Collagen materials and methods for obtaining same
10004825 ยท 2018-06-26
Assignee
Inventors
Cpc classification
Y10T442/20
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
C07K14/78
CHEMISTRY; METALLURGY
A61F2/0077
HUMAN NECESSITIES
Y10T428/1348
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
International classification
C07K14/78
CHEMISTRY; METALLURGY
A61L27/58
HUMAN NECESSITIES
A61F2/00
HUMAN NECESSITIES
Abstract
The invention relates to novel collagen materials and, specifically, collagen membranes, tubes and threads. Said materials combine enhanced properties of resilience and strength. The invention also relates to a method for preparing collagen materials using acid fibrous collagen comprising coagulation and, optionally, cross-linking of the collagen in the presence of ammonia gas.
Claims
1. A collagen material comprising one of a collagen membrane, a collagen film, a collagen thread, a collagen tube, a collagen sponge or a collagen gel, wherein said collagen material comprises a density between 12 mg/cm.sup.2 and 16 mg/cm.sup.2, a swelling ratio less than 6, a suture retention strength greater than 1N, a yield strength greater than 4 MPa and a percentage of enzymatic degradation by trypsin less than 35%.
2. The collagen material of claim 1, wherein said collagen material comprises homogenous cross-linking with a difference between crosslinking on the outside surface and cross-linking inside the material of less than or equal to 25%.
3. The collagen material of claim 1, wherein said collagen material has an increase in denaturation temperature greater than or equal to 3 C. in relation to non-cross-linked collagen material.
4. The collagen material of claim 1, wherein said collagen material has an increase in denaturation temperature in relation to non-cross-linked material of at least 5%.
5. The collagen material of claim 1, wherein said collagen material is a collagen membrane having a length and width greater than 5 cm.
6. A collagen membrane comprising a dry thickness between 30 m and 200 m, a density between 12 mg/cm.sup.2 and 16 mg/cm.sup.2, a swelling ratio less than 6, a suture retention strength greater than 1N, a yield strength greater than 4 MPa and a percentage of enzymatic degradation by trypsin less than 35%.
7. The collagen membrane of claim 6, wherein said collagen membrane consists of a non-porous collagen monolayer with a dry thickness between 50 m and 150 m.
8. The collagen membrane of claim 6, wherein said collagen membrane comprises a dry thickness between 80 m and 120 m.
9. The collagen membrane of claim 6, wherein said collagen membrane comprises a swelling ratio between 4 and 6, a suture retention strength between 1N and 2.5 N, a yield strength between 4 MPa and 7 MPa and a percentage of enzymatic degradation by trypsin between 20% and 35%.
10. A composite material comprising a textile covered on one of its sides by a collagen material comprising a density between 12 mg/cm.sup.2 and 16 mg/cm.sup.2, a swelling ratio less than 6, a suture retention strength greater than 1N, a yield strength greater than 4 MPa and a percentage of enzymatic degradation by trypsin less than 35%.
11. A composite material comprising a textile covered on each of its sides by a collagen material comprising a density between 12 mg/cm.sup.2 and 16 mg/cm.sup.2, a swelling ratio less than 6, a suture retention strength greater than 1N, a yield strength greater than 4 MPa and a percentage of enzymatic degradation by trypsin less than 35%.
12. The composite material of claim 11, wherein said textile is embedded in said collagen material such that both sides of the textile is covered by said collagen material.
13. The collagen material of claim 1, wherein said collagen sponge is in the form of a powder.
Description
DETAILED DESCRIPTION OF THE INVENTION
(1) The invention thus relates to a method for extracting collagen from tendons of young animals leading to a collagen whose fiber length and elasticity, during its use in the manufacture of medical devices, make it possible to obtain materials that are mechanically strong, elastic, suturable and conformable.
(2) Thus, one object of the invention relates to a method for preparing acidic fibrous collagen of tendons comprising the following steps: a) swelling tendons of pig, calf, lamb, foal or mixtures thereof in 0.1 M to 0.5 M aqueous acetic acid solution for at least 7 days, b) mechanically grinding the tendons to obtain an aqueous suspension, c) precipitating and washing the fibrous collagen from the aqueous suspension of step b), d) dehydrating the collagen.
(3) Preferably, the extracting of fibrous collagen is carried out from tendons of animals younger than 10 months, and more preferentially from tendons of pigs younger than 10 months.
(4) The first step thus comprises harvesting tendons from the feet of pigs younger than 10 months (tendons may also be harvested from calves, lambs and foals), cleaning, thoroughly removing conjunctive tissues and other non-tendinous tissues and then cutting the tendons into approximately 1 cm-long pieces and rinsing them with water.
