Microfermentors for rapid screening and analysis of biochemical processes

• US 20040077075A1
• Filed: 05/01/2003
• Published: 04/22/2004
• Est. Priority Date: 05/01/2002
• Status: Abandoned Application

• Current Assignee: Massachusetts Institute of Technology
• Original Assignee: Massachusetts Institute of Technology
• Inventors: Jensen, Klavs F., Schmidt, Martin A., Laibinis, Paul, Sinskey, Anthony J., Zanzotto, Andrea, Ram, Rajeev J., Szita, Nicolas
• Application Number:
  US10/427,373
• Publication Number:
  US 20040077075A1
• Time in Patent Office: Days
• US Class Current: 435/297.2
• CPC Class Codes: B01J 2219/00283 Reactor vessels with top opening
• CPC Class Codes: B01J 2219/00317 Microwell devices, i.e. having large numbers of wells
• CPC Class Codes: B01J 2219/00479 Means for mixing reactants or products in the reaction vessels
• CPC Class Codes: B01J 2219/00481 by the use of moving stirrers within the reaction vessels
• CPC Class Codes: B01J 2219/00484 by shaking, vibrating or oscillating of the reaction vessels
• CPC Class Codes: B01J 2219/00495 Means for heating or cooling the reaction vessels
• CPC Class Codes: B01J 2219/00585 Parallel processes
• CPC Class Codes: B01J 2219/00599 Solution-phase processes
• CPC Class Codes: B01J 2219/00691 using robots
• CPC Class Codes: B01J 2219/00743 Cells
• CPC Class Codes: B01L 2200/027 for microfluidic devices
• CPC Class Codes: B01L 2200/10 Integrating sample preparation and analysis in single entity, e.g. lab-on-a-chip concept
• CPC Class Codes: B01L 2300/0816 Cards, e.g. flat sample carriers usually with flow in two horizontal directions
• CPC Class Codes: B01L 2300/0822 Slides
• CPC Class Codes: B01L 2300/0867 Multiple inlets and one sample wells, e.g. mixing, dilution
• CPC Class Codes: B01L 2300/10 Means to control humidity and/or other gases
• CPC Class Codes: B01L 3/5027 by integrated microfluidic structures, i.e. dimensions of channels and chambers are such that surface tension forces are important, e.g. lab-on-a-chip B01L3/5023 takes precedence; micromixers B01F33/30; microreactors for synthesis B01J19/0093; microcapillary devices in general B81B1/00
• CPC Class Codes: C12M 23/16 Microfluidic devices; Capillary tubes integrated microfluidic structures B01L3/5027; microreactors B01J19/0093
• CPC Class Codes: C12M 23/58 Reaction vessels connected in series or in parallel combinations of bioreactors with other apparatus, C12M43/00
• CPC Class Codes: C12M 29/04 Filters; Permeable or porous membranes or plates, e.g. dialysis
• CPC Class Codes: C12M 29/10 : Perfusion
• CPC Class Codes: G01N 2021/6484 : Optical fibres
• CPC Class Codes: G01N 2021/7783 : Transmission, loss
• CPC Class Codes: G01N 2021/7786 : Fluorescence
• CPC Class Codes: G01N 21/31 : Investigating relative effect of material at wavelengths characteristic of specific elements or molecules, e.g. atomic absorption spectrometry G01N21/72 takes precedence
• CPC Class Codes: G01N 21/6408 : with measurement of decay time, time resolved fluorescence
• CPC Class Codes: G01N 21/6428 : Measuring fluorescence of fluorescent products of reactions or of fluorochrome labelled reactive substances, e.g. measuring quenching effects, using measuring "optrodes" in vivo A61B5/00; immunoassay G01N33/53
• CPC Class Codes: G01N 21/6452 : Individual samples arranged in a regular 2D-array, e.g. multiwell plates
• CPC Class Codes: G01N 21/648 : using evanescent coupling or surface plasmon coupling for the excitation of fluorescence
• CPC Class Codes: G01N 21/7703 : using reagent-clad optical fibres or optical waveguides using measurement of total internal reflection or attenuated total reflection G01N21/552; optical fibres or waveguides per se G02B
• CPC Class Codes: G01N 35/0099 : comprising robots or similar manipulators robots per se B25J

