|Publication number||US3853712 A|
|Publication date||Dec 10, 1974|
|Filing date||Feb 8, 1972|
|Priority date||Feb 9, 1971|
|Publication number||US 3853712 A, US 3853712A, US-A-3853712, US3853712 A, US3853712A|
|Inventors||W House, N Maroudas|
|Original Assignee||Nat Res Dev|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (4), Referenced by (83), Classifications (13)|
|External Links: USPTO, USPTO Assignment, Espacenet|
United States Patent [191 House et al.
1 CELL CULTURE SYSTEMS  Inventors: William Cullingford House,
Southborough; Nicholas George Maroudas, London, both of England  Assignee: National Research Development Corporation, London, England 22 Filed: Feb. 8, 1972 21 Appl. No.: 224,527
 Foreign Application Priority Data Feb. 9, 1971 Great Britain 4266/71 Nov. 4, 1971 Great Britain 51343/71  US. Cl 195/127, l95/1.7, 195/139, 195/142  Int. Cl ..C12b l/00  Field of Search 195/127, 139, 140, 142, 195/143, 109, 1.7, 1.8
 References Cited UNITED STATES PATENTS 2,522,947 9/1950 Hatch et a1. 195/143 X Dec. 10, 1974 3,102,082 8/1963 Brewer 1. 195/139 3,281,307 10/1966 Moeller et a1. 195/142 X 3,740,321 6/1973 Pagano et a1. 195/127 Primary ExaminerA. Louis Monacell Assistant ExaminerR. B. Penland Attorney, Agent, or FirmFinnegan, Henderson, Farabow & Garrett  ABSTRACT The present invention comprises a method for culturing animal cells in which cells adhering to the surface of a flexible strip wound or otherwise formed by successive changes of direction into a compact cell support are contacted with culture medium. The present invention also comprises apparatus for carrying the method into effect, in which apparatus neighbouring surfaces of the support may be spaced apart to provide one or more passageways whereby in operation culture medium has access to the support to nourish cells at the surface thereof.
14 Claims, 11 Drawing Figures PATENTEB DEC] 0 I974 SHEET 3 OF 4 CELL CULTURE SYSTEMS This invention relates to the culture of animal and in particular mammalian cells and apparatus therefor.
Certain of the cell lines used in tissue culture, such as BHKZl, grow by adhering to and spreading over a suitable surface. Surfaces which have hitherto been employed for large scale growth of such cell lines include the inner surfaces of glass bottles (roller bottles) and the outer surfaces of beads, e.g., of porous silica or dextran, glass helices, glass or stainless steel plates and ion exchange beads which are packed or stacked in a suitable vessel.
It has now been found that animal cells can be cultured with advantage on other supports.
According to the present invention, a method for culturing animal cells comprises contacting with culture medium cells adhering to the surface of a flexible strip wound or otherwise formed by successive changes of direction into a compact cell support.
It has been found that in this method excellent results are obtained when the strip material is deformed into a variety of configurations in order to provide a support of large surface area per volume of the support as compared with the supports hitherto employed. Growth and multiplication of the cells proceeds with transfer to the cells of nutrient medium in the bath, the medium also providing a suitable pH and gaseous environment for growth.
The strip material should possess a non-toxic surface to which the cells are adhere and preferably has a thickness within the range -1000 microns. Unplasticised polymers which possess a relatively hydrophilic surface, e.g., polyesters such as Melinex (a Registered Trade Mark), are suitable as materials for the support as also are more hydrophobic materials (e.g., polypropylene and polystyrene), which can be treated so as to possess hydrophilic surfaces, for example Bexphane and Polyflex (Registered Trade Marks). Polyflex, which is particularly suitable, is an oriented polystyrene material which can be treated by corona discharge to give a hydrophilic surface. These materials preferably satisfy the criterion for choice of good cell adhesion, low toxicity, high strength, low weight, low cost and ready availability. The surface tension is preferably at least 40 e. g., at least 50 dynes/cm. Strip material such as aluminised polymers, stainless steel or aluminium may be alternatively employed if so desired.
In a preferred embodiment of the method particularly suitable for batch wise culture, neighbouring surfaces of the support are spaced apart to provide one or more passageways whereby culture medium has access to the support to nourish cells at the surface thereof.