(5) Swelling is carried out for at least 7 days and up to 15 days, preferentially 15 days, in a 0.1 M to 0.5 M, preferentially 0.3 M, acetic acid bath under stirring in a ratio of 1 kg of tendons in a volume between 20 l and 30 l, preferentially 25 l.
(6) The second step consists of gentle grinding, enabling the release of long tendon fibers from the swollen tendon fragments. The grinding of a volume of swelling bath containing pieces of swollen tendons is carried out for example for 2 min at 3000 rpm and then a series of steps, each comprising dilution of the medium with water followed by grinding under the same conditions, are carried out until a paste with a dry matter concentration between 4.8 g/kg and 6.5 g/kg is obtained.
(7) The third step consists of precipitating fibrous collagen from the paste that resulted from the grinding, and then purifying it according to standard methods. This step may comprise one or more precipitations using sodium chloride at a final concentration between 0.45 M and 1.2 M, more particularly at a concentration of 0.6 M, and one or more steps of washing the precipitated collagen in a 0.45 M to 1.2 M, preferentially 0.6 M, NaCl solution. In general, the method also comprises a step of viral inactivation in 1 N sodium hydroxide solution at 20 C. for 1 hour. By its hydrolytic action on non-collagenous proteins, this step constitutes additional purification. At the end of this step, new washes with 0.6 M NaCl are carried out. In order to dehydrate the collagen and to remove salts, acetone treatment is then carried out and a dry fiber is thus obtained.
(8) This particular method applied to tendons leads to collagen that is different from existing collagens in that it is composed of long fibers without containing pieces of tissues and it preserves a portion of soluble collagen.
(9) The invention thus also relates to acidic fibrous collagen of tendons that may be obtained by the methods according to the invention.
(10) The invention also relates to fibrous collagen such that in 0.1% aqueous solution less than 20%, 15% or 10% of the fibers contained in the solution are retained on a 50 m nylon filter and more than 20%, 25% or 30% cross a 5 m nylon filter.
(11) The protocol for measuring fractions of fibrous collagen obtained according to the invention, of less than 5 m and greater than 50 m in size, is as follows: Prepare 0.1% aqueous collagen solution under magnetic or mechanical stirring for 16 to 24 hours (500 mg used). Deposit the solution on a 5 m or 50 m nylon mesh mounted on a 9 cm-diameter circular support. The molecules diffuse in the mesh at atmospheric pressure. The pressure exerted on the mesh is considered negligible as the height of the water column does not exceed 4 cm for a 63 cm.sup.2 section. The solution on the mesh is stirred with a flat square blade that does not scrape across the fabric but is positioned a few millimeters (at most 5) above the fabric. Stirring speed is 80 rpm. The width of the blade is 7 cm. It is positioned in the center of the circular support. After the collagen solution stops flowing through the mesh, the retentate is washed with 50 ml of 0.05 M acetic acid while observing pressure differentials until the flow stops. This operation is repeated three times. The fractions are then recovered (filtrate and retentate) and the collagen is precipitated from each fraction by adding NaCl in order to achieve a final concentration of 0.6 M.
(12) The precipitate is then collected by centrifugation or filtration and then dehydrated with acetone, dried under reduced pressure and weighed.
(13) The invention also relates to methods for forming acidic collagen for preparing a collagen material.
(14) In a first embodiment, the invention relates to a method for preparing a collagen material characterized in that it comprises the following steps: a) preparing an aqueous solution comprising 0.05% to 3% by weight of collagen in acid form, b) molding or casting the aqueous collagen solution, c) coagulating the aqueous collagen solution by treating with ammonia gas, d) removing the ammonia and obtaining the collagen material.
(15) In a particularly advantageous embodiment, the invention thus relates to a method for preparing a collagen material characterized in that it comprises the following steps: a) preparing an aqueous solution of collagen in acid form, b) adding an aldehyde cross-linking agent that is non-reactive at acidic pH, c) molding or casting the aqueous collagen solution, d) coagulating and cross-linking the aqueous collagen solution by treating with ammonia gas, e) removing the ammonia and obtaining the collagen material.
(16) The first step of the methods according to the invention consists of preparing an aqueous collagen solution. Aqueous collagen solution also refers to a collagen suspension.
(17) The method according to the invention uses collagen in acid form. Collagen in acid form refers to collagen in which most of the carboxylic functional groups are protonated and which has an acidic pH in solution or suspension in water.
(18) Preferably, the method for preparing the collagen material according to the invention uses acidic fibrous collagen.
(19) Fibrous collagen refers to collagen in which the molecules of collagen are not individualized or are poorly individualized, and which is thus composed of fibers and fibrils made up of collagen molecules naturally linked together by weak and covalent bonds, and by aggregates of such structures. Fibrous collagen, notably, consists of large particles (mainly greater than 5 m when hydrated) which give a homogeneous suspension by dispersion in aqueous medium.
