The present disclosure relates to medical device having irregular and/or curved silicone surfaces coated with rhamnolipids as well as methods for coating a medical device having irregular and/or curved silicone surfaces with rhamnolipids grafting.
Bacterial colonisation of synthetic materials surfaces constitutes a problem in many fields, for example in the field of implantable medical devices. The use of implantable medical devices is increasing over time. For implantable devices silicone rubber is widely used due to its biocompatibility properties, high mechanical strength and elasticity and potentially long device life time.
One problem commonly associated with implanted medical devices is the formation of biofilms on the surfaces of the device. Biofilms are communities of microorganisms where cells stick to each other and often also to a surface. These communities are embedded within a slimy extracellular matrix consisting of polymeric substance. The formation of biofilm on implanted medical devices is a common source of complications often involving loss of function of the implanted device and shortening of the device lifetime, leading to earlier exchange of the device.
Example of silicone devices on which the formation of biofilm is a known problem are permanent implants like breast implants, nasal implants, gastric bands, joint implants, gluteal implants, pelvic meshes etc. In the case of permanent implants, the formation of biofilm may cause device failure or device-associated infections leading to hospitalization and need for surgery. In devices for shorter duration implantation e.g. voice prostheses, silicone tubes for the nasolacrimal duct and tympanic ear tubes, the formation of biofilm can cause impaired device performance and device failure leading to the need for earlier exchange of the device.
Several surface treatments for silicone medical devices have been suggested to improve the resistance against biofilm formation, including antibiotic, antifungal or antimicrobial surface treatments, e.g. silver oxide or metallic silver, caspofungin peptides, selenium etc. However, the use of silver ions or silver nanoparticles in polymer matrices or quaternary amine compounds may be of concern with regards to damage to human cells and tissue.
An object of the present disclosure is to provide a medical device having a coating preventing or reducing the formation of biofilms on the surface of the medical device as well as methods for coating a medical device with such a coating.
Accordingly, the present invention preferably seeks to mitigate, alleviate or eliminate one or more of the above-identified deficiencies in the art and disadvantages singly or in any combination and solves at least the above mentioned problems by providing a medical device coated with rhamnolipids and by providing a method of coating a medical device with rhamnolipids.
In a first aspect there is provided a medical device having irregular and/or curved silicone surfaces, wherein at least a part of the irregular and/or curved silicone surfaces is coated with rhamnolipids. Such a coating will prevent or reduce the formation of a biofilm on the surface of the medical device.
In a second aspect there is provided a method of coating a medical device having irregular and/or curved silicone surfaces with rhamnolipids, wherein the method comprises the steps of 1) activating the silicone surfaces that are to be coated by introducing free amino-groups; and 2) covalently attaching rhamnolipids to said silicone surfaces. Such a method will result in a stable coating of rhamnolipids on the surfaces of a medical device.
In a third aspect there is provided a voice prosthesis for mounting in a fistula between trachea and esophagus, comprising a tubular body having a lumen; a valve disc and a valve seat, arranged in the lumen of the tubular body, said valve disc and said valve seat controlling the communication through said lumen by interaction between said valve disc and said valve seat; wherein at least a part of the voice prosthesis comprises silicone and at least a part of said silicone being coated with rhamnolipids.
Other objectives, features and advantages of the present disclosure will appear from the following detailed description, from the drawings, as well as from the attached claims. It is noted that the disclosure relates to all possible combination of features.
Generally, all terms used in the claims are to be interpreted according to their ordinary meaning in the technical field, unless explicitly defined otherwise herein. All references to “a/an/the [element, device, component, means, step, etc.]” are to be interpreted openly as referring to at least one instance of said element, device, component, means, step, etc., unless explicitly stated otherwise. The steps of any method disclosed herein do not have to be performed in the exact order disclosed, unless explicitly stated.
As used herein, the term “comprising” and variations of that term are not intended to exclude other additives, components, integers or steps.
These and other aspects, features and advantages of which the invention is capable of will be apparent and elucidated from the following description of embodiments of the present invention, reference being made to the accompanying drawings, in which:
The present disclosure relates to a medical device having irregular and/or curved silicone surfaces, wherein at least a part of the irregular and/or curved silicone surfaces is coated with rhamnolipids. The present disclosure also relates to a method of coating a medical device having irregular and/or curved silicone surfaces with rhamnolipids.
Specific aspects and embodiments of the present disclosure will be described in detail below.