The support in the form of a roll the turns of which are preferably spaced apart by 1 to 10 mm. e.g., 3 to 5mm. to allow access of nutrient medium to the cells, may be formed by winding a length of corrugated strip material and a length of smooth, planar strip material together into a self-spacing spiral, the corrugated strip being preferably much narrower than the noncorrugated strip. If so desired the corrugated strip material may be replaced by a non-corrugated strip possessing a recessed, e.g., a dimpled, surface. Layers of strip material may alternatively be spaced apart by other means e.g., by employing alternating layers of chain, rod, string, beads or the like. When smooth, planar strip material is employed moreover, support may be received from a frame, which can serve to space apart the surfaces of the strip.
The containers employed may of course vary considerably in shape and size. The glass roller-bottles com monly used in tissue culture or other vessels of similar dimensions may be employed, and inclusion of selfspacing spirals may then increase the effective surface area by 5 to 20 fold e.g., 10 fold. When the increase in surface is larger than 5 -fold however it is generally necessary to replace the oxygen and in some cases the nutrient medium either batchwise or continuously via an inlet and outlet which, when rotation of the bottle together with the support is desired, may pass through a closure provided with a rotary seal.
In preferred embodiments of the present invention however the container is fabricated from a suitable plastics material e.g., polystyrene, is preferably generally cylindrical in shape and 5 to 50 cm. in diameter by 20 to 50 cm. long e.g., l0.2 X 30.5 cm., with capacity 500 to 20,000 ml. e.g., 500 to 2,000 ml. The vessel is provided with an inlet for nutrient medium and cells, and a sparge tube and encloses a cell support of flexible strip material preferably 50 to microns thick. It is envisaged that the cell culture apparatus will be supplied to the user witha support in place as a disposable irradiation-sterilised unit. Such units can obviate the handling costs involved in washing and sterilising the glass roller-bottles at present used. Incubation space may be substantially reduced as the units allow the realisation of improved cell growth at a relatively reproducible and uniform surface. Surface/volume ratios of 0.5 to 10 cm can be achieved, typically 3 to 5 cm', e.g., 4 cm.
Whilst rotation of the support is advantageous in promoting inoculation it is not essential for growth. It is possible to obtain good growth by first allowing cells to settle on to a support which is horizontally disposed, following which the vessel containing the support is moved to a position wherein the support surface is vertical. In some cases it may be necessary to provide an inlet and outlet for continuous replenishment of medium. As an alternative to aerating the medium by sparging, recirculated medium may be externally aerated.
In further embodiments of the present invention, the container has a wall portion through which the medium can be aerated. The gas permeable container may be conveniently fabricated from a plastic material e.g., polythylene, polypropylene, a silicone elastomer, fluorocarbons e.g., polytetrafluoroethylene, of such thickness as to allow adequate supply of oxygen and carbon dioxide across the container walls to sustain respiration of the cells within. In practice the container is generally fabricated at least in part from a film of the plastics material, the thickness of which preferably lies within the range 0.001 to 0.01 inches, the film preferably receiving support from an external or internal mesh. The container may be fabricated in a large number of sizes, the upper size limit being set by the rate of gas transport across the membranous container walls required to sustain growth of the cells within the unit. Typically however the container is of a size such that the growth of 0.5 X 10 to 5 X 10 cells e.g., 1.0 X 10 cells can be supported, and such that it can be rotated on a commercial rolling machine, units of size 4 inches X 12 inches having given satisfactory results. Rotation about the longitudinal axis causes the nutrient to flow from the outside to the inside of the cell support following a spiral pathway. When the support is in the form of a roll it is in some cases desirable for the innermost and/or outermost end of the strip to be spaced from the nearest portion of support surface by means of corrugated strips disposed along the length of the roll to facilitate through flow of medium.
In use units comprising gas permeable wall portions and containing cells and culture medium to which has been added a suitable buffer, e.g., a bicarbonate buffer, may be slowly rotated in an incubator containing a carbon dioxide/air mixture at a temperature such as 37 Centigrade. The rate of rotation should be controlled at 1 l revolutions per hour e. g., 4 revolutions per hour to prevent shearing of the cells from the spiral. Rotation about the longitudinal axis of the unit causes nutrient medium to circulate from the exterior to the interior and thence to the ends of the spiral. After cell growth is completed the cells may be harvested by rotation of the unit which is preferably effected manually and at greater speed than that employed during incubation; the shearing action thereby induced in the washing fluid induces transfer of the cells from the spiral thereto. If so desired, harvesting may be effected enzymically. The cells are then detached from their support by washing with a proteolytre enzyme such as Trypsin in conjunction with a chelating agent e.g., EDTA. Inoculation with a virus after cell growth has taken place can be effected by injection through an elastomeric septum which may be incorporated in a portion of the container wall.
