portion of said first loop, said resistance temperature probe being connected to an electronic monitor and controller, said controller including means to compare the signal from said resistance temperature probe with a preselected set point.

7. A hollow fiber cell propagation system as defined by claim 1 in which said means (ii)(c) for determining and changing the temperature of said fluids comprises a resistance heated conduit as a portion of said first loop through which said fluids flow.

8. A hollow fiber cell propagation system as defined by claim 1 in which said means (ii)(c) for determining and changing the temperature of said fluids comprises an etched foil resistance heating element as a portion of said first loop.

9. A hollow fiber cell propagation system as defined by claim 1 in which said means for determining the dissolved oxygen content of said fluids determines the dissolved oxygen content both upstream and downstream of said bioreactor.

10. A hollow fiber cell propagation system as defined by claim 9 further comprising means for determining the difference between the dissolved oxygen content of said fluids upstream and downstream of said bioreactor.

11. A hollow fiber cell propagation system as defined by claim 9 further comprising means for determining the difference between the dissolved oxygen content of said fluids upstream and downstream of said bioreactor and for utilizing said difference to determine the aerobic efficiency and provide a real time verification and measurement of cell metabolism in said bioreactor.

12. A hollow fiber cell propagation system as defined by claim 11 further comprising means for utilizing the difference in the dissolved oxygen content of said fluids upstream and downstream of said bioreactor to assess the performance of said bioreactor.

13. A hollow fiber cell propagation system as defined by claim 1 further including a programmable controller means constructed and arranged so as to control said means (ii) (e) for determining and changing the flow rate of said fluids through said first loop.

14. A hollow fiber cell propagation system as defined by claim 13 in which said programmable controller means receiving data provided by nutrient and ammonia analyzers using fluid from said first loop controls introduction of basal medium into said first loop.

15. A hollow fiber cell propagation system as defined by claim 1 in which said means ii(b) for introducing gases into said first loop further comprises an oxygenator means for introducing gases into basal medium after oxygen depletion due to passage through said bioreactor.

16. A hollow fiber cell propagation system as defined by claim 15 in which said oxygenator means includes means for blending air, nitrogen and carbon dioxide prior to introduction into the basal medium.

17. A hollow fiber cell propagation system as defined by claim 15 in which said oxygenator means comprises a plurality of semipermeable hollow fibers membranes capable of passing gas to the basal medium.

18. A hollow fiber cell propagation system as defined by claim 1 further comprising a waste disposal means for automatically displacing from said first loop a volume substantially identical to the volume of fresh basal medium introduced into said first loop.

19. A hollow fiber cell propagation system as defined by claim 1 in which said means (ii) (d) for determining and changing the dissolved oxygen content of said fluids comprises said flow block means further including a window in a wall of said flow block means through which said sensing portion of said dissolved oxygen determining probe may be observed.

20. A hollow fiber cell propagation system as defined by claim 9 further comprising means for determining the value of the expression GUR/Δ

DO where GUR means glucose utilization rate and Δ

DO means dissolved oxygen differential.

21. A hollow fiber cell propagation system defined by claim 20 further comprising means for using said GUR/Δ

DO value to determine aerobic efficiency of said system.

22. A hollow fiber cell propagation system as defined by claim 11 or claim 20 further comprising means for utilizing the difference in dissolved oxygen content upstream and downstream of said bioreactor to assess the efficiency of cell production by said bioreactor.

23. A hollow fiber cell propagation system as defined by claim 1 in which said means (ii)(b) for introducing gases comprises oxygenator means having a plurality of permeable hollow fibers positioned in an extracapillary space for passing oxygen depleted fluid in said first loop through the lumens of said hollow fibers and means for passing air, oxygen and nitrogen or a blend thereof into and through said extracapillary space for introduction into said oxygen depleted fluid in the lumens of said hollow fibers.

24. A hollow fiber cell propagation system as defined by claim 23 further comprising means for controlling the oxygen content of said fluid in said first loop.

25. A hollow fiber cell propagation system as defined by claim 23 or claim 24 further comprising means for controlling the amount of air, carbon dioxide and nitrogen introduced into said fluid in said first loop passing through the lumens of said hollow fibers of said oxygenator and thereby regulate the pH and oxygen content of said fluid upon exit from said oxygenator.

26. A hollow fiber cell propagation system as defined by claim 23 further comprising a waste disposal system in line with said oxygenator means, said waste disposal system including valve means to preclude siphoning of waste fluid back into said first loop.

27. A hollow fiber cell propagation system as defined by claim 1 further comprising a programmable controller means to control said means (ii)(g) for introducing fluids into said first loop, and for changing flow in said second loop.

