Method for isolation of independent, parallel chemical micro-reactions using a porous filter

• US 20060019264A1
• Filed: 11/23/2004
• Published: 01/26/2006
• Est. Priority Date: 12/01/2003
• Status: Abandoned Application

• Current Assignee: Chun Heen Ho, John Simpson, Ming Lei, Roth C. Thomas, Said Attiya, Vinod B. Makhijani, Yi-Ju Chen
• Original Assignee: Chun Heen Ho, John Simpson, Ming Lei, Roth C. Thomas, Said Attiya, Vinod B. Makhijani, Yi-Ju Chen
• Inventors: Chen, Yi-Ju, Makhijani, Vinod B., Simpson, John, Lei, Ming, Roth, C. Thomas, Ho, Chun Heen, Attiya, Said
• Application Number:
  US11/016,942
• Publication Number:
  US 20060019264A1
• Time in Patent Office: Days
• US Class Current: 435/6
• CPC Class Codes: B01D 2325/38 Hydrophobic membranes
• CPC Class Codes: B01D 61/18 Apparatus therefor
• CPC Class Codes: B01D 69/02 characterised by their properties
• CPC Class Codes: B01D 69/10 Supported membranes; Membrane supports
• CPC Class Codes: B01D 69/1071 Woven, non-woven or net mesh
• CPC Class Codes: B01D 71/56 Polyamides, e.g. polyester-amides
• CPC Class Codes: B01J 19/0046 Sequential or parallel reactions, e.g. for the synthesis of polypeptides or polynucleotides; Apparatus and devices for combinatorial chemistry or for making molecular arrays synthesis methods per se C40B50/00
• CPC Class Codes: B01J 2219/00286 Reactor vessels with top and bottom openings
• CPC Class Codes: B01J 2219/00317 Microwell devices, i.e. having large numbers of wells
• CPC Class Codes: B01J 2219/00414 using suction
• CPC Class Codes: B01J 2219/00423 using filtration, e.g. through porous frits
• CPC Class Codes: B01J 2219/00466 in a slurry
• CPC Class Codes: B01J 2219/005 Beads
• CPC Class Codes: B01J 2219/00576 fluorophore
• CPC Class Codes: B01J 2219/00585 Parallel processes
• CPC Class Codes: B01J 2219/00596 Solid-phase processes
• CPC Class Codes: B01J 2219/00704 integrated with the reactor apparatus
• CPC Class Codes: B01J 2219/00722 Nucleotides
• CPC Class Codes: B01L 2200/16 Reagents, handling or storing thereof
• CPC Class Codes: B01L 2300/0681 Filter
• CPC Class Codes: B01L 2300/0819 : Microarrays; Biochips
• CPC Class Codes: B01L 2300/0829 : Multi-well plates; Microtitration plates
• CPC Class Codes: B01L 2300/0877 : Flow chambers
• CPC Class Codes: B01L 2400/0487 : fluid pressure, pneumatics
• CPC Class Codes: B01L 3/5025 : for parallel transport of multiple samples
• CPC Class Codes: B01L 3/50255 : Multi-well filtration
• CPC Class Codes: B01L 7/52 : with provision for submitting samples to a predetermined sequence of different temperatures, e.g. for treating nucleic acid samples amplification or hybridisation processes per se C12Q1/68; controlling sequential reactions for synthesis B01J19/0046
• CPC Class Codes: C12Q 1/6869 : Methods for sequencing
• CPC Class Codes: C12Q 1/6874 : involving nucleic acid arrays, e.g. sequencing by hybridisation
• CPC Class Codes: C12Q 2535/107 : Maxam and Gilbert method, i.e. sequential release and detection of nucleotides
• CPC Class Codes: C12Q 2565/301 : Pyrophosphate (PPi)
• CPC Class Codes: C12Q 2565/501 : being an array of oligonucleotides
• CPC Class Codes: G01N 21/6452 : Individual samples arranged in a regular 2D-array, e.g. multiwell plates

Abstract

The present invention relates to methods and apparati for conducting densely packed, independent chemical reactions in parallel in a substantially two-dimensional array. Accordingly, this invention also focuses on the use of this array for applications such as DNA sequencing, most preferably pyrosequencing, and DNA amplification.

Claims

1. A membrane reactor array comprising:

a planar array layer comprising a plurality of pores with reagent-carrying beads disposed in a plurality of said pores, with a maximum of one bead per pore, wherein the array is substantially permeable to aqueous solutions but is substantially impermeable to said beads; and

a porous high flow resistance membrane layer, in contact with the planar array layer, that is permeable to nucleic acids and proteins to provide flow resistance of greater than 10 fold that of the flow resistance of the aqueous solutions through a bead-containing pore in said planar array.

