Highly flexible degradable fibers

Abstract

The present invention relates to a method for producing biodegradable fibers on the basis of a silane compound, said silane compound being crosslinked during production and, at least to some extent, an organic acid being incorporated into the forming crosslinked structure via covalent bonds and/or contributing to the crosslinking. The present invention also relates to the fibers that can be produced by the method according to the invention and to the use thereof.

Claims

1. A process for producing biodegradable fibres comprising the following steps: a) providing an alcoholic solution of a silane compound selected from the group consisting of tetraalkoxysilanes, trialkoxysilanes, halosilanes, and mixtures thereof; b) providing an aqueous solution of an organic acid selected from the group consisting of sulfonic acids, sulfuric esters, phosphonic acids, phosphoric esters, and mixtures thereof; c) combining the solutions provided in steps a) and b) and mixing for 4 hours to 1 week at a temperature of 20 to 70° C.; d) removing at least part of the alcohol from the mixture from step c) and cooling the concentrated mixture to a temperature of 20 to −25° C.; e) storing the cooled mixture from step d) until a viscosity of 10 to 75 Pa.Math.s is reached; and f) spinning the mixture from step e) into continuous fibres; wherein during steps c) to e), the silane compound undergoes crosslinking and at least part of the organic acid is incorporated into the resulting network via covalent bonds and/or contributes to the crosslinking.

2. The process according to claim 1, wherein the silane compound selected in step a) is a mixed or unmixed tetraalkoxysilane corresponding to the general formula Si(OC.sub.xH.sub.2x+1).sub.4 where x=1-12, and/or the alcohol from step a) is a monohydric, dihydric or trihydric, branched or unbranched alcohol that can be aliphatic or aromatic.

3. The process according claim 1, wherein the organic acid in step b) is 0.01 to 1 N; and/or the content of organic acid in the aqueous solution from step b) is in the range from 0.01 to 2% by weight, based on the total weight of the solution.

4. The process according to claim 1, wherein the mixing in step c) is carried out by adding the aqueous solution of the organic acid dropwise to the alcoholic silane solution; or the mixing in step c) is carried out by adding the alcoholic silane solution dropwise to the aqueous solution of the organic acid; or the mixing in step c) is carried out by simultaneous combination of the alcoholic silane solution and the aqueous solution of the organic acid; and/or the mixing in step c) is carried out by stirring or agitation; and/or the mixture from step c) is stirred for 5 hours to 144 hours; and/or the temperature in step c) is 20 to 60° C.; and the pH of the mixture in step c) is <5.

5. The process according to claim 1, wherein during step d) 40 to 80% by weight of the solvent mixture, based on the total mass of mixture provided in step b), is removed; and/or the concentrated mixture from step d) is cooled to a temperature of 20 to −25° C.; and/or at least part of the water from step b) is also removed during step d).

6. The process according to claim 1, wherein step e) is carried out until a viscosity of 10 to 70 Pa.Math.s is reached.

7. The process according to claim 1, wherein spinning is carried out with the application of pressure in the range from 10 to 60 bar.

8. The process according to claim 1, wherein the process comprises the following further process steps, which take place after step f): g) cutting or die-cutting the continuous fibres obtained after spinning in step f), and/or h) sterilizing the fibres from step f) or g).

9. The process according to claim 1, wherein exactly one alcohol is used as solvent in step a) and/or exactly one silane compound is dissolved in the solution from step a); and/or an aqueous solution of exactly one organic acid is provided in step b).

10. The process according to claim 1, wherein the process is carried out as a continuous or batch-wise operation.

11. A biodegradable fibre produced by a process comprising the following steps: a) providing an alcoholic solution of a silane compound selected from the group consisting of tetraalkoxysilanes, trialkoxysilanes, halosilanes, and mixtures thereof; b) providing an aqueous solution of an organic acid selected from the group consisting of sulfonic acids, sulfuric esters, phosphonic acids, phosphoric esters, and mixtures thereof; c) combining the solutions provided in steps a) and b) and mixing for 4 hours to 1 week at a temperature of 20 to 70° C.; d) removing at least part of the alcohol from the mixture from step c) and cooling the concentrated mixture to a temperature of 20 to −25° C.; e) storing the cooled mixture from step d) until a viscosity of 10 to 75 Pa.Math.s is reached; and f) spinning the mixture from step e) into continuous fibres; wherein during steps c) to e), the silane compound undergoes crosslinking and at least part of the organic acid is incorporated into the resulting network via covalent bonds and/or contributes to the crosslinking.

