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Publication numberUS3014024 A
Publication typeGrant
Publication dateDec 19, 1961
Filing dateMar 19, 1958
Priority dateMar 19, 1958
Publication numberUS 3014024 A, US 3014024A, US-A-3014024, US3014024 A, US3014024A
InventorsEmanuel R Lieberman, Irving B Oneson
Original AssigneeJohnson & Johnson
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Collagen film
US 3014024 A
Abstract  available in
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Claims  available in
Description  (OCR text may contain errors)

United rates Patent @ffice Patented Dec. 19, 1961 3,014,024 COLLAGEN FILM Emanuel R. Lieberman and lrving B. Oneson, Somerville, N.J., assignors to Johnson & Johnson, a corporation of New Jersey No Drawing. Filed Mar. 19, 1958, Ser. No. 722,376 2 Claims. (Cl. 260-117) The present invention relates to a highly oriented collagen film of uniform thickness, characterized by an eX- ceptional tensile strength in the direction of orientation and to a method of preparing the collagen film.

Films of collagen are customarily prepared by casting (pouring) a fluid dispersion of collagen fibers on a fiat or screened surface and permitting the dispersing media to evaporate. In general, one or two days are required to completely evaporate the dispersing media at room temperature, the residual film being uneven and varying widely in cross-section. The prior art collagen films have not been uniform in thickness because of the viscous nature of the collagen dispersions and the non-uniform manner of drying. Moreover, since the collagen dispersion is laid down in a fiat surface without the application of any external force, the individual collagen fibers in the dried film are in a random and disoriented state.

Attempts to speed up the process described above by elevating the temperature results in denaturation and degradation of the collagen fibers to such a degree that gelatin films are obtained in place of the desired collagen films. Removal of the liquid phase in a vacuum is also impractical as the viscous dispersion foams and the resulting film has a rough and uneven surface. Blowing air over the collagen dries the surface rapidly, but the dried surface film then interferes with evaporation of the solvent trapped beneath this surface layer.

It is an object, therefore, of the present invention to substantially reduce the time required in the manufacture of collagen films.

It is a further object of the present invention to produce a clear collagen film that is extremely uniform in thickness.

, -t is also an object of the present invention to pro-- duce a dry uniform collagen film at least 5 mills in thickness.

Still another object of the present invention is to manufacture a collagen film characterized by a substantial orientation of the collagen fibers in a single direction and an improved tensile strength in the direction of orientation.

Another object of the present invention is to provide a process that will enable the operator to add plasticizers and/or tanning agents to the collagen film after it has been formed.

It has now been discovered that superior collagen films may be obtained by centrifuging a uniform collagen dispersion of comparatively low viscosity. A basket centrifuge is particularly well adapted to the present process, and for ready removal of the dried collagen film, a filter cloth is placed into the basket centrifuge prior to addition of the collagen dispersion.

The collagen dispersion that is suitable for the present invention should contain collagen fibers in a pure and undenatured state. Such a dispersion may be obtained by swelling collagen in aqueous acid solutions and removing the associated impurities that do not swell by filtration. The preparation of a collagen dispersion that is satisfactory for the practice of the present invention has been described in the Salo Patent No. 2,598,608. The concentration of the collagen fibers in the dispersion should preferably be maintained below about 1% as higher concentrations in the neighborhood of 2% 01' above are too viscous to give satisfactory films unless a special type of centrifuge is employed that has an interior blade to distribute the dispersion. Excellent results have been obtained with a dispersion containing 0.5% by weight collagen fibers.

The following examples illustrate procedures suitable for the production of collagen films from collagen fiber dispersions, but are not intended to limit the scope of this invention.

Example I Beef tendon from freshly killed steers is trimmed free of fat and other extraneous tissues. The cleaned tendon is sliced and the slices are added to about 20 volumes of 2.55.0% acetic acid. The mixture is stirred for approximately four hours, during which time the collagen is swollen. The mixture is then diluted with an addition- 211 volumes of Water to facilitate removal of unswollen particles by filtration. The diluted dispersion is filtered under pressure through a ZO-mesh stainless steel screen. The filtered liquid at this stage contains approximately ().1% collagen and small unswollen particles that are not removed by the first filtration step. These impurities may be removed by additional filtration through successively finer screens or by centrifuga'- tion.