2. The membrane reactor array of claim 1 wherein said planar array layer is formed to provide a spacing of pores of less than 100 μ

m center to center.

3. The membrane reactor array of claim 1 wherein said planar array layer is formed to provide a spacing of pores of about 50 to 78 μ

m center to center.

4. The membrane reactor array of claim 1 wherein said planar array layer comprises pores with a pore size length in one dimension of about 15 μ

m to 100 μ

m in diameter.

5. The membrane reactor array of claim 1 wherein said planar array layer comprises pores of a pore size length in one dimension of about 20 to 35 μ

m in diameter.

6. The membrane reactor array of claim 1 wherein said planar array layer comprises substantially square pores with an average size of about 15 to 100 μ

m.

7. The membrane reactor array of claim 1 wherein said planar array layer comprises substantially square pores with an average size of about 20 to 35 μ

m.

8. The membrane reactor array of claim 1 wherein said planar array layer comprises substantially square pores with an average size of about, 25 μ

m, 28 μ

m, 30 μ

m or 31 μ

m.

9. The membrane reactor array of claim 1 wherein said planar array layer comprises pores that are rectangular.

10. The membrane reactor array of claim 1 wherein said planar array layer comprises at least 10,000 pores.

11. The membrane reactor array of claim 1 wherein said planar array layer comprises at least 50,000 pores.

12. The membrane reactor array of claim 1 wherein said planar array layer comprises at least 100,000 pores.

13. The membrane reactor array of claim 1 wherein said planar array layer comprises at least 250,000 pores.

14. The membrane reactor array of claim 1 wherein said high flow resistance membrane has a pore size between 0.01 μ

m and 10 μ

m.

15. The membrane reactor array of claim 1 wherein said high flow resistance membrane has a pore size between 0.01 μ

m and 0.5 μ

m.

16. The membrane reactor array of claim 1 wherein said high flow resistance membrane has a pore size between less than 0.1 μ

m and 1 μ

m.

17. The membrane reactor array of claim 1 wherein said high flow resistance membrane is a hydrophobic membrane with a pore size less than 20 μ

m.

18. The membrane reactor array of claim 1 wherein said high flow resistance membrane has a flow resistance to a liquid that is 100 fold greater than that of the planar array layer.

19. The membrane reactor array of claim 1 wherein said high flow resistance membrane has a pore diameter that is less than 10% of the pore diameter of the planar array layer.

20. The membrane reactor array of claim 1 wherein said high flow resistance membrane has a pore diameter that is less than 1% of the pore diameter of the planar array layer.

21. The membrane reactor array of claim 1 wherein said planar array layer is a woven mesh of a plurality of fibers with pores formed between said fibers.

22. The membrane reactor array of claim 1 wherein said planar array layer is a planar surface comprising pores.

23. The membrane reactor array of claim 1, additionally comprising a porous structural support layer which has less resistance to fluid flow than the planar array or the porous high flow resistance membrane layer.

24. The membrane reactor array of claim 23, wherein said porous structural support layer is made from a material selected from the group consisting of metal, ceramic, and porous silicon.

25. The membrane reactor array of claim 1, further comprising a pyrophosphate degrading enzyme immobilized on one said layer or on said bead.

26. A cartridge comprising a membrane reactor array of claim 1 wherein said membrane reactor array bisects said cartridge into a first and a second chamber, and wherein said cartridge comprise a first opening in said first chamber and a second opening in said second chamber to allow a fluid to flow through said first opening, through said membrane reactor array, and through said second opening.

27. The cartridge of claim 26, further comprising a third opening in said first chamber to allow a fluid to flow through said first opening laterally over said membrane reactor array and through said third opening.

39. A method of identifying a base at a target position in a sample DNA sequence comprising:

providing a sample DNA sequence and an extension primer that hybridizes to the sample DNA immediately adjacent to the target position and subjecting the sample DNA and extension primer to a polymerase reaction in the presence of a deoxynucleotide or deoxynucleotide,

wherein said sample DNA sequence is immobilized on a bead within a membrane reactor array of claim 1;

and

whereby the deoxynucleotide or dideoxynucleotide will only become incorporated and release pyrophosphate (PP_i) if it is complementary to the base in the target position, and any release of PP_i can be detected enzymatically;

adding different deoxynucleotides or dideoxynucleotides successively to the ample-primer mixture; and

determining which deoxynucleotide or dideoxynucleotide is incorporated, thereby identifying a base that is complementary to the base at the target position.

