Method of making enhanced cell growth surface

Abstract

A method of producing an improved cell growth surface and cell attachment surface. According to the present invention, a polymer article is molded at temperature in excess of 550° F. at the injection tip. After allowing the part to cool, a stream of plasma comprised of activated gaseous species generated by a microwave source is imparted on the article. This stream is directed at the surface of a polymer substrate in a controlled fashion such that the surface is imparted with attributes for cell adhesion superior to those of untreated polymer or polymer treated by other methods.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a schematic drawing of the microwave plasma treatment apparatus of the present invention.

FIG. 2 is a graphical representation of a comparative cell growth study performed with injection molded polystyrene microplates molded at a variety of temperature and with 2 different plasma gases.

DETAILED DESCRIPTION

Typically, injection molded polymer articles for use as disposable cell culture vessels are molded at temperatures of between 400° F. and 500° F. However, it has been discovered that maintaining all other standard molding conditions (pressure, fill time, cycle time, etc.) but raising the molding temperatures imparts characteristics in the article surface that, after proper post treatment processing, aids in the attachment and growth of cells. Although not intending to being bound by theories of operation, it is thought that molding at higher temperature creates a surface with greater texturing than those surfaces molded at relatively lower, industry standard temperatures. To that end, it is preferable that molding occur at temperatures in excess of 500° F., 550° F., and even in excess of 600° F. For purposes of this invention, ideal molding temperatures may vary depending on the type of polymer. For polystyrene, articles should be molded at temperatures of 550-650° F., 590-630° F., or 600-620° F. Cycle times for molding will typically run 12-17 seconds. Once removed from the mold and cooled, the articles are subjected to a microwave plasma stream.

With reference to FIG. 1, a basic construction of the microwave plasma stream apparatus for carrying out the method of the present invention is provided. A 2.45 GHz microwave generator 10 (MKS Astex, Wilmington, Mass.) serves as the energy source of this apparatus. The equipment preferably includes a generator, circulator, dummy load, tuner, and applicator. A gas line 12 connects to a gas source and delivers the process gas, which when sufficiently energized creates a continuous stream of activated or ionized gas. Suitable plasma gases include argon, nitrogen, oxygen, nitrous oxide, ammonia, carbon dioxide, helium, hydrogen, air and other gases known to those of skill in the art. A plasma chamber 14 serves as a manifold for the reaction between gas and microwave energy, and is in fluid communication with both the gas line 12, via a valve 13, as well as the microwave generator 10. A conduit 16 connects the plasma chamber with a treatment chamber 18 through an aperture 20. Within the first or outer treatment chamber 18, a second or inner treatment chamber 22 is located. The inner chamber has a frusto-conical baffle section which serves to contain the plasma flow and direct it onto a part that is placed at its base. In this embodiment, the inner chamber shares a common base 25 with the outer chamber. The approximate 1-6 inch gap between the aperture and the neck of the second treatment chamber enable the plasma to flow out of the outer treatment chamber through a valved vacuum line 24. A pneumatic elevating system 29 may be employed to move the base portion 25 away from the treatment chamber in order to remove treated parts and place new parts into the inner chamber in an automated fashion. The conduit 16 and outer treatment chamber may be made from conductive or nonconductive materials, especially quartz, aluminum or stainless steel. The inner treatment chamber may be made from a nonconductive material, and most preferably, quartz.