Abstract

The present invention provides a variety of microscale bioreactors (microfermentors) and microscale bioreactor arrays for use in culturing cells. The microfermentors include a vessel for culturing cells and means for providing oxygen to the interior of the vessel at a concentration sufficient to support cell growth, e.g., growth of bacterial cells. Depending on the embodiment, the microfermentor vessel may have various interior volumes less than approximately 1 ml. The microfermentors may include an aeration membrane and optionally a variety of sensing devices. The invention further provides a chamber to contain the microfermentors and microfermentor arrays and to provide environmental control. Certain of the microfermentors include a second chamber that may be used, e.g., to provide oxygen, nutrients, pH control, etc., to the culture vessel and/or to remove metabolites, etc. Various methods of using the microfermentors, e.g., to select optimum cell strains or bioprocess parameters are provided.

Claims

1. A microscale bioreactor comprising:

a vessel having an interior volume of less than 200 microliters; and

means for providing oxygen to the vessel at a concentration sufficient to support cell growth.

2. The microscale bioreactor of claim 1, further comprising at least one channel extending from and in communication with the vessel.

3. The microscale bioreactor of claim 2, further comprising:

means for introducing a component into the vessel or removing a sample from the vessel via a channel.

4. The microscale bioreactor of claim 1, wherein the interior volume is between approximately 100 and 200 microliters, inclusive.

5. The microscale bioreactor of claim 1, wherein the interior volume is between approximately 50 and 100 microliters, inclusive.

6. The microscale bioreactor of claim 1, wherein the interior volume is between approximately 5 and 50 microliters, inclusive.

7. The microscale bioreactor of claim 1, wherein the interior volume is approximately 5 microliters.

8. The microscale bioreactor of claim 1, wherein the means for providing oxygen is integrated into a vessel wall.

9. The microscale bioreactor of claim 1, wherein the means for providing oxygen forms a structural component of the bioreactor.

10. The microscale bioreactor of claim 1, wherein the means for providing oxygen comprises an aeration membrane, and wherein oxygen diffuses through the membrane into the vessel.

11. The microscale bioreactor of claim 10, wherein the membrane comprises a material selected from the group consisting of fluoropolymers and silicones.

12. The microscale bioreactor of claim 10, wherein the membrane comprises polydimethylsiloxane or Teflon AF 2400.

13. The microscale bioreactor of claim 10, wherein the membrane has a permeability of approximately 800 Barrer.

14. The microscale bioreactor of claim 10, wherein the membrane has a permeability of between approximately 600 and approximately 800 Barrer.

15. The microscale bioreactor of claim 10, wherein the membrane has a permeability of between approximately 400 and approximately 600 Barrer.

16. The microscale bioreactor of claim 10, wherein the membrane has a permeability of between approximately 200 and approximately 400 Barrer.

17. The microscale bioreactor of claim 10, wherein the membrane has a permeability of between approximately 80 and approximately 200 Barrer.

18. The microscale bioreactor of claim 10, wherein the membrane is biocompatible.

19. The microscale bioreactor of claim 10, wherein the membrane is optically transparent.

20. The microscale bioreactor of claim 1, wherein the bioreactor supports cell growth for a period of at least approximately 6 hours.

21. The microscale bioreactor of claim 1, wherein the bioreactor supports cell growth for a period of at least approximately 10 hours.

22. The microscale bioreactor of claim 1, wherein the bioreactor supports exponential cell growth for a period of at least approximately 2.5 hours.

23. The microscale bioreactor of claim 1, wherein the bioreactor supports cell growth that achieves a viable cell density of at least 10⁹ cells per liter.