12. The biodegradable fibre according to claim 11, wherein the fibre degrades in a period of >6 months.

13. The biodegradable fibre according to claim 11, wherein the fibre is coilable and/or the proportion of functional groups from the organic acid that are covalently attached in the network is 30 to 80%, based on the functional groups provided in step b).

14. A fibre mesh or filter comprising biodegradable fibres according to claim 11.

Description

BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWINGS

(1) FIG. 1 depicts the results of bending tests on the fibers of the invention and of a prior art.

(2) FIG. 2 depicts degradation profiles of the fibers of the invention and of a prior art.

(3) FIG. 3 depicts SEM images of the fibre of the invention after storage in PBS.

(4) FIG. 4 depicts the biocompatibility of the fibre of the invention.

(5) FIG. 5 depicts the results of cell-proliferation studies carried on the fibre of the invention.

DETAILED DESCRIPTION OF EMBODIMENTS OF THE INVENTION

Definitions of Terms

(6) A “biodegradable” fibre in the context of the present invention means a fibre that is biocompatible and that is broken down under physiological conditions.

(7) In the context of the present invention, the term “viscosity” means the dynamic viscosity, which is preferably determined using a Physica MCR301 rheometer from Anton Paar equipped with a CC17/T200/S coaxial cylinder measuring attachment at a shear rate of 10 s.sup.−1.

(8) The “crosslinking of the silane compound” and the covalent incorporation of the organic acid into the network is illustrated in the following diagram taking the incorporation of methanesulfonic acid as an example.

(9) ##STR00001##

(10) The term “coilable fibre” is understood as meaning a fibre that can be coiled onto a reel without the fibre being destroyed in the process.

(11) Process

(12) In a preferred embodiment of the present invention, the silane compound selected in step a) is a mixed or unmixed tetraalkoxysilane corresponding to the general formula Si(OC.sub.xH.sub.2x+1).sub.4 where x=1-12, which is preferably selected from the group consisting of tetraethoxysilane, tetrapropoxysilane, tetrabutoxysilane and mixtures thereof, wherein particular preference is given to tetraethoxysilane.

(13) Another preferred embodiment of the present invention envisages that the alcohol from step a) is a monohydric, dihydric or trihydric, branched or unbranched alcohol that may be aliphatic or aromatic and is preferably selected from the group consisting of ethanol, propanol, butanol, ethylene glycol, phenol and mixtures thereof, wherein preference is given to ethanol.

(14) According to another preferred embodiment of the present invention, the silane compound selected in step a) is a mixed or unmixed tetraalkoxysilane corresponding to the general formula Si(OC.sub.xH.sub.2x+1).sub.4 where x=1-12, which is preferably selected from the group consisting of tetraethoxysilane, tetrapropoxysilane, tetrabutoxysilane and mixtures thereof, wherein particular preference is given to tetraethoxysilane and the alcohol from step a) is a monohydric, dihydric or trihydric, branched or unbranched alcohol that may be aliphatic or aromatic and is preferably selected from the group consisting of ethanol, propanol, butanol, ethylene glycol, phenol and mixtures thereof, wherein preference is given to ethanol.

(15) Another preferred embodiment of the present invention envisages that the organic acid in step b) is selected from the group consisting of sulfonic acids, in particular methanesulfonic acid, carboxylic acids, carboxylic esters, sulfuric esters, amino acids, phosphonic acids, phosphoric esters and mixtures thereof, wherein particular preference is given to methanesulfonic acid.

(16) According to another preferred embodiment of the present invention, the organic acid in step b) is 0.01 to 1 N and more preferably 0.1 N.