(20) Fibrous collagen may notably be fibrous collagen of skin or fibrous collagen of tendons. Fibrous collagen of skin comprises relatively short fibers due to the natural organization of the tissue, acid-soluble collagen and small aggregates. Collagen of tendons comprises long fibers and very little soluble collagen.
(21) Preferably, the methods according to the present invention are implemented with fibrous collagen of tendons, preferably with fibrous collagen of pig tendons and more preferentially with collagen of tendons of pigs younger than 10 months.
(22) Advantageously, the methods of the present invention use acidic fibrous collagen of tendons prepared according to the method described above and with long fibers.
(23) The first step thus consists of dissolving the collagen in water. It is carried out according to standard methods described in the literature. When the collagen is an acidic fibrous collagen, this step enables the suspension of fibers surrounded by microfibrillar collagen and so-called soluble collagen that have maintained a structure necessary to fibrillation.
(24) Typically, the aqueous collagen solution comprises between 0.05% and 3% by weight of collagen and preferably between 0.05%, 0.1%, 0.8%, 1%, 1.5%, 2%, 2.5% and 3% of collagen. Advantageously, the aqueous solution comprises 0.8% by weight of collagen. Said dissolution is usually carried out in water by mechanical stirring, preferably under reduced pressure.
(25) The suspension or solution may also be heated at a temperature between 30 C. and 100 C. for 2 minutes to 20 minutes to partially or completely denature the collagen.
(26) The methods according to the invention make it possible to obtain various collagen materials according to the form selected during molding or casting. The collagen material may thus notably take the form of a membrane, a matrix, a film, a thread, a gel, a tube or a sponge.
(27) The casting or molding of an aqueous collagen solution is well known to the person skilled in the art and is described in the literature. The second step is thus the casting or molding of the collagen solution into molds, wherein the thickness varies according to the material desired and according to the surface of the mold.
(28) Collagen membranes are two-dimensional materials that result from the drying in a flat mold of a homogeneous suspension or a collagen solution containing a proportion of fibers and fibrils. The collagen may or may not be cross-linked. The concentration of the dried suspension determines the thickness of the final material, which may range from a few microns to several hundred microns.
(29) A collagen film is a two-dimensional material that results from the drying in a flat mold of a homogeneous collagen solution. The collagen may or may not be cross-linked. The concentration of the dried solution determines the thickness of the final material. Films and membranes may be folded to form sleeves which may be closed if need be by sutures or glue. The thickness may vary from a few microns to several hundred microns. A collagen tube is a hollow, three-dimensional cylindrical object whose walls may be a collagen film or membrane. Tubes may be obtained by molding around a mold or by extrusion. The collagen may or may not be cross-linked. Wall thickness is determined by the quantity of collagen deposited on the molds or used in the extrusion solution.
(30) A collagen thread is a large assembly of collagen whose mechanical strength is sufficient to be part of the composition of a larger multi-stranded thread, a composite or non-composite textile or another collagen material.
(31) A collagen sponge may be obtained by freeze-drying a collagen solution or suspension (or a mixture of the two). Before or after freeze-drying, the collagen may be cross-linked. Freeze-drying generally leads to three-dimensional materials or to powders.
(32) In order to obtain a membrane or a film, the collagen solution may be deposited on a flat mold to obtain a two-dimensional material after drying the solution or suspension. The film or membrane may be obtained by evaporating the solvent.
(33) Collagen tubes are obtained by depositing the solution or suspension on a cylindrical mold and drying or freeze-drying.
(34) In order to obtain sponges, the solvent may be removed by freeze-drying and not by evaporating the solvent in liquid form.
(35) It was previously known to use ammonia for coagulating and forming collagen but in general known methods involved the use of ammonia to coagulate a solution or a gel during extrusion, for example. Treating with ammonia was then very rapid and in baths. The method according to the invention rests on the diffusion rate of ammonia in the collagen solution, a rate that primarily depends on the concentration of this base on the surface of the solution. The collagen and the ammonia are left in contact for a period of time sufficient to enable coagulation of the collagen but also its fibrillation throughout the totality of the treated solution. This has led to the preparation of collagen materials with mechanical properties that are not obtained with the methods of the state of the art, in terms of tensile strength, elasticity and suture retention strength.
(36) The third step is thus coagulating the collagen by treating it with ammonia for a period of time sufficient to enable both the coagulation and the fibrillation of the collagen. Typically, the ammonia treatment is carried out for a period of 4 hours, 8 hours, 12 hours, 24 hours, 36 hours or 48 hours. Preferably, the treatment period is greater than 24 hours or 36 hours.