24. The microscale bioreactor of claim 1, wherein the bioreactor supports cell growth that achieves a viable cell density of at least 10¹⁰ cells per liter.

25. The microscale bioreactor of claim 1, wherein the bioreactor supports cell growth that achieves a viable cell density of at least 10¹¹ cells per liter.

26. The microscale bioreactor of claim 1, wherein the bioreactor supports cell growth that achieves a viable cell density of at least 10¹² cells per liter.

27. The microscale bioreactor of any of claims 20 through 26, wherein the cell growth is bacterial cell growth.

28. The microscale bioreactor of claim 1, wherein at least one interior surface of the vessel or of a channel extending from or in communication with the vessel is coated with a substance that alters adsorption of cells.

29. The microscale bioreactor of claim 28, wherein the substance decreases adsorption of cells.

30. The microscale bioreactor of claim 28, wherein the substance increases adherence of cells.

31. The microscale bioreactor of claim 28 wherein the substance is a silanecontaining film.

32. The microscale bioreactor of claim 28, wherein the surface is modified using a Grignard reagent.

33. The microscale bioreactor of claim 28, wherein the surface is modified using a ring-opening metathesis polymerization reaction to form a film.

34. The microscale bioreactor of claim 28, wherein the substance is a polymer.

35. The microscale bioreactor of claim 34, wherein the polymer is a comb polymer comprising a backbone and a plurality of polymeric side chains attached thereto.

36. The microscale bioreactor of claim 34, wherein the backbone is selected to adsorb to a substrate.

37. The microscale bioreactor of claim 34, wherein the polymeric side chains are selected to retard adsorption of proteins, cells, or both.

38. The microscale bioreactor of claim 34, wherein the polymer comprises a poly(acrylic acid) backbone.

39. The microscale bioreactor of claim 34, wherein the polymer comprises poly(ethylene glycol).

40. The microscale bioreactor of claim 1, further comprising:

means for quantification of biomass within the vessel.

41. The microscale bioreactor of claim 40, wherein the means for quantification of biomass comprises optical detection means.

42. The microscale bioreactor of claim 40, wherein the means for quantification of biomass includes a light source and an optical fiber.

43. The microscale bioreactor of claim 1 or claim 40, further comprising:

means for measuring dissolved oxygen within the vessel.

44. The microscale bioreactor of claim 43, wherein the means for measuring dissolved oxygen comprises an optical sensor.

45. The microscale bioreactor of claim 44, wherein the optical sensor comprises a compound whose fluorescence or luminescence varies depending on oxygen concentration.

46. The microscale bioreactor of claim 45, wherein the compound is a ruthenium compound.

47. The microscale bioreactor of claim 45, wherein the compound is Ruthenium II tris(4,7-diphenyl-1,1-phenanthroline)²⁺.

48. The microscale bioreactor of claim 1, further comprising:

means for quantification of biomass within the vessel;

means for measuring dissolved oxygen within the vessel; and

means for measuring at least one other parameter within the vessel.

49. The microscale bioreactor of claim 48, wherein the at least one other parameter is selected from the group consisting of:

temperature, pH, carbon dioxide concentration, carbon source concentration, concentration of an ionic species, and concentration of a cellular metabolite.

50. The microscale bioreactor of claim 49, wherein the at least one other parameter is pH.

51. The microscale bioreactor of claim 48, wherein at least one of the means comprises an optical chemical sensor.

52. The microscale bioreactor of claim 1, further comprising:

at least one waveguide sensor.

53. The microscale bioreactor of claim 1, further comprising a self-assembling sensor.

54. The microscale bioreactor of claim 53, wherein the self-assembling sensor comprises an electroactive thiol reagent.

55. The microscale bioreactor of claim 1, further comprising:

means for controlling the temperature within the vessel.

56. The microscale bioreactor of claim 55, wherein the means for controlling the temperature within the vessel comprises a resistance heater.