In yet further embodiments of the present invention an incubation vessel contains a support e.g., a selfspacing spiral support which is secured to a frame rotatable with respect to the vessel. Medium can be continuously supplied to and discharged from the vessel via an inlet and outlet.
Also included within the scope of the present invention are cell culture processes which employ looped or folded strip, particularly planar strip, to form part of a conveyor system, the support members of the frame employed to support the strip being preferably rotatable. The conveyor system can carry cells from one set of incubating conditions to another and may be continuously inoculated with fresh cells at one end with harvesting of cells of a precisely determined age and growth regime at the other. The conveyor can either be supplied with continuously fresh strip when it is desirable to harvest both the cells and their support or alternatively can form a belt i.e., a continuous re-entrant loop, with inoculation at the head-end and harvesting at the later stage. In the latter case a part of the cells may be left on the conveyor belt after harvesting for return to the head-end as inoculum.
In particular mitotic cells may be preferentially removed from the strip material by washing and used as an inoculum to provide a synchronous population.
Cells can be eficiently and easily harvested from extended surfaces simply by scraping, with the use of water jets or both operations simultaneously. In the latter case the surface is wiped in a manner analagous to the operation of a windscreen wiper.
The foregoing general requirement for spacing apart the film surfaces to allow access of nutrient medium to the adherent cells during growth may be avoided if desired. In accordance with a second aspect of the present invention, a surface portion of the support is intermittently exposed to a bath of nutrient medium for a period such that sufficient nutrient is taken up to nourish cells adhering to said portion during the interval between exposures, the portion being incorporated for said interval into a configuration in which access of nutrient to said portion is relatively reduced. The latter process may be operated by employing two spools which may be enclosed within the vessel containing nutrient and between which the strip material is transferred through the bath of nutrient medium by periodic reversal of the direction of rotation. When this system is employed, inoculation and harvesting can be effected with great convenience at e.g., the end of the growth cycle by the action of a wiper blade or water jet or both together. The support can be conveniently inoculated by means of a jet.
Embodiments of the invention will now be described by way of example only with reference to the accompanying drawings of which:
FIG. I shows a longitudinal cross-section of a cell culture unit suitable for aeration by sparging;
FIG. 2 shows view in cross section of the unit shown in FIG. 1;
FIG. 3 represents diagrammatically a method for forming a support;
FIG. 4 shows a side view of a second embodiment with the support shown in FIG. 3 in place;
FIG. 5 shows an end view of the embodiment shown in FIG. d;
FIG. 6 shows a side view of a third embodiment of the invention;
FIG. 7 shows a sectional view of the third embodiment shown in FIG. 6;
FIG. 8 shows a longitudinal cross-section of a cell culture unit possessing a gas permeable wall portion;
FIG. 9 shows a view along the line IIII of FIG. 8;
FIG. 10 shows a sectional view of a fifth embodiment of the invention; and
FIG. 11 represents diagrammatically a sixth embodiment of the invention.
Referring now to FIGS. 1 and 2, a generally cylindrical vessel I of polystyrene is provided at one end with an inlet port for mediuim 2 and for gas 3, eg. an air/- CO mixture and an exhaust port 4 for waste gas. The gas inlet port communicates with an axially disposed sparge tube 5 of plastics material which extends from one end of the vessel to the region of the other end. The vessel is formed from two generally cylindrical portions 6, 7 of approximately equal length which are joined at their rims by waterproof tape (not shown). The vessel bears on each end face a cruciform arrangement of four L-shaped ribs 8,9, the limbs of which serve to space a cell support 10 enclosed within the vessel from the end faces and curved surface of the vessel. The support 10 takes the form of a roll of polystyrene film the turns of which are spaced 4 mm. apart by two narrow corrugated strips ll, 12 of Melinex, one at each end of the roll. Spacing of the ends of the polystyrene sheet from the surface of the neighbouring layer is additionally assisted by inclusion of two corrugated strips l3, 14 arranged along the length of the roll, the interior of which is penetrated by the centrally arranged sparge tube 5.
The unit as supplied is sterile and disposable and the inlet ports 2, 3, 4 are screw threaded to take caps which are removed before use. Removal of the tape after cell culture permits the cell support to be removed and the cells to be harvested by unwinding the roll followed by squeegee action.