The dilute dispersions of pure collagen fibers is next treated with Normal ammonium hydroxide to neutralize all of the acetic acid (pH 7.0). The collagen fibers that are precipitated by the ammonium hydroxide are thoroughly washed in distilled water to remove all traces of salts and the washed fibers are redispersed in an aqueous acid solution containing 6 grams of malonic acid per liter. The dispersion so obtained contains 0.5% by weight collagen fibers.

Example 11 A canvas filter cloth is wetted down with concentrated ammonia and placed into a basket centrifuge 4 /2 inches in diameter. Two hundred and fifty cubic centimeters of the 0.5% aqueous collagen dispersion described in Example I above is added to the centrifuge, which is rotated at just sufficient speed to bring the dispersion evenly up the sides of the basket onto the canvas cloth. The film so formed is then sprayed with about 20 cc.

of ammonia to precipitate the collagen fibers and the The tensile strength of this film is measured perpen dicular to and parallel with the direction of fiber orientation.

Strips of the film exactly one-half inch in I width are tested on an Instron tester and compared with a control film of the same width obtained by casting the dispersion of Example I on a fine wire mesh base. The results indicate a distinct orientation of collagen fibers as a result of the centrifugal force on the collagen dispersion and the subsequently precipitated fibers.

Example III The procedure of Example II is repeated using an 0.5% aqueous dispersion prepared from the sheath tendon of cattle swollen in an 0.1% malonic acid solution. The dispersion is added to the centrifuge basket and the speed immediately brought to 1750 r.p.m. After two minutes, concentrated ammonia is sprayed on the dispersion and the film is sprayed again after ten minutes. The speed is maintained at 1750 r.p.m. for 35 minutes, raised to 2600 r.p.m. for 40 minutes and finally to 3500 r.p.m. for 25 minutes. The speed is reduced to 2600 r.p.m. for 20 minutes, during which time the film is dried by means of a draft of Warm air. This film has a thickness of 2.5 mills with a perpendicular tensile strength of 9.5 pounds and a parallel tensile strength of 19.9 pounds.

Example IV The perforated basket of a large centrifuge 20 inches in diameter is lined with an Orlon filter cloth saturated with concentrated ammonium hydroxide. This centrifuge is rotated at 800 r.p.m. while 4 liters of an 0.47% collagen dispersion prepared as described in Example I above, is added slowly to the centrifuge over a period of ten seconds. The surface of the dispersion layer is then sprayed immediately with concentrated ammonia, and is sprayed two more times at one-hour intervals. The speed of the centrifuge is then increased to 1500 r.p.m. and the centrifuge is allowed to spin at this speed for an additional three hours. Finally, a current of air at 35 C., is passed into the centrifuge for half an hour. A very thin film is obtained, approximately 1.0 mil in thickness. The tensile strength of this film is indicated on the Instron tensile tester is 5.5 pounds in a direction perpendicular to the fiber orientation and 11.0 pounds in a direction parallel to the fiber orientation.

Example V The procedure of Example II is repeated and the film, after spraying with 20 cc. of ammonia and spinning for 1 hours at 2500 r.p.m., is sprayed with 20 cc. of a 2% formaldehyde solution. The basket is allowed to spin at a speed of 2500 r.p.m. for half an hour and then sprayed again with an additional 25 cc. of 2% f0rmal dehyde solution. One-half hour after the second addition of formaldehyde, the speed of the centrifuge is increased to 3500 r.p.m. and a draft of warm air is directed into the basket until the collagen film is completely dry. The dried film is easily removed from the canvas cloth and has properties similar to those obtained when the film is tanned in a formaldehyde tanning bath. In a similar manner, aqueous solutions of known plasticizers such as glycerol or sorbitol can be sprayed directly into the centrifuge to produce a plasticized collagen film.

Strips of collagen film prepared by the procedure described above may be sterilized and used as a surgical suture or ligature for the purposes described in United States Patent No. 2,039,145. Such films may be used in surgery for hernia repair and may be formed into tubes for arterial graphs.

The collagen films of the present invention are also useful in wrapping meat products such as ground sausage.

While the invention has been described with particular reference to specific embodiments, it is to be under stood that it is not to be limited thereto, but it is to be construed broadly and restricted solely by the scope of the appended claims.