(37) The quantity of ammonia will be adjusted to increase the pH of the acidic-pH collagen gel to a pH of at least greater than 8. Indeed, cross-linking of the collagen begins when the collagen gel reaches a pH at least greater than 8. This long treatment enables a progressive increase in the pH of the collagen, which not only leads to its coagulation but also to its fibrillation. Depending on the length of the collagen fibers used, said fibrillation forms a meshwork which gives the materials both mechanical strength and elasticity.
(38) In a preferred embodiment, ammonia gas is prepared from an ammonia solution from which it is released. A suitable quantity of ammonia gas is generally obtained from at least 30% ammonia solution at a temperature between 10 C. and 25 C. Preferably, this step is carried out in a hermetically sealed enclosure in such a way that the ammonia gas spreads inside the enclosure and comes into contact with the collagen solution, which is not in contact with the ammonia solution.
(39) The collagen gel obtained is treated to remove excess ammonia and is either preserved as-is or in a dehydrated state. To that end, the gel may be placed in an enclosure equipped with a system to remove moisture and/or with an ammonia absorber. After removing excess ammonia, the membranes, films and tubes are obtained by dehydrating the gel under a stream of dry air, whereas sponges, 3-D matrices and tubes are obtained by freeze-drying the gel. Gels may be maintained in a hydrated state.
(40) In said method for preparing collagen materials, the fibrillation process takes place in a highly viscous liquid medium. Said fibrillation occurs from the outside toward the inside of the solution and progresses with the increase in pH due to the diffusion of ammonia. It occurs when the pH reaches a value greater than 4 or 5. The advantage of the ammonia vapor method is that the material does not need to be immersed in neutralization solutions, which increases time savings, profitability and homogeneity.
(41) When it is desired to increase the resorption time of a collagen medical device and also to strengthen its mechanical properties, the collagen material may be cross-linked. There are many collagen cross-linking methods well known to the person skilled in the art. They are grouped into two main categories: physical cross-linking such as, for example, thermal dehydration, and chemical cross-linking by adding or contacting with cross-linking agents. The most well-known collagen cross-linking agents are aldehyde agents, in particular formaldehyde and glutaraldehyde. Said cross-linking methods may of course be used on the collagen materials obtained above.
(42) Thus, collagen and collagen materials may thus be cross-linked in order to increase their mechanical strength. Said cross-linking step is thus carried out after the last step d) of the method leading to the obtaining of the collagen material. It is carried out, for example, by immersing the collagen material in a bath comprising a cross-linking agent selected from formaldehyde, glutaraldehyde, oxidized glycogen and oxidized amylopectin.
(43) Particularly advantageously, cross-linking may in contrast take place in a single step but in a sequential manner with coagulation and fibrillation of the collagen. In this case, an aldehyde agent that does not react with collagen at acidic pH is added to the starting collagen solution and then ammonia treatment is carried out to obtain a pH at least greater than 8.
(44) The aldehyde cross-linking agent is preferably selected from polysaccharides, more particularly oxidized polysaccharides. Preferably, the aldehyde cross-linking agent is selected from oxidized glycogen and oxidized amylopectins. Cross-linking agents that may be used in the methods according to the present invention are, for example, oxidized starch, oxidized dextran and oxidized cellulose known to the person skilled in the art. Preferentially, the aldehyde cross-linking agent is oxidized glycogen.
(45) The cross-linking agent is added in proportions ranging from 0.05, 0.1, 0.5, 1, 1.5, 2, 2.5, 3, 3.5, 4, 4.5 to 5 for the CHO ratio of the aldehyde cross-linking agent on the NH.sub.2 of the collagen. The proportions of cross-linking agent may be adjusted by the person skilled in the art according to the cross-linking rate desired. The quantity of cross-linking agent to be added to the collagen solution may thus be determined using the general knowledge of the person skilled in the art.
(46) Preferably, a concentrated (15%) aqueous solution of the selected oxidized polysaccharide is thus prepared. The oxidation rate and the quantity of cross-linking agent to be added are determined according to the resorption desired and the mechanical properties sought. It is then possible to add the cross-linking agent to the collagen in a perfectly controlled and reproducible quantity (unlike cross-linking by formaldehyde vapor, for example, or immersion in baths). Here, only the added cross-linking agent may react. The cross-linking solution is added to the collagen solution before casting or forming, i.e., at the end of homogenization under reduced pressure. The resulting medium is a homogeneous mixture of collagen and cross-linking agent, although bonds between the two have not been created since the mixture has not reached basic pH. The subsequent steps are identical to those of the fibrillation of collagen, wherein fibrillation and cross-linking are carried out successively and in that order.
(47) The person skilled in the art will be able to adapt the quantity of ammonia and the exposure time to achieve the desired fibrillation and cross-linking.
