Claims
- 1. A method of producing a thin film of oriented polymer structures, comprising the steps of:
controlling the flow of a polymer solution into a device having a substrate, the device generating a shear flow to induce alignment of polymer structures; controlling a plurality of parameters during polymerization; and generating a layer of oriented polymer.
- 2. The method of claim 1, wherein the polymer is a biopolymer such as collagen.
- 3. The method of claim 2, wherein the method further comprises the steps of:
mixing a solution of collagen with phosphate buffered saline solution; adjusting the pH of the solution to 7.4±0.2; applying the solution at a controlled rate onto a substrate which generates a shearing flow; causing preferential orientation of the gelling collagen fibrils; and generating successive layers, each layer representing a portion of the component.
- 4. The method of claim 3, wherein the layers have a uniform, controllable thickness ranging from sub-micron to 100 microns.
- 5. The method of claim 2, wherein the collagen is either type I or type V collagen.
- 6. The method of claim 1, wherein the principle orientation of the aligned fibrils in a single layer alternates in each successive layer.
- 7. The method of claim 3, wherein the angle between the principle orientation of each layer is approximately in the range of 0 to 180 degrees.
- 8. The method of claim 1, wherein the solution properties, including temperature, concentration and surfactant composition are controlled.
- 9. The method of claim 1, wherein the shear flow is generated by spinning the substrate at a controlled rate in a range of approximately 50 to 50,000 Hz.
- 10. The method of claim 1, wherein the shear flow is generated by drawing the substrate out of the collagen solution.
- 11. The method of claim 1, wherein the atmosphere is controlled to a specified temperature and relative humidity.
- 12. The method of claim 1, wherein the solution conditions are modulated to control the polymerization kinetics and morphology.
- 13. The method of claim 1, wherein the use of shear flow aligns polymerizing polymer chains in a layer such that polymers are predominantly aligned parallel to each other.
- 14. The method of claim 1, further comprising angular rotation of the substrate providing shear flow and confinement to orient the polymerized polymers.
- 15. The method of claim 14, wherein an input flow rate, solution viscosity and substrate rotational velocity combine to produce a shear rate between 1 s−1 and 500,000 s−1.
- 16. The method of claim 14, wherein an input flow rate, solution viscosity and substrate rotational velocity combine to produce a shear rate preferably between the range 10 s−1 and 10,000 s−1.
- 17. The method of claim 1, wherein a second aligned polymer layer is produced on top of a first polymer layer by repeating the method.
- 18. The method of claim 17, wherein a rotating surface is moved to change a deposition direction on the substrate.
- 19. The method of claim 17, wherein the second layer comprises a different material than the first layer.
- 20. The method of claim 17, wherein the second layer is a promoter of at least one of cell adhesion and proliferation.
- 21. The method of claim 17, wherein an additional layer comprising collagen type IV and cell adhesion proteins such as, laminin, fibronectin and/or any integrin receptor is deposited between aligned polymer layers.
- 22. The method of claim 15, wherein a construct of a plurality aligned layers is used as a replacement or repair of the human stroma.
- 23. The method of claim 17, wherein the alignment of the polymers in a plane of second and subsequent layers is predominantly parallel with the alignment of the polymers in a plane of the layer in the first layers.
- 24. The method of claim 17, wherein the alignment of the polymers in a plane of a layer in a second and subsequent layers is predominantly orthogonal with the alignment of the polymers in the plane of a layer in the first layers.
- 25. The method of claim 17, wherein the alignment of the polymers in a plane of a layer in the second and subsequent layers does not have a defined angular relationship to the alignment of the polymers in a plane of a layer in the first layers.
- 26. The method of claim 1, wherein the end-associating biopolymer monomer is included in an aqueous solution.
- 27. The method of claim 26, wherein the biopolymer monomer is collagen.
- 28. The method of claim 26, wherein the biopolymer monomer is extracted or recombinant collagen.
- 29. The method of claim 26, wherein the collagen is Type I as the polymerizing medium.
- 30. The method of claim 26, wherein the collagen is Type I and Type V to assist in creation of heterotypic fibrils.
- 31. The method of claim 1, wherein the polymer solution is injected at a constant rate.
- 32. The method of claim 1, wherein the polymer solution is injected with a flow rate between 0.05-1000 ml/min.
- 33. The method of claim 1, wherein the material is preferably injected with a flow rate between of 0.1-100.0 ml/min.
- 34. The method of claim 1, further comprising a post-processing step including spinning off any effluent material from the substrate.
- 35. The method of claim 1, further comprising the substrate and a substrate holder being modified to minimize waste of polymerization solution.
- 36. The method of claim 1, wherein the solution is preferably composed of 8:1:1 ratio of collagen type I (3 mg/ml) to 10× PBS to 0.1M NaOH with pH adjusted to 7.4.