57. The microscale bioreactor of claim 1, further comprising:

means for controlling the pH of medium within the vessel.

58. The microscale bioreactor of claim 1, further comprising:

means for delivering nutrients to the vessel.

62. A bioreactor system comprising:

the microscale bioreactor of claim 1;

and

a chamber sufficiently large to accommodate the microscale bioreactor, wherein the chamber provides means to control at least one environmental parameter.

63. The microscale bioreactor system of claim 62, wherein the chamber controls either temperature or humidity or both experienced by the microscale bioreactor.

64. The microscale bioreactor system of claim 62, further comprising an optical excitation source positioned so as to direct optical excitation into the bioreactor and an optical detection means positioned so as to sense light transmitted by or emitted from the bioreactor.

65. The microscale bioreactor of claim 64, wherein the optical detection means comprises a Raman spectrometer.

66. The microscale bioreactor system of claim 64, wherein the optical excitation source, the optical detection means, or both include an optical fiber.

67. A bioreactor assembly for performing multiple fermentations in parallel comprising:

a plurality of microscale bioreactors as described in any of claims 1, 40, 52, or 55.

68. A bioreactor assembly for performing multiple fermentations in parallel comprising:

a plurality of microscale bioreactors as described in claim 43.

69. A microfermenter system comprising:

one or more microscale bioreactors as described in claim 1, or one or more arrays of such microscale bioreactors, optionally with associated microfluidic components, and one or more of the following;

a plate or platform on or in which one more microscale bioreactors or microscale bioreactor arrays, optionally with associated microfluidics, is mounted or housed;

a chamber in which the microfermentors or microfermentor arrays, plates, or platforms are enclosed;

a pump;

sensing means;

detection means;

energy delivery means;

excitation means;

analytical equipment;

robotics;

software; and

computers.

73. A method of selecting a strain that produces a desired product or degrades an unwanted compound comprising steps of:

culturing a plurality of different strains, each in an individual microscale bioreactor as provided in any of claims 1, 40, 52, or 55;

measuring the amount of the desired or unwanted product in each of the microscale bioreactors; and

selecting a strain that produces an optimum amount of a desired product or degrades a maximum amount of the unwanted compound.

74. A method of selecting a bioprocess parameter comprising steps of:

culturing an organism type in a plurality of microscale bioreactors as provided in any of claims 1, 40, 52, or 55, wherein the microscale bioreactors are operated under conditions in which the value of the bioprocess parameter varies and wherein the organism produces a product or degrades a compound;

monitoring biomass in each of the microscale bioreactors; and

identifying the value of the bioprocess parameter that results in optimum biomass, optimum product formation, or optimum compound degradation.

75. The method of claim 74, in which the bioprocess parameter is actively controlled.

76. The method of claim 74, further comprising monitoring at least one bioprocess parameter in addition to biomass.

77. A method of performing a fermentation comprising:

selecting a cell strain in accordance with the method of claim 73;

and

culturing the cell strain in a production scale fermentor.

78. A method of performing a fermentation comprising:

culturing cells in a production scale fermentor, wherein one or more bioprocess parameters for the production scale fermentor is selected according to the method of claim 74.

59. A microscale bioreactor comprising:

at least one waveguide sensor.

60. The microscale bioreactor of claim 59, wherein the waveguide sensor incorporates a photodetector.

61. The microscale bioreactor of claim 60, wherein the photodetector comprises a single-photon avalanche diode.

70. A microscale bioreactor comprising

first vessel having an interior volume of 1 ml or less for culturing cells;

and

a second vessel separated from the first vessel at least in part by a membrane permeable to oxygen and carbon dioxide.

71. The microscale bioreactor of claim 70, wherein the membrane is permeable to cell products and nutrients but not permeable to cells.

72. The microscale bioreactor of claim 70, further comprising:

means for flowing a liquid or gas through the second vessel.