If so desired, however, the cells may be washed from the support without dismantling the apparatus. In this case, or when for example the 'cells on the support are to be infected by contact with a small volume of a virus suspension, the circumferentially disposed limbs of the L-shaped ribs 8, 9 preferably vary in thickness e.g., logarithmically so that the outer edge of the support contacts the wall of the vessel 1 so that it can act as a scoop. On rotation, a small volume of liquid introduced into the vessel will then flow preferentially to the inside of the support.
FIG. 3 represents a diagrammatically a method of forming the cell support by winding together a length of corrugated strip material and a length of smooth planar strip material 15. The corrugated strip material may be made by passing Melinex, 1 cm wide by 125 microns thick, firstly through the air from a hot-air blower of exit temperature 300C, then through a pair of spur gears of pitch 4 mm (British 12 P.C.D., 1% inch wide by 1% inches in diameter) on a hand-operated rotary crimper, and finally through a blast of cold compressed air. To produce corrugations which withstand subsequent autoclaving, it is necessary to have the tape almost melting as it enters the gears, and to cool it immediately upon exit.
An example of the use of the apparatus now follows:
Procedure To inoclate with cells, medium is added, followed by a suspension of cells to a final volume of 2 litres, the unit inverted several times to distribute the cells evenly throughout the windings of the spiral support. The cells are then allowed to settle and spread evenly over both sides of the film, by rolling on a very slow machine (about 2 revolutions per hour). Normal roller speeds (10 to 60 r.p.h.) tend to wash cells off the surface and produce aggregates (presumably because of the increased hydrodynamic shear due to the narrower spacing in the spiral, as compared with a normal roller bottle). Cells are deposited uniformly, on both sides of the film, over its whole length, by selecting the optimum roller speed, non-uniform spreading being found to be the most frequent cause of low cell yield. For routine inspection, the outer layer of the spiral can be examined by placing the bottles on an inverted microscope in the usual way.
When the attachment and spreading of the cells is complete (from 3 to 18 hours, depending on the type of cell) the bottles are removed from the rollers and placed upright for aeration.
Boththe inlet and the outlet tube for air are fitted with a glass tube containing a cotton-wool plug. In the absence of anti-foam, the rate of aeration is of necessity very low, about ten bubbles per minute. However, to ensure uniform stirring throughout the spiral, a more vigorous gassing, with added anti-foam (Midland Silicone, Anti-foam Emulsion RD) is preferred. Spacing of the roll from the end of the vessel distal from the inlet port 2 by the L-shaped ribs 8 allows free recirculation of medium through the turns of the roll from one end to the other when the container and support are sprayed in a vertical position.
The medium used is Dulbeccos modification of Eagles medium, with 10 percent calf serum and aeration is usually done with l0percent C0,]air mixture, at
to 300 cc per minute per bottle. In some experiments a pH-stat can be used to operate a solenoid valve on the CO line; with this device it is possible to maintain the required pH within i 0.1 unit if required; however, for the comparative growth studies described below, the gas composition is kept constant at 10 percent CO Harvesting is done with trypsin in the same way as from a normal roller bottle, but with the volumes of trypsin and other reagents being scaled up proportionately to the number of cells. Mechanical harvesting is also possible by scraping or washing the cells off the plastic film, but may produce sheets and clumps of cells.
Results 8 X 10 BHK C13 are cultured in 2 litres of medium. After 5 days 1.0 X 10 cells are harvested. In comparative tests, with primary. cells (whole mouse embryo), 10 cells are routinely obtained with a 2 litre vessel containing a spiral support, compared to 10 cells from an ordinary roller bottle containing 200 ml of medium.
If so desired, when cells have become confluent, the medium can be removed from the culture vessel and replaced by a much smaller amount of a liquid e.g., a virus suspension which can be efiiciently distributed over the surface of the support when the vessel is rotated on a. roller machine.
Referring now to FIGS. 4 and 5, a glass roller-bottle 16 contains a self-spacing spiral support 17 and is provided with an inlet for medium 18 and outlet 19. Rotation of the bottle 16 together with the support 17 is made possible by a rotary seal 20.
Referring to FIGS. 6 and 7, a cylindrical incubation vessel 21 contains a self-spacing spiral support 22 mounted on a frame 23 which is rotatable with respect to the vessel 21 on a shaft 24 provided with a bearing 25. Medium can be continuously supplied and discharged through an inlet 26 and outlet 27.