In operation, the apparatus of FIG. 1 performs as follows: A molded polymer part to be treated is located within the inner chamber 22. For purposes of illustration, a multiwell plate 26 has been placed on the base 25, but the inner and outer chamber may be shaped, dimensioned and configured to accommodate any of a variety of polymer parts. A vacuum seal is created between the base 25 and the sidewalls 27 of the outer chamber. To enable continuous flow, vacuum pumping is maintained through the process. The valves 13, 23 are opened and the process gas is allowed to flow into the plasma chamber 14, through the aperture 20 and into the dual chambered treatment area. The gas flows at a pressure preferably between 100 and 2,000 millitorr, and more preferably between 200 and 300 millitorr. The gas is preferably set to flow at a rate of 100 to 5,000 cc/min, and more preferably between 400 and 600 cc/min. While the process may run at any range of temperatures, it preferably runs between 40 and 150 degrees Fahrenheit and more preferably at room temperature, or approximately 72 degrees Fahrenheit. The microwave generator is engaged to create an output of between 300 and 10,000 watts, and preferably between 300 and 3,000 watts. The microwave energy entering the plasma chamber 14 interacts with the gas entering the plasma chamber resulting in activation of the gas thereby creating the resultant plasma. Due to the constant flow characteristics of the assembly, the plasma is directed through the conduit 16, through the aperture 20, and into the treatment chamber. The stream or jet created by the plasma flow through the conduit and aperture is directed into the outer treatment chamber 18, subsequently into the inner treatment chamber 22, and onto the polymer part 26 placed at the base 25 of the chamber. Flow out of both the inner chamber 22 and outer chamber 18 is assured due to the vacuum line 24, which serves to evacuate the dual chambered treatment area. It should be noted that due to the inner treatment chamber 22, the plasma stream is directed onto the part as opposed to directly toward the outlet valve 23, thereby enabling the part 26 to have optimal contact with the stream. The inner treatment chamber 22 should be entirely enclosed and sealed from the outer chamber 18, but for the opening at the neck.

The plasma is energized for between 1 second and 5 minutes and more preferably for between 5 and 20 seconds. Once treatment is complete, the microwave energy is ceased, valves are closed, an atmospheric vent valve 32 is opened to introduce nitrogen or dry air to the system and in order to return all the chambers to atmospheric pressure. After normalization of pressure, the part is removed by operating the pneumatic elevating system 29. Optimally, a computer control system performs the steps outlined above in an automated fashion. After removal, the part is preferably given a standard sterilization treatment by exposure to gamma radiation.

The surface of the polymeric substrate to be treated can have any shape, for example it can be flat, curved or tubular. Preferably, it is a flat planar surface. For purposes of this invention, the polymeric substrate can be biodegradable or non-biodegradable. Preferably, to be useful in both in vivo and in vitro applications, the polymeric substrates of the present invention are non-toxic, biocompatible, processable, transparent for microscopic analysis, and mechanically stable.

A large variety of polymers may be used as substrates in the articles of the present invention. Examples of polymers useful in the present invention include polyacrylates, polymethylacrylates, polycarbonates, polystyrenes, polysulphones, polyhydroxy acids, polyanhydrides, polyorthoesters, polypropylenes,

polyphosphazenes, polyphosphates, polyesters, nylons or mixtures thereof.

Examples of substrates that can be treated by the method disclosed herein include but are not limited to: flasks, dishes, flat plates, well plates, bottles, containers, pipettes, tubes, medical devices, filter devices, membranes, slides, and medical implants. These items are typically formed by commonly practiced techniques such as injection molding, extrusion with end capping, blow molding, injection blow molding, etc.

Although the invention is targeted for cell adhesion, attachment, and growth, the resultant polymer substrate surface promotes adsorption of a number of biologically active molecules including but not limited to: peptides, proteins, carbohydrates, nucleic acid, lipids, polysaccarides, or combinations thereof, hormones, extracellular matrix molecules, cell adhesion molecules, natural polymers, enzymes, antibodies, antigens, polynuceotides, growth factors, synthetic polymers, polylysine, drugs and other molecules.

Any cell type known to one of skill in the art may be attached and grown on the treated substrates of the present invention. Examples of cell types which can be used include nerve cells, epithelial cells, mesenchymal stem cells, fibroblast cells, and other cell types.

While the mechanism for enhanced cell attachment to the substrate treated according to the present method is not fully understood, it is believed to stem from three general characteristics: surface morphology, chemical functionalities, and surface energy.