40. The method of claim 39 wherein said different deoxynucleotides or dideoxynucleotides are added to said DNA sequence by a fluid flow that is normal to a plane of the planar membrane reactor array.

41. The membrane reactor array of claim 40 wherein said fluid flow has a flow rate of 0.15 ml/minute/cm² to 4 ml/minute/cm².

42. A method of identifying a base at a target position in a sample DNA sequence comprising:

arranging a multiplicity of DNA sequences, each immobilized on a bead, in array format on a membrane reactor array of claim 1;

providing to each sample an extension primer, which hybridizes to the sample DNA immediately adjacent to the target position and subjecting the sample DNA and extension primer to a polymerase reaction in the presence of a deoxynucleotide or dideoxynucleotide, whereby the deoxynucleotide or dideoxynucleotide will only become incorporated and release pyrophosphate (PP_i) if it is complementary to the base in the target position and detecting any release of PP_i enzymatically, and whereby a nucleotide-degrading enzyme is included during the polymerase reaction such that unincorporated nucleotides are degraded;

adding different deoxynucleotides or dideoxynucleotides successively to the same sample-primer mixture in a fluid flow that is normal to the plane of the planar mesh;

determining which deoxynucleotide or dideoxynucleotide is incorporated, thereby identifying a base that is complementary to the base at the target position.

43. The method of claim 42 wherein said nucleotide-degrading enzyme is apyrase.

44. A method of loading a membrane reactor array comprising the steps of:

(a) providing a membrane reactor array of claim 1 which is substantially permeable to a fluid but substantially impermeable to a population of microreactor beads;

(b) depositing said fluid comprising a suspension of said population of microreactor beads on the surface of the membrane reactor array; and

(c) settling said microreactor beads onto the pores at no more than one bead per pore.

45. The method of claim 44 wherein said settling comprises drawing said fluid through said membrane reactor array whereby said microreactor beads are trapped in said membrane reactor array.

46. The method of claim 44 wherein said microreactor beads have a diameter of between 20 to 35 μ

m.

47. A microimaging lens system for imaging a light emission from a membrane reactor array of claim 1 comprising:

(a) a front lens group for collecting a light emission from a sequencing reaction; and

(b) a rear lens group for imaging said light emission in a spatially ordered manner onto an optical detector.

48. The microimaging lens system of claim 47 wherein at least one said lens group has a focal length of at least 30 mm focal length.

49. The microimaging lens system of claim 47 wherein at least one said lens group has a focal length of at least 50 mm focal length.

50. The microimaging lens system of claim 47 wherein at least one said lens group has a focal length of at least 70 mm focal length.

51. The microimaging lens system of claim 47 wherein at least one said lens group has an aperture brighter than or equal to 4.0.

52. The microimaging lens system of claim 47 wherein at least one said lens group has an aperture brighter than or equal to 2.8.

53. The microimaging lens system of claim 47 wherein at least one said lens group has a numeric aperture larger than or equal to 0.1.

54. The microimaging lens system of claim 47 wherein at least one said lens group has a numeric aperture larger than or equal to 0.2.

55. The microimaging lens system of claim 47 wherein at least one said lens group has a numeric aperture larger than or equal to 0.3.

56. The microimaging lens system of claim 47 wherein said front lens group and rear lens group are identical.

57. The microimaging lens system of claim 47, further comprising a solid state optical detector.

58. The microimaging lens system of claim 57 wherein the solid state optical detector is a CCD array.

59. The microimaging lens system of claim 47 further comprising a structure to block light not originating from the membrane reactor array from reaching the optical detector.

60. The microimaging lens system of claim 59 wherein said structure is an opaque tube comprising a first end which forms a light tight fit to one end of the microimaging lens and comprising a second end which forms a light tight fit the optical detector.

61. The microimaging lens system of claim 59 wherein said structure is an opaque tube comprising a first end which forms a light tight fit to one end of the microimaging lens and comprising a second end which forms a light tight fit to a membrane adaptor array.

62. A sequencing cartridge comprising:

(a) a flow chamber enclosing a membrane reactor array of claim 1 with an inlet port and an outlet port,

(b) an optical window for the optical examination of said membrane reactor array;

(c) an inlet port for delivering sequencing reagents;

(d) a first outlet port for removal of sequencing reagents; and

(e) a second outlet port for removal of effluents.

63. The sequencing cartridge of claim 62 wherein the optical window is circular.

64. The sequencing cartridge of claim 62 wherein the flow chamber is substantially funnel shaped with the wide section of the funnel proximal to the membrane support structure and the narrow section of the funnel at the second outlet port.