- 37. The method of claim 1, wherein the viscosity of the solution is between 1 mPa.s and 100 Pa.s.
- 38. The method of claim 1, where the viscosity solution is preferably between 5 mPa.s and 1 Pa.s.
- 39. The method of claim 1, wherein the substrate comprises one of a flat surface or curved surface.
- 40. The method of claim 39, wherein the flat surface is optically smooth.
- 41. The method of claim 39, wherein preferably the flat surface has a surface roughness of approximately less than 10 microns.
- 42. The method of claim 39, wherein the substrate is a borosilicate glass disk.
- 43. The method of claim 1, wherein a surface of the substrate is treated to control adhesion of the polymer and wetting of the solution.
- 44. The method of claim 1, wherein a surface of the substrate is ultrasonicated in 10% micro90 (Brand) cleaner for a time duration.
- 45. The method of claim 1, wherein a surface of the substrate is plasma cleaned.
- 46. The method of claim 1, wherein a surface of the substrate is homogeneous.
- 47. The method of claim 1, wherein the substrate has a surface treatment that is heterogeneous.
- 48. The method of claim 1, wherein the substrate has a surface treatment that is patterned.
- 49. The method of claim 1, wherein a substrate is patterned to constrain the flow.
- 50. The method of claim 1, wherein a surface of the substrate and atmospheric conditions are modulated to control self-assembly.
- 51. The method of claim 50, wherein the atmospheric conditions include a temperature range of 30° C.-45° C. and humidity range of 80-100%.
- 52. The method of claim 51, wherein the preferred range is 35° C.-42° C. with 90-100%.
- 53. The method of claim 1, wherein a substrate of the rotation velocity is used to control layer thickness and final polymerized material morphology.
- 54. The method of claim 53, wherein a layer thickness is between 100 nm and 1 mm.
- 55. The method of claim 53, wherein layer thickness is preferably between 0.5 μm and 100 μm.
- 56. The method of claim 53, wherein the substrate rotational velocity is varied.
- 57. The method of claim 53, wherein the velocity is initially between 10 to 5,000 rpm.
- 58. The method of claim 53, wherein the velocity is preferably initially between 60 to 1,000 rpm.
- 59. The method of claim 53, wherein the velocity during polymerization is constant.
- 60. The method of claim 53, wherein the velocity during polymerization is varied.
- 61. The method of claim 53, wherein the velocity is in the range 100 to 50,000 rpm.
- 62. The method of claim 53, wherein the velocity is preferably in the range 500 to 10,000 rpm.
- 63. The method of claim 53, wherein the average velocity is in the range 100 to 50,000 rpm.
- 64. The method of claim 63, wherein the average velocity is preferably in the range 500 to 10,000 rpm.
- 65. The method of claim 1, wherein additives are injected with the polymer solution to control the polymerization process and final morphology of the layer.
- 66. The method of claim 65, wherein the additives are proteoglycans.
- 67. The method of claim 65, wherein the additives are at least one of chondroitin sulfate, dermatan sulfate and keratan sulfate proteoglycans.
- 68. The method of claim 65, wherein the proteoglycans are one of at least or a combination of decorin, lumican, biglycan, keratocan or syndican.
- 69. The method of claim 65, wherein the percent (by weight) of added proteoglycans is between 0.25 and 50.0.
- 70. The method of claim 65, wherein the percent by weight of added proteoglycans is between 0.5 and 10.
- 71. The method of claim 1, wherein a network of channels is used to guide the growth of the polymerizing polymers.
- 72. The method of claim 71, wherein the growing polymer is attached to a fixed point and extruded from a channel as it polymerizes.
- 73. The method of claim 71, wherein the growing polymer is attached to a moving plate pulled through a channel where conditions conducive to polymerization are maintained.
- 74. The method of claim 71, wherein conditions outside the channels are not conducive to polymerization.
- 75. The method of claim 71, where in said channel is part of an array of identical channels.
- 76. The method of claim 71 wherein said channel is treated to prevent adhesion of polymerizing material.
- 77. The method of claim 71, wherein said channels are manufactured using any standard microfabrication process.
- 78. The method of claim 71, wherein said channels are obtained from a self-assembled three dimensional network.
- 79. A system to align polymerizing polymer chains in a layer such that polymers are predominantly aligned parallel to each other, comprising:
an apparatus to generate shear flow; a plurality of sensors to monitor a plurality of parameters; and a processor to modulate a plurality of control parameters.
CROSS REFERENCES TO RELATED APPLICATIONS
[0001] This application claims the benefit of U.S. Provisional Application No. 60/337,286 filed on Nov. 30, 2001, the entire contents of which are incorporated herein by reference in its entirety.
Provisional Applications (1)
|
Number |
Date |
Country |
|
60337286 |
Nov 2001 |
US |