(48) This step of the method according to the invention is remarkable for several reasons. Cross-linking by aldehyde polysaccharides has already been described in the literature (Gagnieu C H and Forest P O, EP0862468). Said cross-linking may be carried out either by immersing the materials to be cross-linked in oxidized polysaccharide solution or by adding oxidized polysaccharide to the material and then immersing the dry product in a bath enabling the cross-linking reaction (increase in pH). In general, the change in pH is carried out by a buffer. Taking into account the well-known principle of cross-linking (Maillard reaction.fwdarw.reaction of CHO groups of the cross-linking agent with NH.sub.2 groups of the collagen), changing the pH using bases that themselves have amine residues is avoided. Thus, in the presence of ammonia, the theory predicts that the oxidized polysaccharide will react with the amine of ammonia and consequently will be inactivated. Cross-linking thus cannot take place.
(49) In practice, it turns out that the presence of ammonia satisfactorily modifies the pH of the collagen gel to enable fibrillation but also cross-linking. In a completely surprising manner, cross-linking takes place at an effective rate because the Maillard reaction, which would have had to occur between the ammonia and the aldehydes of the cross-linking agent, thus inactivating the latter, is either absent, very weak, or not competitive with the cross-linking reaction between the aldehyde groups of the oxidized polysaccharide and the lysine amines of the collagen. This is demonstrated by the fact that materials cross-linked in this way are no longer soluble in acidic aqueous medium and have fewer degradations in contact with proteolytic enzymes than non-cross-linked materials, and by the fact that the mechanical properties of materials in hydrated form, and notably mechanical strength, are also improved in relation to non-cross-linked material.
(50) The invention also relates to collagen material that may be obtained by the methods according to the invention. Preferably, the collagen material is cross-linked. Said collagen material may, for example, consist of a collagen membrane, a collagen thread, a collagen tube, a collagen sponge or a collagen gel.
(51) The invention thus also relates to collagen films, threads and tubes that may be obtained by the methods according to the present invention. In one embodiment, the invention relates to collagen membranes that may be obtained by the methods according to the invention.
(52) The methods according to the invention enable the preparation of dry membranes of variable thickness ranging from a few microns to a few hundred microns. The thickness generally used to ensure guided cicatrization (conservation of cleavage planes) or tissue substitution in urologic, gynecologic, cardiac, thoracic, vascular, articular, digestive, plastic, spinal, neurological, orthopedic, trauma, dental, oral and maxillofacial surgeries, for guided cicatrization of tissues (dura mater, gums, bones, nerves, tendons, ligaments, viscera, pericardium, peritoneum, conjunctive tissues in general, dermis, muscle, cartilage) is between 30 m and 200 m.
(53) The invention thus relates to collagen membranes that may be obtained by the methods according to the invention that have a dry thickness between 30 m and 200 m. Preferably, said membranes are cross-linked.
(54) Advantageously, said membranes consist of a non-porous collagen monolayer with a dry thickness between 50 m and 150 m.
(55) In one embodiment, the object of the invention relates to collagen membranes that have a dry thickness between 80 m and 120 m, a density between 12 mg/cm.sup.2 and 16 mg/cm.sup.2, a swelling ratio less than 6, a suture retention strength greater than 1 N, a yield strength greater than 4 MPa and a percentage of enzymatic degradation by trypsin less than 35%.
(56) In a preferred embodiment, the invention relates to the collagen membranes described above with a swelling ratio between 4 and 6, a suture retention strength between 1 N and 2.5 N, a yield strength between 4 Mpa and 7 MPa and a percentage of enzymatic degradation by trypsin between 20% and 35%.
(57) Swelling ratio is measured as follows: 20 mg of material is immersed in 1 phosphate buffered saline, pH 7.4, for 60 minutes at 37 C. After the hour, excess water is removed with absorbent paper and the sample is weighed again. Swelling ratio is calculated by the ratio of the weight of the wet material to the weight of the dry material.
(58) Measurements of mechanical stress (suture retention strength and yield strength) are measured on a moistened 5 mm-wide test tube using a tensile strength test bench. Regarding suture retention strength, a braided 3-0 polyamide suture thread is passed through the membrane and then the maximum force applied that breaks the suture is measured using a tensile strength test bench.
(59) To determine enzymatic degradation by trypsin, fragments of material weighing between 10 mg and 20 mg are immersed in 3 ml of 1PBS, pH 7.6, and 500 units of trypsin are added to the sample. After 48 hours of degradation, the digested samples are collected, dehydrated and weighed. The loss of weight in relation to the starting weight is then calculated.