65. The sequencing cartridge of claim 62 wherein said support structure comprises a porous solid surface.

66. The sequencing cartridge of claim 62 wherein said inlet is in fluid communication with a pump for controlling a flow of fluids through said inlet.

67. The sequencing cartridge of claim 62 wherein said first outlet port is in fluid communication with a first pump for controlling a flow of fluids through said first outlet port.

68. The sequencing cartridge of claim 62 wherein said second outlet port is in fluid communication with a second pump for controlling a flow of fluids through said second outlet port.

69. The sequencing cartridge of claim 62 wherein said inlet and said first and said second outlet is each in fluid communication with a different pump for controlling a flow of fluids so that a flow of fluids normal to the plane of the membrane reactor array and a flow of fluid tangential to the plane of the membrane reactor array can be controlled simultaneously.

70. A method of producing a membrane reactor array of nucleic acids comprising the steps of:

(a) providing one or more nucleic acid templates to be amplified wherein a plurality of nucleic acid templates are individually attached to separate beads to form a population of nucleic acid template-carrying beads;

(b) suspending said nucleic acid template-carrying beads in an amplification reaction solution containing reagents necessary to perform nucleic acid amplification;

c) forming an emulsion wherein a plurality of said template-carrying beads and PCR reaction solution are individually isolated in the emulsion to form a plurality of microreactors;

(d) amplifying the one or more nucleic acid templates in fluidic isolation from each other to form amplified nucleic acid;

(e) attaching the amplified nucleic acid to said beads; and

(f) loading said beads onto a membrane reactor array of claim 1.

71. A method of producing a membrane reactor array of nucleic acids comprising the steps of:

(a) providing one or more nucleic acid templates to be amplified wherein a plurality of nucleic acid templates are individually attached to separate beads to form a population of nucleic acid template-carrying beads;

(b) loading said beads onto a membrane reactor array of claim 1;

(c) contacting said nucleic acid template-carrying beads to an amplification reaction solution containing reagents necessary to perform nucleic acid amplification; and

(d) amplifying the one or more nucleic acid templates in fluidic isolation from each other to form amplified nucleic acids.

28. A membrane reactor array, comprising

(a) a planar array layer comprising a plurality of pores with reagent-carrying beads disposed in a plurality of said pores such that a maximum of one bead is disposed within any one pore, wherein said beads restrict but do not completely block the flow of fluid through said pores, and wherein the array is substantially permeable to aqueous solutions but is substantially impermeable to said beads, and wherein said planar array is made from a fiber material of substantially uniform cross-section weaved to form a mesh layer comprising an array of pores of uniform size, and wherein each pore is an opening of less than 40 μ

m; and

(b) a porous high flow resistance membrane layer, in contact with the planar array layer, that is permeable to nucleic acids and proteins to provide flow resistance of greater than 10 fold that of the flow resistance of aqueous solutes through a bead containing pore in said planar array.

29. The membrane reactor array of claim 28 wherein said planar array layer comprises two sets of parallel fibers woven together such that the two sets of parallel fibers are substantially at right angle to each other, wherein each individual fiber of each set has a center to center spacing of less than 100 μ

m, and wherein the fibers form an array of pores.

30. The membrane reactor array of claim 28 wherein said planar array layer comprises pores with a pore size length in one dimension of about 20 μ

m to 35 μ

m and a spacing of pores of about 50 to 78 μ

m center to center.

31. The membrane reactor array of claim 28 wherein the percentage of pores in the mesh layer that are loaded with beads is selected from the group consisting of 5%, 10%, and 25%.

32. The membrane reactor array of claim 28 wherein at least one sequencing enzyme is immobilized on said mesh layer or said bead.

33. The membrane reactor array of claim 32 wherein the sequencing enzyme is selected from the group consisting of ATP sulfurylase, luciferase, polymerase, hypoxanthine phosphoribosyltransferase, xanthine oxidase, uricase, and peroxidase.

34. The membrane reactor array of claim 28 wherein said array is substantially impermeable to a bead with a diameter of more than 40 μ

m.

35. The membrane reactor array of claim 28 wherein said plurality of beads are attached to at least one nucleic acid molecule.

36. The membrane reactor array of claim 35 wherein each said bead is attached to a single nucleic acid molecule.

37. The membrane reactor array of claim 35 wherein each said bead is attached to a single species of nucleic acid molecule.

38. The membrane reactor array of claim 32, further comprising a pyrophosphate degrading enzyme immobilized on one said layer or on said bead.