(17) Another preferred embodiment envisages that the content of organic acid in the aqueous solution from step b) is in the range from 0.01 to 2% by weight, preferably 0.05 to 1% by weight and more preferably 0.1 to 0.5% by weight, based on the total weight of the solution.

(18) In another preferred embodiment of the present invention, the organic acid in step b) is selected from the group consisting of sulfonic acids, in particular methanesulfonic acid, carboxylic acids, carboxylic esters, sulfuric esters, amino acids, phosphonic acids, phosphoric esters and mixtures thereof, wherein particular preference is given to methanesulfonic acid, and the organic acid in step b) is 0.01 to 1 N, more preferably 0.1 N.

(19) According to another preferred embodiment of the present invention, the organic acid in step b) is selected from the group consisting of sulfonic acids, in particular methanesulfonic acid, carboxylic acids, carboxylic esters, sulfuric esters, amino acids, phosphonic acids, phosphoric esters and mixtures thereof, wherein particular preference is given to methanesulfonic acid, and the organic acid in step b) is 0.01 to 1 N, more preferably 0.1 N, and the content of organic acid in the aqueous solution from step b) is in the range from 0.01 to 2% by weight, preferably 0.05 to 1% by weight and more preferably 0.1 to 0.5% by weight, based on the total weight of the solution.

(20) Another preferred embodiment of the present invention envisages that the mixing in step c) is carried out by adding the aqueous solution of the organic acid dropwise to the alcoholic silane solution or the mixing in step c) is carried out by adding the alcoholic silane solution dropwise to the aqueous solution of the organic acid or the mixing in step c) is carried out by simultaneous combination of the alcoholic silane solution and the aqueous solution of the organic acid.

(21) In another preferred embodiment of the present invention, the mixing in step c) is carried out by stirring or shaking.

(22) According to another preferred embodiment of the present invention, the mixture from step c) is stirred for 5 hours to 144 hours, preferably 10 to 24 hours and more preferably for 16 to 18 hours.

(23) Another preferred embodiment of the present invention envisages that the temperature in step c) is 20 to 60° C., preferably 20 to 50° C. and more preferably 25 to 40° C.

(24) In another preferred embodiment of the present invention, the pH of the mixture in step c) is <5, preferably 1 to 4.9 and more preferably 4 to 4.9.

(25) Another preferred embodiment of the present invention envisages that the mixing in step c) is carried out by adding the aqueous solution of the organic acid dropwise to the alcoholic silane solution or the mixing in step c) is carried out by adding the alcoholic silane solution dropwise to the aqueous solution of the organic acid or the mixing in step c) is carried out by simultaneous combination of the alcoholic silane solution and the aqueous solution of the organic acid and the mixing in step c) is carried out by stirring and the mixture from step c) is stirred for 5 hours to 144 hours, preferably 10 to 24 hours and more preferably for 16 to 18 hours and the temperature in step c) is 20 to 60° C., preferably 20 to 50° C. and more preferably 25 to 40° C. and the pH of the mixture in step c) is <5, preferably 1 to 4.9 and more preferably 4 to 4.9.

(26) In another preferred embodiment of the present invention, during step d) 40 to 80% by weight, preferably 45 to 75% by weight and more preferably 50 to 65% by weight, of the solvent mixture, based on the total mass of mixture provided in step b), is removed.

(27) According to another preferred embodiment of the present invention, the concentrated mixture from step d) is cooled to a temperature of 20 to −25° C., preferably 10 to −25° C. and more preferably 4 to −20° C.

(28) Another preferred embodiment envisages that at least part of the water from step b) is also removed during step d).

(29) In another preferred embodiment of the present invention, during step d) 40 to 80% by weight, preferably 45 to 75% by weight and more preferably 50 to 65% by weight, of the solvent mixture, based on the total mass of mixture provided in step b), is removed and the concentrated mixture from step d) is cooled to a temperature of 20 to −25° C., preferably 10 to −25° C. and more preferably 4 to −20° C. and at least part of the water from step b) is removed.