(60) The invention also relates to collagen membranes reinforced with a resorbable or non-resorbable textile. Said textile-reinforced membranes constitute a parietal reinforcement and are particularly suited to visceral and urogynecologic surgery or to a ligament patch to reinforce, extend or replace a ligament or a tendon.
(61) Thus, another object of the invention relates to a composite material comprising, or consisting of, a textile covered on one side by a collagen material as described above.
(62) It may notably be a textile bearing a collagen membrane according to the invention on one of its sides. Such prosthetic fabrics and methods for manufacturing same, for example, are described in U.S. Pat. No. 6,451,032.
(63) The fabric-reinforced collagen membranes according to the invention may further be manufactured according to methods well known to the person skilled in the art.
(64) In the context of the present invention, such a method may comprise the following steps: preparing an aqueous solution of collagen in acid form, adding an aldehyde cross-linking agent that is non-reactive at acidic pH, molding or casting the aqueous collagen solution, depositing the textile on the collagen, coagulating and cross-linking the aqueous collagen solution by treating with ammonia, removing the ammonia and obtaining the collagen material.
(65) Membranes reinforced on one side with a textile obtained according to the method above are particularly suited for parietal surgery.
(66) Alternatively, the method may comprise the following steps: preparing an aqueous solution of collagen in acid form, adding an aldehyde cross-linking agent that is non-reactive at acidic pH, molding or casting the aqueous collagen solution, including the textile in the collagen, coagulating and cross-linking the aqueous collagen solution by treating with ammonia, removing the ammonia and obtaining the collagen material.
(67) Textiles thus comprising a membrane according to the invention on both sides are particularly suited for ligament surgery, for example.
(68) Another object of the invention thus relates to a composite material comprising, indeed consisting of, a textile covered on two, notably on each, of its sides by a collagen material such as described above, wherein in particular the textile may be included in the collagen material.
(69) Other methods for combining a collagen material according to the invention with a textile are known to the person skilled in the art.
(70) The invention thus also relates to a collagen material according to the invention, notably a membrane, combined with a textile.
(71) The methods according to the invention also lead to the preparation of tubes to ensure the guiding of organs in nerve, tendon, ligament and vascular surgery. Membranes for this indication may also be rolled and closed in sleeve form by suture and/or glue.
(72) Lastly, the methods enable the preparation of porous or non-porous 3-D matrices greater than 200 m in thickness which enable, among other things, inoculation of cells prior to or at the time of surgical implantation of the material for applications in regenerative medicine, and which enable suturable and elastic patches for cardiac applications, dura mater regeneration and guiding of soft and hard tissue to be obtained.
EXAMPLES
Example 1
Production of acidic fibrous Collagen of tendons
(73) .fwdarw.Swelling of the Tendons
(74) One kilogram of tendons from the feet of pigs is cleaned to remove muscle and aponeurotic tissue. They are immersed in 25 l of 0.3 M aqueous acetic acid solution for 10 days at 20 C. (2 C.) under slow stirring.
(75) .fwdarw.Grinding of the Tendons
(76) Three liters of the suspension obtained is ground at 3000 rpm in a knife mill for 2 minutes. The medium is diluted with 2 l of water and then homogenized for 1 minute. The medium is filtered on a filter with a pore size of 200 m and the filtrate is adjusted with 0.6 M NaCl to precipitate the collagen.
(77) .fwdarw.Recovery of Collagen and Washes
(78) The suspension is filtered or centrifuged to separate the precipitate from the supernatant. The precipitate is collected and washed in 10 l of 0.6 M NaCl under stirring for at least 1 hour; the precipitate is collected again by filtration on fabric or centrifugation. The washing step may be carried out the number of times desired according to the desired purity of the final collagen (ideally twice).
(79) .fwdarw.Viral Inactivation and Washes
(80) The precipitated and spun-dry collagen is dissolved to 1% in water for 16 hours under stirring. The concentration of the medium is brought to 1 M NaOH and the solution is stirred for 1 hour at 20 C. At the end of the inactivation step, the solution is neutralized with 6 M hydrochloric acid until the collagen precipitates. The collagen is recovered by filtration or centrifugation. The collagen may be washed again in 10 l of 0.6 M NaCl and then collected by filtration on fabric or by centrifugation. The washing step may be carried out the number of times desired according to the desired purity of the final collagen (ideally twice).
(81) .fwdarw.Harvesting and Drying
(82) At the end of the purification process, the precipitated collagen is spin-dried and then dried in acetone baths. The collagen is finally dried under a controlled stream of air to remove residual acetone and then stored at 20 C., for example.