28. A process for the conversion of a raw material to a useful product by cell metabolism which comprises

(i) inoculating the extracapillary space of a hollow fiber bioreactor with cells and a growth factor mixture for said cells;

(ii) circulating basal medium comprising a nutrient into and through the lumens of the hollow fibers of said bioreactor;

(iii) measuring dissolving oxygen content of said circulating basal medium before and after passage through said bioreactor with dissolved oxygen content determining means while said circulating basal medium is in a fluid flow loop including said lumens of said hollow fibers of said bioreactor;

(iv) calibrating said dissolved oxygen determining means while said dissolving oxygen determining means is positioned in flow block means with a sensing portion of said dissolved oxygen determining means positioned in said flow block means so as to be in contact with fluid flowing in said fluid flow loop when said dissolved oxygen determining means is not being calibrated, passing calibrating gas into said flow block means so as to be in contact with said sensing portion for calibrating said dissolved oxygen determining means at a pressure equal to that of fluid flowing in said fluid flow loop;

(v) introducing oxygen into said circulating basal medium to establish and maintain an oxygen content sufficient to support aerobic metabolism of said cells;

(vi) utilizing the differential in dissolved oxygen content of the circulating basal medium before and after passage through the lumens of the hollow fibers of said bioreactor to determine aerobic efficiency and provide a real time verification and measurement of cell metabolism in said bioreactor.

29. A process as defined by claim 28 in which oxygen is introduced into said circulating basal medium in step (iii) by passage of said circulating basal medium through the lumens of a hollow fiber oxygenator in which gases containing oxygen are present in the extracapillary space surrounding said hollow fibers of said oxygenator.

30. A process as defined by claim 28 further comprising simultaneously introducing said growth factor into and removing product from said extracapillary space of said hollow fiber bioreactor at rates which do not differ by more than about five percent.

31. A process as defined by claim 28 in which said nutrient is maintained at a level of not more than about one millimolar in said bioreactor.

32. A process as defined by claim 28 in which said nutrient is glucose.

33. A process as defined by claim 28 in which said conversion is accomplished by mammalian, insect, avian, plant or fungal cells.

34. A process is defined by claim 28 in which said conversion is accomplished by anchorage dependent cells.

35. A process as defined by claim 28 in which said conversion in accomplished by suspension cells.

36. A process as defined by claim 28 in which said conversion is accomplished by cells which yield a viral protein.

37. A process as defined by claim 35 in which said conversion is accomplished by a hybridoma.

38. A process as defined by claim 28 in which the rate of circulation of said basal medium into and through the lumens of said hollow fibers in said bioreactor is controlled to provide a predetermined bioreactor nutrient utilization rate.

39. A process as defined by claim 28 in which said nutrient is glucose and in which the concentration of said glucose is maintained at a level of not more than about one millimolar in said bioreactor.

40. A process as defined by claim 28 in which the adverse effects of product and metabolite feedback inhibition are ameliorated by control of rate at which (i) fluids are introduced into said extracapillary space or (ii) product is removed from said extracapillary space.

41. A process as defined by claim 28 in which the temperature in said bioreactor is maintained at about 37°

C.

42. A process as defined by claim 28 in which samples from said circulating basal medium are subjected to ammonia and nutrient analyses and the data from such analyses is used to determine a rate of introduction of basal medium.

43. A process as defined by claim 42 in which said nutrient is glucose and said data is used to determine the rate of introduction of basal medium required to provide a preselected glucose utilization rate.

44. A process as defined by claim 42 in which said conversion is accomplished by an anchorage dependent or suspended mammalian cells.

45. A hollow fiber process for the conversion of a raw material by cell metabolism which comprises

(i) inoculating the extracapillary space of a hollow fiber bioreactor with cells and a growth factor for said cells;

(ii) passing basal medium and nutrients from a storage vessel into and through the lumens of said hollow fibers;

(a) the rate of passage of said medium and reagents through said lumens being controlled to provide a preselected bioreactor glucose utilization rate;

(iii) measuring dissolved oxygen content of said circulating basal medium before and after passage through said bioreactor with dissolved oxygen content determining means while said circulating basal medium is in a fluid flow loop including said lumens of said hollow fibers of said bioreactor, said dissolved oxygen content determining means including means for calibrating said dissolved oxygen content determining means at the same pressure as fluid flowing in said fluid flow loop;

(iv) calibrating said dissolved oxygen determining means while said dissolved oxygen determining means is positioned in flow block means with a sensing portion of said dissolved oxygen determining means positioned in said flow block means so as to be in contact with fluid flowing in said fluid flow loop when said dissolved oxygen determining means is not being calibrated, passing calibrating gas into said flow block means so as to be in contact with said sensing portion for calibrating said dissolved oxygen determining means at a pressure equal to that of fluid flowing in said fluid flow loop;

(v) introducing oxygen into said basal medium and nutrients in a predetermined amount sufficient to support aerobic metabolism of said cells;

(vi) determining the differential in the dissolved oxygen content of said basal medium and nutrients upstream and downstream of said bioreactor;

(vii) utilizing said dissolved oxygen differential to determine the aerobic efficiency of the cell metabolism in the bioreactor and to provide a real time verification and measurement of said cell metabolism; and

(viii) simultaneously introducing growth factor into and removing product from said extracapillary space at rates which do not differ by more than about 5%.

46. A process as defined by claim 45 in which said conversion is accomplished by mammalian cells and in which the basal medium comprises glucose.