Referring now to FIGS. 8 and 9, a generally cylindrical container for culture medium comprises a cylindrical polythene membrane 0.001 inches thick 28 sealed at one end to a thick walled polythylene cap 29 provided with a generally cruciform arrangement of four ribs 30 and sealed at the other end to a thick walled end portion 31 also bearing a cruciform rib arrangement 32 and bearing a screw closure 33 provided with an elastomeric insert 34 for injection of liquids. The container is enclosed and thereby protected by a inch plastics mesh work 35 and contains a 0.006 inch thick sheet of polystyrene or Melinex (a Registered Trade Mark) formed into a roll 36 the layers of which are spaced 4 mm apart by incorporation of two narrower corrugated strips 37, 38 one at each end of the roll, to provide spiral passageways 39 for culture medium. Spacing of the ends of the polystyrene sheet from the surface of the neighbouring layer is additionally assisted by inclusion of two corrugated strips 40, 41 which'arranged along the length of the roll, the outer surface of which is supported and spaced 4 mm from the membrane 28 by the end portion 31 and cap 29, and the ends of which are spaced from the end walls 42, 43 of the end portion 31 and cap 29 by means of the two cruciform sets of ribs 30, 32.
An example of the use of the latter embodiment for cell culture will now be described.
1,600 ml Dulbeccos modification of Eagles medium with 10 percent calf serum and 8 X 10" cells (BHK C13) are introduced into the sterilised cell culture unit. The stopper is flamed and replaced tightly, the bottle is placed on a Luckham roller machine, inside a cabinet heated to 37 and providing an atmosphere of percent CO /90 percent air and rolled at four revolutions per hour. After five days the cells are confluent and the bottle is then removed, the medium discarded and trypsin/EDTA (200 ml) added to the unit and the cell removed by manual rotation of the bottle. 7 X 10 cells are produced representing an approximately 9 fold increase. As hereinbefore described, in some cases if may be desirable for the outer longitudinal edge of the roll to contact the wall of the vessel so as to act as a scoop when small volumes of iiquid are introduced, and facilitate distribution to the inside of the roll.
Referring to FIG. 10, a length of non-corrugated strip 43 is wound upon support members or circular crosssection 44 in a vessel 45. When the support members 44 are rotatable, the support can form part of a conveyor system possessing a large area per unit volume of container.
Referring to FIG. 11 a vessel 46 is provided with an inlet 47 and outlet 48 for nutrient medium, and encloses capstans 49 and 50 on to which strip material 51 (which may be flat surfaced, dimpled or crimped) is wound. An inoculator 52 and harvester 53 are provided. in operation, the film is wound between the two capstans which periodically reverse their direction of rotation. The cells adhering to the film are thus periodically exposed to fresh medium from the vessel. The speed and tension of the capstans and length of film exposed to the medium are adjusted so that the amount of fresh medium picked up by any portion of the film in its travel between the capstans is sufficient to nourish the cells adhering to that portion for the period during which the portion spends on the capstan i.e., during which it is not fully exposed to the nutrient medium in the vessel and the speed at which the exposed film moves should be sufficiently slow that cells are not washed off into the medium.
1. Cell culture apparatus comprising a container for culture medium which encloses a compact cell support of a flexible strip material formed into turns which are spaced one from another to provide a continuous passageway through which cells and medium can travel progressively and continuously on rotary movement of the support during inoculation.
2. Apparatus according to claim l which incorporates a sparge tube for aeration of the medium during cell growth said sparge tube being so disposed within the container that aeration promotes circulation of culture medium along the length of the support between the turns.
3. Apparatus according to claim 1 in which the support is a roll of flexible strip material the turns of which in cross-section approximate to a spiral.
4. Apparatus according to claim 1 in which the turns of the support are spaced apart by corrugated strips located in the region of the end of the support.
5. Apparatus according to claim 2 in which the sparge tube is axially located within a support in the form of a roll of flexible strip material having an approximately spiral cross-section.
6. Apparatus according to claim 1 in which the strip material is formed of a material selected from the group consisting of polyester and polypropylene.
7. Apparatus according to claim l in which the strip material is formed of polystyrene which has been treated by corona discharge so as to produce a hydrophilic surface.
8. Apparatus according to claim 1 in which the surface tension of the strip material is not less than 40 dynes/cm.
9. Apparatus according to claim 3 in which the turns of the roll are spaced 1 to 10 mm. apart.
10. Apparatus according to claim 1 in which the ratio of the surface of the support and container to the volume of the container is between 0.5 and 10 cm.
1 1. Apparatus according to claim 1 in which the container has a gas permeable wall portion through which the medium can be aerated.