Example 2
Characterization of a batch of acidic fibrous collagen of tendons
(83) 603 mg of acidic fibrous collagen of tendons with a water content of 17.05% is dispersed in 500 ml of demineralized water for 16 hours under magnetic stirring. A fabric with a pore size of 50 m is placed on a 9 cm-diameter cylindrical support above a container. A volume of collagen solution is poured on the fabric in such a way as not to exceed 4 cm in height. A 7 cm-diameter blade is placed 2 mm from the fabric and rotated at 80 rpm; the collagen solution gradually flows through the fabric. When the volume contained in the upper chamber decreases no further, the system is reloaded in such a way as to never exceed 4 cm in height. Said operations are carried out until the prepared solution is exhausted. Upon equilibration of the system, the retentate is washed with 350 ml of 0.05 M acetic acid with the same system, while respecting pressure differentials. The upper fraction is collected.
(84) The lower fraction is recovered and the analysis is continued in the same way on a fabric with a pore size of 5 m. Retentate as well as filtrate are collected.
(85) The three fractions, i.e., retentate from the 50 m filtration and retentate and filtrate from the 5 m filtration, are brought to 0.6 M NaCl and the collagen is recovered by centrifugation and then dried in two baths of 70% acetone and three baths of 100% acetone. Excess acetone is removed by drying under a stream of air. The fractions are weighed and compared to the total weight collected. Analysis shows that 6.5% of the fibers are retained on a 50 m filter, 27% of the fibers crossed a 5 m filter and thus 66.5% are between 5 m and 50 m.
Example 3
Preparation of a cross-linked collagen film/membrane #1
(86) 800 mg of acidic fibrous collagen of tendons is suspended under mechanical stirring in 100 ml of water for 16 hours. The viscous suspension is poured into a mold at a density of 4 mg of collagen/cm.sup.2. The mold containing the collagen solution is placed in a 3 l hermetically sealed enclosure containing 2 ml of 30% ammonia for 24 hours at 20 C. The gel is placed in an enclosure for removing excess ammonia with an ammonia and moisture absorber in order to obtain a film roughly 40 m in thickness. The film may be used as-is or cross-linked by immersion in a bath of formaldehyde, glutaraldehyde, oxidized glycogen or oxidized amylopectin of various concentrations for periods ranging between 2 minutes and 24 hours. Cross-linking agents are inactivated by immersing the film in a 0.1 M glycine solution, pH 8, for 2 hours. The film is then dried again.
(87) For example, the film obtained after the first drying is immersed for 1 hour in a 0.1% formaldehyde bath, pH 8, and then rinsed in a 0.1 M glycine bath, pH 8, for 2 hours. After a rinsing with water, the film is dried again.
Example 4
Preparation of a cross-linked collagen membrane #2
(88) In order to obtain a membrane containing 10 mg of collagen/cm.sup.2, 100 g of collagen is suspended in 12.5 l of water under mechanical stirring for 16 hours. At the same time, 2.5 g of oxidized glycogen dissolved to 15% in pH 7.7 phosphate buffer is prepared and added to the suspension at the end of the 16 hours. After homogenization, the solution is poured into 1 m.sup.2 molds (or equivalent). The molds containing the collagen solution are placed in a roughly 300 l hermetically sealed enclosure containing 160 ml of 32% ammonia distributed homogeneously for 48 hours at 20 C. At the end of the fibrillation and cross-linking phase, the gels are placed in an enclosure for removing excess ammonia with an ammonia and moisture absorber in order to obtain a membrane roughly 100 m in thickness.
Example 5
Measurement of the swelling ratio of a membrane prepared in example 4
(89) Three samples of 20.5 mg, 22 mg and 20 mg of material are weighed precisely and immersed in 3 ml of 1PBS, pH 7.4, for 1 hour at 37 C. At the end of the hour, excess water from each sample is removed and the samples are weighed again. The results are as follows:
(90) TABLE-US-00001 Sample Weight after Swelling weight swelling ratio Sample 1 20.5 110 5.5 Sample 2 22 127.6 5.8 Sample 3 20 114 5.7 Average 5.66
Example 6
Sponge of acidic fibrous collagen cross-linked by oxidized amylopectins
(91) An aqueous solution of acidic fibrous collagen is obtained by mixing 0.8 g of acidic fibrous collagen in 100 ml of water. The medium is stirred for 16 hours at 20 C. 28 mg of amylopectin containing 1.4 moles of aldehydes/mole of saccharides is heated at 75 C. in 1 ml of 0.1 M phosphate buffer, pH 7.7, until complete dissolution. After cooling to 20 C., said solution is poured under stirring into the 0.8% collagen solution. The homogeneous medium is poured into a mold to a height of 5 mm and transferred to a hermetically sealed enclosure of roughly 3 l in volume containing 3 ml of 28% ammonia for 16 hours. The device containing the gel is then placed in a hermetically sealed enclosure containing an ammonia absorber until all the ammonia in the enclosure is removed. The collagen gel is then frozen and then freeze-dried to yield a sponge of cross-linked atelocollagen.