47. A process as defined by claim 46 in which said mammalian cells are anchorage dependent.

48. A process as defined by claim 46 in which said mammalian cells are suspended.

49. A process for conversion of a raw material into a useful product by cell metabolism which comprises:

(i) inoculating the extracapillary space of a hollow fiber bioreactor with cells and a growth factor for said cells;

(ii) circulating basal medium comprising a nutrient into and through the lumens of the hollow fibers of said bioreactor;

(iii) measuring dissolved oxygen content of said circulating basal medium before and after passage through said bioreactor with dissolved oxygen content determining means while said lumens of said hollow fibers of said bioreactor;

(iv) calibrating said dissolved oxygen determining means while said dissolved oxygen determining means is positioned in flow block means with a sensing portion of said dissolved oxygen determining means positioned in said flow block means so as to be in contact with fluid flowing in said fluid flow loop when said dissolved oxygen determining means is not being calibrated, passing calibrating gas into said flow block means so as to be in contact with said sensing portion for calibrating said dissolved oxygen determining means at a pressure equal to that of fluid flowing in said fluid flow loop;

(v) introducing oxygen into said circulating basal medium to establish and maintain an oxygen content sufficient to support aerobic metabolism of said cells; and

(vi) simultaneously measuring the glucose utilization rate (GUR) of said bioreactor and the dissolved oxygen (Δ

DO) differential across said bioreactor and using the GUR/Δ

DO ratio to assess the bioreactor cell production efficiency of said bioreactor.

50. A process as defined by claim 49 in which said GUR/Δ

DO ratio is maintained at 3 to 6 milligrams per hour.

51. A process as defined by claim 49 in which steps (ii) and (iii) are conducted in response to a programmable controller.

52. A process as defined by claim 50 in which feedback inhibition is precluded by a programmable controller.

53. A process for the conversion of a raw material into a useful product by cell metabolism which comprises:

(i) inoculating the extracapillary space of a hollow fiber bioreactor with cells and a growth factor for said cells;

(ii) introducing a glucose free basal medium into a means for circulating fluids through the lumens of the hollow fibers of said bioreactor;

(iii) separately introducing glucose into said means for circulating fluids through the lumens of said hollow fibers of said bioreactor;

(iv) measuring dissolved oxygen content of said circulating basal medium before and after passage through said bioreactor with dissolved oxygen content determining means while said circulating basal medium is in a fluid flow loop including said lumens of said hollow fibers of said bioreactor;

(v) calibrating said dissolved oxygen determining means while said dissolved oxygen determining means is positioned in flow block means with a sensing portion of said dissolved oxygen determining means positioned in said flow block means so as to be in contact with fluid flowing in said fluid flow loop when said dissolved oxygen determining means is not being calibrated, passing calibrating gas into said flow block means so as to be in contact with said sensing portion for calibrating said dissolved oxygen determining means at a pressure equal to that of fluid flowing in said fluid flow loop;

(vi) introducing oxygen into said circulating basal medium to establish and maintain an oxygen content sufficient to support aerobic metabolism of said cells; and

(vii) simultaneously measuring the glucose utilization rate (GUR) of said bioreactor and the dissolved oxygen (Δ

DO) differential across said bioreactor and using the GUR/Δ

DO ratio to assess the bioreactor cell production efficiency of said bioreactor.

54. A process as defined by claim 53 further comprising:

(viii) monitoring and controlling one or more of steps (i) through (vii) with a programmable controller.

55. A hollow fiber process for the conversion of raw material by cell metabolism which comprises

(i) inoculating the extracapillary space of a hollow fiber bioreactor will cells and a growth factor for said cells;

(ii) passing basal medium and nutrients from a storage vessel into and through the lumens of said hollow fibers;

(a) the rate of passage of said medium and reagents through said lumens being controlled to provide a selected bioreactor glucose utilization rate;

(iii) measuring dissolved oxygen content of said circulating basal medium before and after passage through said bioreactor with dissolved oxygen content determining means while said circulating basal medium is in a fluid flow loop including said lumens of said hollow fibers of said bioreactor;

(iv) calibrating said dissolved oxygen determining means while said dissolved oxygen determining means is positioned in flow block means with a sensing portion of said dissolved oxygen determining means positioned in said flow block means so as to be in contact with fluid flowing in said fluid flow loop when said dissolved oxygen determining means is not being calibrated, passing calibrating gas into said flow block means so as to be in contact with said sensing portion for calibrating said dissolved oxygen determining means at a pressure equal to that of fluid flowing in said fluid flow loop;

(v) introducing oxygen into said basal medium and nutrients in a predetermined amount sufficient to support aerobic metabolism of said cells;

(vi) simultaneously measuring the glucose utilization rate (GUR) of said bioreactor and the dissolved oxygen (Δ

DO) differential across said bioreactor and using the GUR/Δ

DO ratio to assess the bioreactor cell production efficiency of said bioreactor; and

(vii) monitoring and controlling one or more of steps (i) through (vi) with a programmable controller.