What is claimed is:

1. A collagen film of uniform thickness characterized by a substantial orientation of collagen fibers in a single direction and a tensile strength in the direction of orientation at least about 1.6 times the tensile strength in a direction perpendicular to the direction of orientation; produced by centrifuging an acid dispersion of collagen fibers to form a film, spraying the film with an alkaline reagent to neutralize the acid and continuing to centrifuge until the dispersing liquid has been substantially removed from the film and removing the film so obtained from the centrifuge.

2. A collagen film as described in claim 1, the thickness of which is at least 5 mils.

References Cited in the file of this patent UNITED STATES PATENTS 669,119 Krank Mar. 5, 1901 925,328 Goldsmith June 15, 1909 2,039,262 Schulte Apr. 28, 1936 2,058,835 Schulte Oct. 27, 1936 2,114,220 Freudenberg et al. Apr. 12, 1938 2,280,636 Kraft Apr. 21, 1942 2,518,504 Stott Aug. 15, 1950 2,598,608 Salo et al. May 27, 1952 2,747,228 Braun et al. May 29, 1956 2,842,799 Politzer July 15, 1958 FOREIGN PATENTS 133,428 Sweden Oct. 30, 1951

Patent Citations
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Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3152203 *May 31, 1961Oct 6, 1964Dow Chemical CoPreparation of collagen films
US3272204 *Sep 22, 1965Sep 13, 1966Ethicon IncAbsorbable collagen prosthetic implant with non-absorbable reinforcing strands
US3285903 *May 24, 1962Nov 15, 1966American Cyanamid CoCollagen film
US3723244 *Jan 18, 1971Mar 27, 1973Atomic Energy CommissionFibrous fibrin sheet and method for producing same
US4621482 *Apr 18, 1985Nov 11, 1986Naturin-Werk Becker & Co.Method and apparatus for forming netted meat products wrapped in an edible collagen film
US4670014 *Feb 21, 1985Jun 2, 1987Bioetica S.A.Implantable, biocompatible reservoirs permitting conservation, cellular culturing, or controlled liberation of an active principle
US4716713 *Aug 20, 1986Jan 5, 1988Naturin-Werk Becker & Co.Method and apparatus for forming netted meat products wrapped in an edible collagen film
US4719116 *Aug 27, 1986Jan 12, 1988Naturin-Werk Becker & Co.Wrapping in an edible film and compression molding
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US6916910Nov 28, 2001Jul 12, 2005Bioscience ConsultantsCosmetic, drugs; extraction, precipitation, washing
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US7063610Jun 15, 2004Jun 20, 2006Poly-Clip System Corp.Apparatus and method to net food products in shirred tubular casing
US7214765 *Jul 8, 2005May 8, 2007Kensey Nash CorporationApplying a gyroscopic force to a low concentration slurry of polymer fibers, evenly dispersed and randomly oriented throughout the volume of the suspension fluid, to cause the fibers to flocculate and migrate through the fluid and amass at a center point where they interlace with one another
US7404758Oct 28, 2003Jul 29, 2008Poly-Clip System Corp.Apparatus and method to net food products in shirred tubular casing
US7429349Feb 20, 2004Sep 30, 2008Naturin Gmbh And Co.Method of perforating a flat film based on collagen
US7910690Apr 27, 2007Mar 22, 2011Kensey Nash Bvf Technology, LlcHigh density fibrous polymers suitable for implant
US8109995Aug 8, 2008Feb 7, 2012Colibri Heart Valve LlcPercutaneously implantable replacement heart valve device and method of making same
US8188229 *Feb 14, 2011May 29, 2012Kensey Nash Bvf Technology, LlcHigh density fibrous polymers suitable for implant
US8308797Jul 10, 2004Nov 13, 2012Colibri Heart Valve, LLCPercutaneously implantable replacement heart valve device and method of making same
US8361144Mar 1, 2011Jan 29, 2013Colibri Heart Valve LlcPercutaneously deliverable heart valve and methods associated therewith
US8633299May 25, 2012Jan 21, 2014Kensey Nash Bvf Technology LlcHigh density fibrous polymers suitable for implant
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Classifications
U.S. Classification530/356, 264/86, 8/127.5, 530/840, 264/311
International ClassificationC08H1/00, A23L1/317, B29C55/00, C08L89/00
Cooperative ClassificationB29C55/00, C08H1/00, A23L1/317, Y10S530/84, C08H1/06
European ClassificationB29C55/00, A23L1/317, C08L89/00, C08H1/00