Example 7
Measurement of cross-linking homogeneity
(92) A gel roughly 1 cm in thickness was prepared by the method described in example 4 up to the cross-linking step.
(93) At the end of said cross-linking step, the gel was unmolded, cut into two, approximately in the middle, in the horizontal direction, and the two sections were dried separately.
(94) An external and an internal sample of material (roughly 10 mg each) are taken from areas corresponding to the external portion and the internal portion of the gel, respectively.
(95) Cross-linking rate is determined by an assay of amines remaining free in the collagen by TNBS (2,4,6-trinitrobenzenesulfonic acid). Said TNBS reagent specifically reacts with amines of lysine residues and free terminal amino acids.
(96) The internal and external samples are taken and incubated in a water/propanol solution (1 ml) at 60 C. for 1 hour. 500 l of 8% bicarbonate and 1 ml of TNBS diluted to 1/120 are added. The reaction takes place for 3 hours at 40 C.
(97) After cooling, 200 l of 6 N HCl is added to quench the reaction. Excess TNBS is extracted with 5 ml of ethyl acetate. Acid hydrolysis (3 ml of 6 N HCl for 1.25 hours) releases all the amino acids. N-TNBS terminal amino acids are extracted in the same manner as excess TNBS.
(98) After adequate dilution, absorbance of the aqueous phase is measured at 345 nm. The molar extinction coefficient of the complex at 345 nm, measured according to the protocol described by Kakade et al., is 1.46.Math.10.sup.4 M.sup.1.Math.cm.sup.1, which makes it possible to calculate the quantity of lysines remaining free in the membrane. The result is expressed in mol of free lysines per mg of membrane.
(99) For a membrane cross-linked with oxidized glycogen in a ratio of 0.4 CHO of oxidized glycogen for 1 NH.sub.2, the results are as follows:
(100) TABLE-US-00002 mol of free lysine/mg of membrane External sample 0.161 Internal sample 0.150
(101) The difference in cross-linking is thus 3.5%, which is ((0.161-0.150)/(0.161+0.150)100). The cross-linking rates of the external portion and the internal portion are thus roughly the same. Cross-linking is thus quite homogeneous throughout the thickness of the material.
Example 8
Measurement of cross-linking
(102) A so-called cross-linked membrane was prepared according to the method described in example 4, including the step of adding ammonia.
(103) A so-called non-cross-linked membrane was prepared according to the method described in example 4, wherein the step of adding ammonia is omitted.
(104) Cross-linking may be measured using differential scanning calorimetry (DSC). Said method measures the differences in the transfer of heat between a sample to be analyzed and a reference.
(105) DSC is used to detect phase transitions: glass transition temperature (T.sub.g) fusion or denaturation temperatures reaction enthalpies (to determine the cross-linking rates of polymers).
(106) The analyses are carried out under a stream of inert gas (nitrogen or argon, for example) to avoid any reaction of the material studied with the atmosphere of the furnace.
(107) With regard to collagen, cross-linking increases denaturation temperature. To demonstrate that incubating the collagen solution containing the cross-linking agent in ammonia vapors leads to the formation of stable chemical cross-linking bonds between the collagen and the cross-linking agent, the DSC profile of a cross-linked membrane and a non-cross-linked membrane were determined.
(108) TABLE-US-00003 Denaturation temperature ( C.) Cross-linked membrane 49.62 Non-cross-linked membrane 42.37
(109) The denaturation temperature of the cross-linked membrane is thus clearly higher than that of the non-cross-linked membrane. The reaction between the aldehyde cross-linking agent and the collagen thus clearly takes place during the incubation of the solutions in ammonia vapors.
REFERENCES
(110) Forest P O, Karoum R, Gagnieu C H. Influence of gradual introduction of hydrophobic groups (stearic acid) in denatured atelocollagen on fibroblasts behavior in vitro, J Biomed Mater Res A. 2007 Mar. 1; 80(3): 758-67. Gagnieu C H, Forest P O. In vivo biodegradability and biocompatibility of porcine type I atelocollagen newly crosslinked by oxidized glycogen, Biomed Mater Eng. 2007; 17(1): 9-18). Rousseau C F and Gagnieu C H. In vitro cytocompatibility of porcine type I atelocollagen crosslinked by oxidized glycogen. Biomaterials, 2002. 23(6): p. 1503-10. Kakade M L, Liener I E. Determination of available lysine in proteins. Anal Biochem, 1969; 27(2): 273-280
PATENT REFERENCES
(111) WO2007/147739 FR2810889 FR2877669 EP0862468 U.S. Pat. No. 4,931,546