12. Apparatus according to claim 11 in which the wall portion is of film 0.001 to 0.01 inches in thickness.
13. Apparatus according to claim 3 in which the outennost longitudinal edge of the roll contacts the wall of the container.
14. Apparatus according to claim I in which the container and cell support form a sterile unit.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US2522947 *||Mar 27, 1947||Sep 19, 1950||Weyerhaeuser Timber Co||Apparatus for growing aerobic organisms|
|US3102082 *||Jul 17, 1961||Aug 27, 1963||John H Brewer||Apparatus and method for culturing micro-organisms|
|US3281307 *||Nov 5, 1962||Oct 25, 1966||Dow Chemical Co||Packing|
|US3740321 *||Apr 15, 1970||Jun 19, 1973||Smith Kline French Lab||Cell propagator|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US3948732 *||Aug 22, 1974||Apr 6, 1976||Instrumentation Laboratory, Inc.||Cell culture assembly|
|US4144136 *||Jun 6, 1977||Mar 13, 1979||Institut Armand-Frappier||Apparatus for cellular culture|
|US4184922 *||Nov 11, 1977||Jan 22, 1980||The Government Of The United States||Dual circuit, woven artificial capillary bundle for cell culture|
|US4228242 *||Aug 16, 1978||Oct 14, 1980||Chemap Ag||Arrangement for cultivating cells of animal and human tissues|
|US4264739 *||Jan 5, 1979||Apr 28, 1981||Merck & Co., Inc.||Sparger for cell culture system|
|US4296204 *||Jul 7, 1980||Oct 20, 1981||Merck & Co., Inc.||Use of motionless mixer as cell culture propagator|
|US4310630 *||Mar 13, 1980||Jan 12, 1982||Chemap Ag||Arrangement for cultivating cells of animal and human tissues|
|US4317886 *||Aug 11, 1980||Mar 2, 1982||Becton, Dickinson And Company||Multiple interior surface roller bottle|
|US4415670 *||Jun 22, 1981||Nov 15, 1983||Merck & Co., Inc.||Motionless mixer as cell culture propagator|
|US4514499 *||Feb 4, 1983||Apr 30, 1985||Corning Glass Works||Cell culture using a monolithic support|
|US4559299 *||Feb 4, 1983||Dec 17, 1985||Brown University Research Foundation Inc.||Cytotoxicity assays in cell culturing devices|
|US4689302 *||Apr 2, 1984||Aug 25, 1987||Amerace Corporation||Spiral designed reactor|
|US4810652 *||Jan 13, 1988||Mar 7, 1989||Becton, Dickinson And Company||Cell growth harvester for roller bottles|
|US4861725 *||Mar 29, 1988||Aug 29, 1989||Liau Ming Y||Mammalian cell culture apparatus|
|US4912058 *||Apr 27, 1989||Mar 27, 1990||Becton, Dickinson And Company||Roller bottle|
|US4919659 *||Dec 21, 1987||Apr 24, 1990||The Board Of Regents For The University Of Washington||Radio frequency plasma deposited polymers that enhance cell growth|
|US4937187 *||Feb 5, 1987||Jun 26, 1990||Brown University Research Foundation||Methods for separating malignant cells from clinical specimens|
|US5081035 *||Feb 11, 1991||Jan 14, 1992||The University Of Michigan||Bioreactor system|
|US5084393 *||Aug 28, 1989||Jan 28, 1992||Alena Rogalsky||Container for a biological culture|
|US5094955 *||Feb 15, 1990||Mar 10, 1992||Akzo N.V.||Device and method for detecting microorganisms|
|US5162229 *||Jul 19, 1991||Nov 10, 1992||Akzo N.V.||Device and method for enhanced recovery and detection of microbial growth in the presence of antimicrobial substances|
|US5164796 *||Feb 1, 1991||Nov 17, 1992||Akzo N.V.||Apparatus and method for detection of microorganisms|
|US5168058 *||Jun 27, 1990||Dec 1, 1992||Yeda Research And Development Company, Ltd.||Cell culture carriers and method of use|
|US5217876 *||Apr 7, 1992||Jun 8, 1993||Akzo N.V.||Method for detecting microorganisms|
|US5217899 *||Aug 24, 1990||Jun 8, 1993||The General Hospital Corporation||Cell stretching apparatus|
|US5240854 *||May 28, 1991||Aug 31, 1993||Berry Eric S||Continuous high-density cell culture system|