(30) In another preferred embodiment of the present invention, step e) is carried out until a viscosity of 10 to 70 Pa.Math.s, preferably 10 to 40 Pa.Math.s and more preferably 20 to 25 Pa.Math.s is reached.

(31) Another preferred embodiment of the present invention envisages that spinning is carried out with the application of pressure in the range from 10 to 60 bar, preferably 10 to 40 bar and more preferably 20 to 40 bar.

(32) Another preferred embodiment of the present invention envisages that the process comprises the following further process steps, which take place after step f):

(33) g) cutting or stamping the continuous fibres obtained after spinning in step f), and/or

(34) h) sterilizing the fibres from step f) or g), preferably by γ-radiation or by treatment with ethylene oxide, 70% ethanol solution or chloroform.

(35) According to another preferred embodiment of the present invention, exactly one alcohol is used as the solvent in step a).

(36) Another preferred embodiment of the present invention envisages that exactly one silane compound is dissolved in the solution according to step a).

(37) In another preferred embodiment of the present invention, an aqueous solution of exactly one organic acid is provided in step b).

(38) Another preferred embodiment of the present invention envisages that exactly one alcohol is used as solvent in step a) and exactly one silane compound is dissolved in the solution according to step a) and an aqueous solution of exactly one organic acid is provided in step b).

(39) In another preferred embodiment of the present invention, the process is carried out as a continuous or batchwise operation.

(40) According to another preferred embodiment of the present invention, the process comprises no process steps other than steps a) to h) mentioned above.

(41) Biodegradable Fibres

(42) The present invention further relates to a fibre producible by the process of the invention.

(43) In a preferred embodiment of the present invention, the fibre degrades in a period of >6 months, for example more than 3 years, more preferably of from 6 to 18 months and particularly preferably of from 10 to 12 months.

(44) Another preferred embodiment of the present invention envisages that the fibre is coilable.

(45) In another preferred embodiment of the present invention, the proportion of functional groups from the organic acid that are covalently attached in the network is 30 to 80%, preferably 45 to 75% and more preferably 53 to 65%, based on the functional groups provided in step b).

(46) Use

(47) The present invention further relates to the use of the fibres of the invention or of fibre meshes made from these fibres.

(48) Preference is given to use in the following fields: Regenerative therapies, preferably as cell-support materials for the development of tissues or cell cultures or as light guides, more preferably in the field of minimally invasive surgery; Microbiology, preferably the application or culture of bacteria, yeasts and fungi on the fibres; Pharmaceutical uses, preferably for encapsulating or coupling active substances, enzymes or nanoparticles; Cosmetics industry, preferably by integrating the fibres in cosmetic products; Diagnostics, preferably in vitro and/or in vivo, more preferably for the covalent or adsorptive attachment of antibodies, aptamers and/or enzyme-substrate complexes; Food industry, preferably to improve mouthfeel, more preferably by integrating flavourings, fats, proteins, enzymes, ions and food additives; Filters, preferably for neutralizing waste water or for releasing ions into liquids; Fibre reinforcement of materials, preferably in composite materials; Optics, preferably in light therapy or endoscopy.

(49) The invention is elucidated in more detail with reference to the examples that follow, without intending to restrict it to the specific embodiments shown here.

WORKING EXAMPLES

(50) 1) Methanesulfonic Acid

(51) 5 mol of tetraethoxysilane (Sigma Aldrich) was mixed in ethanolic solution (400 ml). To this sol was added dropwise, over a 2 h period, 0.02 mol of methanesulfonic acid (Sigma Aldrich) in a 0.1 N aqueous solution and the resulting mixture was stirred for a further 18 h at 40° C. This resulted in the covalent incorporation of the methanesulfonic acid into the Si—O framework (see below for demonstration of this).

(52) 906.5 g of solvent was then stripped from the sol and the sol was matured at −20° C. to a honey-like viscosity (21 Pa*s measured at 4° C.). The viscous liquid was transferred to a pressure vessel thermally equilibrated at −15° C. and forced with a pressure of 20 bar through a die plate having seven dies (die diameter: 150 μm). After a fall distance of 2.5 m, the fibres were collected and stored at 20% atmospheric humidity. The spinning conditions specified in the article “Nanostructured surfaces of biodegradable silica fibres enhance direct amoeboid cell migration in a microtubule-dependent process” by Martin Emmert, Patrick Witzel, Miranda Rothenburger-Glaubitt and Doris Heinrich, published in The Royal Society of Chemistry 2017, volume 7, pages 5708 to 5714, are likewise very well suited to the spinning of the fibres of the invention.