EXAMPLE

FIG. 2 is a graphical representation of a comparative cell growth study performed with injection molded 96-well polystyrene clear plates that have been molded at a variety of temperature conditions and subjected to two different types of microwave plasma treatments. A Cincinnati Milacron 300 ton injection molding machine was employed for making the plates that were later post treated with microwave plasma. The molding conditions were as follows: For “High Temperature” molding, temperatures at the injection tip were approximately 610° F. For “Cold Temperature” molding, temperature at the injection tip was approximately 570° F. For the “Cont” or control condition, a more standard molding temperature of 460° F. was employed. In “Type I” treatment, the plasma gas utilized was a nitrous oxide. The nitrous oxide generally imparts a negative charge to the treated surface. In “Type II” treatment, the plasma gas utilized was ammonia. Ammonia, when utilized as the plasma gas tends to impart a negative charge to the treated surface. Finally, all samples were compared to plates treated with known chemical cell attachment coating, poly-D lysine (PDL). Cells were seeded at 70,000 cells per well of the plate and tested in triplicate. Cell growth conditions were measured by optical density readings under 10% serum growth conditions for 24 hours. Optical density assay quantification was carried out by a standard calorimetric kit (Cell Titer 96-Aq., Promega Corporation, Madison, Wis.). The cell line used was Hek-293. Cells were seeded onto all surfaces at the same time, with the same initial number of cells, under the same conditions. Table 1 displays the data.

	Molding Condition	Treatment Gas	Optical Density
	High	Nitrous Oxide	0.281
		(Type I)
	High	Nitrous Oxide	0.568
	High	Nitrous Oxide	0.569
	Low	Nitrous Oxide	0.250
	Low	Nitrous Oxide	0.360
	Low	Nitrous Oxide	0.421
	Control	Nitrous Oxide	0.362
	Control	Nitrous Oxide	0.277
	Control	Nitrous Oxide	0.303
	High	Ammonia	0.312
		(Type II)
	High	Ammonia	0.345
	High	Ammonia	0.321
	Low	Ammonia	0.349
	Low	Ammonia	0.244
	Low	Ammonia	0.269
	Control	Ammonia	0.320
	Control	Ammonia	0.380
	Control	Ammonia	0.321
	Poly-D Lysine	None	0.281
	Ploy-D Lysine	None	0.342

As demonstrated in the graph of FIG. 2, the microwave nitrous oxide plasma treatment molded at high temperatures significantly outperformed the plates molded at different conditions.

From the foregoing description of the various preferred embodiments, it should be appreciated that the present invention may take many various forms and that the present invention is to be limited only by the following claims.

Claims

1. A method for creating a polymer article having a working surface upon which cells can be cultured comprising the steps of: a) molding a polymer article at a molding temperature at the injection tip of greater than 550° F., andb) subjecting said working surface of said article to a gaseous stream that has been energized by microwave energy.

2. The method of claim 1 wherein said polymer is a polyacrylate, a polymethylacrylate, a polycarbonate, a polystyrene, a polysulphone, a polyhydroxy acid, a polyanhydride, a polyorthoester, a polypropylene, a polyphosphazene, a polyphosphate, a polyester, a nylon or mixtures thereof.

3. The method of claim 2 wherein said polymer is polystyrene.

4. The method of claim 1, wherein the working surface includes at least a portion of a flask, a dish, a flat plate, a well plate, a bottle, a container, a pipette, a tube, a medical device, a filter device, a membrane, a slide, or a medical implant.

5. The method of claim 4, wherein the working surface includes at least a portion of a flask, a roller bottle, or a multiwell plate.

6. The method of claim 1 wherein the gaseous stream is activated argon, nitrogen, oxygen, nitrous oxide, ammonia, carbon dioxide, helium or hydrogen.

7. The method of claim 6 wherein the gaseous stream is activated nitrous oxide.

8. The method of claim 1 wherein the molding temperature is greater than 600° F.

9. A polymer article produced by the method of claim 1.