|US5272084 *||Dec 18, 1991||Dec 21, 1993||Corning Incorporated||Cell culture vessels having interior ridges and method for cultivating cells in same|
|US5348879 *||Feb 19, 1993||Sep 20, 1994||The General Hospital Corporation||Cell stretching method|
|US5376548 *||Jun 11, 1993||Dec 27, 1994||Fuji Photo Film Co., Ltd.||Bioreactor apparatus|
|US5512480 *||Jun 1, 1995||Apr 30, 1996||Baxter International Inc.||Flow-through bioreactor with grooves for cell retention|
|US5518895 *||Mar 24, 1995||May 21, 1996||Akzo N.V.||Device for detecting microorganisms using piezoelectric means|
|US5856175 *||May 21, 1996||Jan 5, 1999||Akzo Nobel N.V.||Device for detecting microorganisms|
|US5858769 *||May 15, 1996||Jan 12, 1999||Akzo Nobel N.V.||Device for detecting microorganisms|
|US5869329 *||Aug 25, 1997||Feb 9, 1999||Becton Dickinson And Company||Blood culture vial or bottle having an agitation paddle|
|US5939314 *||Jul 9, 1997||Aug 17, 1999||The United States Of America As Represented The Administrator Of The National Aeronautics And Space Administration||Distributed pore chemistry in porous organic polymers in tissue culture flasks|
|US6107085 *||Jul 3, 1998||Aug 22, 2000||Corning Incorporated||Self contained cell growth system|
|US6245557||Jan 5, 2000||Jun 12, 2001||Robert P. Fouts||Cell and protein harvesting assemblies and methods|
|US6569675||Jun 15, 2001||May 27, 2003||Corning Incorporated||Cell cultivating flask and method for using the cell cultivating flask|
|US6818438||Sep 30, 2003||Nov 16, 2004||Becton, Dickinson And Company||Culture flask|
|US6987019||Sep 3, 2004||Jan 17, 2006||Vitaly Rogalsky||Device for growing cells|
|US7449331||Sep 19, 2003||Nov 11, 2008||Whitley Kenneth W||Roller bottle|
|US7514256||Feb 11, 2005||Apr 7, 2009||Emilio Barbera-Guillem||Bioreactor for selectively controlling the molecular diffusion between fluids|
|US8066965||Sep 28, 2009||Nov 29, 2011||Co2 Solution Inc.||Process for recycling carbon dioxide emissions from power plants into carbonated species|
|US8158426||Jul 29, 2011||Apr 17, 2012||Wilson Wolf Manufacturing Corporation||Cell culture methods and devices utilizing gas permeable materials|
|US8158427||Jul 29, 2011||Apr 17, 2012||Wilson Wolf Manufacturing Corporation||Cell culture methods and devices utilizing gas permeable materials|
|US8168432||Feb 17, 2011||May 1, 2012||Wilson Wolf Manufacturing||Cell culture methods and devices utilizing gas permeable materials|
|US8277769||Oct 14, 2011||Oct 2, 2012||Co2 Solutions Inc.||Process for treating carbon dioxide containing gas|
|US8329458||Jun 4, 2010||Dec 11, 2012||Co2 Solutions Inc.||Carbonic anhydrase bioreactor and process for CO2 containing gas effluent treatment|
|US8329459||Nov 4, 2010||Dec 11, 2012||Co2 Solutions Inc.||Carbonic anhydrase system and process for CO2 containing gas effluent treatment|
|US8329460||Apr 7, 2011||Dec 11, 2012||CO2 Solutions, Inc.||Carbonic anhydrase bioreactor and process|
|US8415144 *||Aug 16, 2006||Apr 9, 2013||Wilson Wolf Manufacturing||Cell culture methods and devices utilizing gas permeable materials|
|US8435479||Aug 23, 2012||May 7, 2013||Co2 Solutions Inc.||Process for treating carbon dioxide containing gas|
|US8518692||Jul 8, 2009||Aug 27, 2013||Wilson Wolf Manufacturing Corporation||Gas permeable cell culture device and method of use|
|US8551740 *||Dec 21, 2011||Oct 8, 2013||Food Industry Research And Development Institute||Bioreactor and method for producing microbial cellulose|
|US8697443||Apr 2, 2010||Apr 15, 2014||Wilson Wolf Manufacturing Corporation||Cell culture methods and devices utilizing gas permeable materials|
|US8809044||Dec 7, 2007||Aug 19, 2014||Wilson Wolf Manufacturing Corporation||Highly efficient gas permeable devices and methods for culturing cells|