(53) The fibres were stored at low atmospheric humidity and showed very flexible properties. For the test of flexible properties, a fibre of the invention was coiled around a cylindrical rod of varying diameters and examined to see whether the fibre breaks at the given diameter or remains intact. This test was carried out on a total of 10 different fibres and the number of intact fibres after the 10 tests was plotted for each rod diameter. The comparison system used was a fibre of the prior art produced according to DE 196 09 551 C1. As can be seen from FIG. 1, the fibre of the invention (MSA fibre) has greater flexibility than the fibre of the prior art (HNO.sub.3 fibre) and breaks only at a diameter of <0.7 mm.

(54) FIG. 2 (top) shows the degradation profile of a fibre of the invention in phosphate-buffered saline (PBS) and the lower part of FIG. 2 shows the degradation profile of a fibre produced according to the prior art. The tests were carried out statically, i.e. the degradation medium was replaced on each measurement day. The degradation profile was generated gravimetrically by removing the fibres on the respective measurement day, drying to constant weight and determining the remaining fibre mass. The fibres were then returned to the degradation medium for further degradation.

(55) It can be seen from the figures that the fibre of the invention degrades slowly, whereas the fibre of the prior art was completely degraded within just 5 weeks.

(56) FIG. 3 shows SEM images of the fibre of the invention after storage in PBS for 30 minutes, 4 days, 22 days and 40 days. Progressive degradation is clearly visible.

(57) In addition, a biocompatibility test with the fibre of the invention was carried out in accordance with DIN ISO 10993-5. The data are summarized in FIG. 4 and the fibre of the invention is biocompatible, values over 80% being considered non-cytotoxic.

(58) FIG. 5 summarizes results of cell-proliferation studies with the fibre of the invention.

(59) For this, 60 mg of fibre material was washed with phosphate-buffered saline (PBS) and populated with 50 000 human dermal fibroblasts (hdF) in a 12-well plate. The populated nonwovens were incubated in cell-culture medium (DMEM) containing 10% foetal calf serum for 2, 4, 7 and 10 days. On each measurement day, the fibres were transferred to a new multiwell plate and the WST-1 activity of the cells measured and the cell count determined. As a negative control, cells were incubated without fibres in a well containing DMEM (+10% FCS) and as a positive control with DMEM (+10% FCS) containing 1% sodium dodecyl sulfate (SDS).

(60) It can be seen from the figure that human dermal fibroblasts proliferate much more rapidly on the fibre of the invention. Moreover, the fibre of the invention shows high cell metabolic activity.

(61) As shown by thermogravimetric analyses in a synthetic air atmosphere coupled to a mass spectrometer (TGA-MS), SO.sub.x is liberated only at temperatures above 400° C. This demonstrates the covalent attachment of the sulfonic acid.

(62) 2) Para-Toluenesulfonic Acid

(63) 5 mol of tetraethoxysilane (Sigma Aldrich) was mixed in ethanolic solution (400 ml). To this sol was added dropwise, over a 2 h period, 0.02 mol of para-toluenesulfonic acid (Sigma Aldrich) in a 0.1 N aqueous solution and the resulting mixture was stirred for a further 18 h at 40° C. This resulted in the covalent incorporation of the para-toluenesulfonic acid into the Si—O framework.

(64) 906.5 g of solvent was then stripped from the sol and the sol was matured at −20° C. to a honey-like viscosity (22 Pa*s measured at 4° C.). The viscous liquid was transferred to a pressure vessel thermally equilibrated at −15° C. and forced with a pressure of 20 bar through a die plate having seven dies (die diameter: 150 μm). After a fall distance of 2.5 m, the fibres were collected and stored at 20% atmospheric humidity.