|US8871485||Jun 22, 2011||Oct 28, 2014||University Of Florida Research Foundation, Inc.||Modified carbonic anhydrase enzymes and their use in carbon dioxide sequestration and elimination|
|US9255243||Oct 8, 2004||Feb 9, 2016||Wilson Wolf Manufacturing Corporation||Cell culture methods and devices utilizing gas permeable materials|
|US9290730||Apr 16, 2014||Mar 22, 2016||Corning Incorporated||Multilayered cell culture apparatus|
|US9410114||Jul 27, 2015||Aug 9, 2016||Wilson Wolf Manufacturing||Cell culture methods and devices utilizing gas permeable materials|
|US9441192||Jul 27, 2015||Sep 13, 2016||Wilson Wolf Manufacturing||Cell culture methods and devices utilizing gas permeable materials|
|US20040029266 *||Aug 9, 2002||Feb 12, 2004||Emilio Barbera-Guillem||Cell and tissue culture device|
|US20040191895 *||Sep 19, 2003||Sep 30, 2004||Whitley Kenneth W.||Roller bottle|
|US20060180529 *||Feb 11, 2005||Aug 17, 2006||Emilio Barbera-Guillem||Bioreactor for selectively controlling the molecular diffusion between fluids|
|US20060246564 *||Apr 27, 2006||Nov 2, 2006||Carmen Parent||Immobilized biological material with improved functionality and method for producing the same|
|US20070254356 *||Aug 16, 2006||Nov 1, 2007||Wilson Wolf Manufacturing Corporation||Cell culture methods and devices utilizing gas permeable materials|
|US20080227176 *||Dec 7, 2007||Sep 18, 2008||Wilson John R||Highly efficient gas permeable devices and methods for culturing cells|
|US20100021981 *||Sep 28, 2009||Jan 28, 2010||Sylvie Fradette||Process and a plant for recycling carbon dioxide emissions from power plants into useful carbonated species|
|US20100248323 *||Jun 4, 2010||Sep 30, 2010||Carmen Parent||Carbonic anhydrase bioreactor and process for CO2 containing gas effluent treatment|
|US20100317066 *||Aug 6, 2009||Dec 16, 2010||Food Industry Research And Development Institute||Bioreactor and method for producing microbial cellulose|
|US20110045576 *||Nov 4, 2010||Feb 24, 2011||Carmen Parent||Carbonic Anhydrase System and Process for CO2 Containing Gas Effluent Treatment|
|US20110129923 *||Feb 17, 2011||Jun 2, 2011||Wilson John R||Cell culture methods and devices utilizing gas permeable materials|
|US20110183397 *||Apr 7, 2011||Jul 28, 2011||Co2 Solution Inc.||Carbonic Anhydrase Bioreactor and Process|
|US20120094334 *||Dec 21, 2011||Apr 19, 2012||Food Industry Research And Development Institute||bioreactor and method for producing microbial cellulose|
|DE3413707A1 *||Apr 12, 1984||Oct 17, 1985||Skoda Rastislav Dr Med Vet||Process for the mass cultivation of cells in lamellar chambers|
|EP0289666A1 *||Apr 3, 1987||Nov 9, 1988||Yeda Research And Development Company Limited||Cell culture carriers etc.|
|EP0345415A1 *||Feb 15, 1989||Dec 13, 1989||Becton Dickinson and Company||Expanded surface roller bottle|
|EP0481820A2 *||Oct 18, 1991||Apr 22, 1992||Costar Corporation||Continuous high-density cell culture system|
|EP0481820A3 *||Oct 18, 1991||Jun 10, 1992||Costar Corporation||Continuous high-density cell culture system|
|WO1984003047A1 *||Jan 12, 1984||Aug 16, 1984||Univ Brown Res Found||Cytotoxicity assays in artificial organs|
|WO1990002793A1 *||Aug 28, 1989||Mar 22, 1990||Alena Rogalsky||Container for a biological culture|
|WO1992005243A1 *||Sep 19, 1990||Apr 2, 1992||Scott Berry E||Continuous high-density cell culture system|
|WO1999002646A1 *||Jul 7, 1998||Jan 21, 1999||Corning Incorporated||Self contained cell growth system|
|U.S. Classification||435/293.2, 435/304.2, 435/299.1, 435/297.1|
|Cooperative Classification||C12M27/12, C12M27/20, C12M29/06, C12M25/02|
|European Classification||C12M27/20, C12M29/06, C12M27/12, C12M25/02|