Microorganisms synthesize a wide range of surface-active compounds (SAC), generally referred to as biosurfactants (BS). Microbial biosurfactants function as anti-adhesives and prevent or reduce the formation of biofilms. In the present disclosure, rhamnolipids are used for coating medical devices. Rhamnolipids are able to significantly inhibit fungal and bacterial biofilm formation on silicone. Thus, rhamnolipids inhibit fungal and bacterial biofilm growth and can prolong the device lifetime of medical devices of silicone and potentially reduce the use of antimicrobial drugs.
The rhamnolipids of the present disclosure are composed of homologues of the mono- and di-rhamnolipid families. The rhamnolipids may be produced by the bacteria Pseudomonas aeruginosa 89 and such rhamnolipids are herein referred to as R89 or R89BS.
The purity of the raw extract is typically about 91%. Typically, the rhamnolipids comprise 70-85% (weight/weight), preferably 75% (weight/weight), mono-rhamnolipids and 15-30% (weight/weight), preferably 25% (weight/weight), di-rhamnolipid.
At pH 7.0, the surface tension of alkaline distilled water, measured with a ring tensiometer, decreases rapidly as the concentration of biosurfactant is increased, with a minimum surface tension of about 30 mN/m. The maximum surfactant concentration in a solution that can be achieved without formation of clusters of surfactant molecules, so called micelles, defines the Critical Micelle Concentration (CMC). The CMC value for R89BS has been found to be at a concentration of 40 to 50 μg/mL, such as 42 to 48 μg/mL, such as about 46.1 μg/mL. Thus, the CMC value indicates the amount of surfactant required to reach maximum surface tension reduction, and the lower the CMC, the less surfactant is required to reduce the surface tension. Biofilm formation is reduced at low surface tension. Hence, in order to accomplish a certain reduction of biofilm formation, a lower concentration of R89BS is needed than of a biosurfactant having a higher CMC. This is reflected in the rather low minimal inhibitory concentrations (MICs) of crude rhamnolipid. The MIC of crude rhamnolipid is 0.06 mg/ml for S. aureus and 0.12 mg/ml for S. epidermidis and >2 mg/ml for C. albicans.
Specifically, rhamnolipid raw extract, also referred to as rhamnolipid crude extract, has the ability to inhibit S. aureus adhesion to silicone and its activity is not significantly different from that of the mono- and di-rhamnolipid purified fractions. This implies that these two fractions contribute equally to the anti-adhesive activity of the crude extract. Thus, the crude extract can be used directly for coating of silicone surfaces for the inhibition of microbial growth and biofilm formation, without any further purification steps. This is advantageous, since downstream operation costs typically represent about 50-80% of the total processing costs.
A further advantage of rhamnolipids is that these biosurfactants retain their surface activity over a wide pH-range.
Furthermore, R89 covalently grafted to silicone according to the present disclosure is able to inhibit biofilm formation of C. albicans and S. aureus at eight days of incubation of 85% and 82%, respectively.
The medical devices disclosed herein have irregular and/or curved silicone surfaces, wherein at least a part of the irregular and/or curved silicone surfaces is coated with rhamnolipids. The formation of biofilms on such devices is reduced compared to devices not having a coating of rhamnolipids. Furthermore, as demonstrated in the experiments below, coating with rhamnolipid shows a significant ability to attach to silicone elastomer surfaces and to counteract biofilm formation of silicone elastomers compared to for example AC7BS (a lipopeptide from Bacillus subtilis AC7).
General features applicable to devices disclosed herein as well as specific examples of such devices are described below.
The rhamnolipids may comprise 70-85% (weight/weight), preferably 75% (weight/weight), mono-rhamnolipids and 15-30% (weight/weight), preferably 25% (weight/weight), di-rhamnolipids. The total amount of mono-rhamnolipids and di-rhamnolipids is 100% (weight/weight).
In one specific embodiment, the rhamnolipids comprise 75% (weight/weight) mono-rhamnolipids and 25% (weight/weight), di-rhamnolipids.
The rhamnolipids may have a purity of at least 85%, more preferably a purity of at least 90%.
The rhamnolipids may be covalently attached to at least a part of the irregular and/or curved silicone surfaces. One advantage of such a coating is that the rhamnolipid coating is stable for a longer period of time than a rhamnolipid coating that is not covalently attached to the silicone surface.
The rhamnolipids may be covalently attached to the surface via a linker comprising an amide-bond.
In one embodiment, the linker is —O—Si—(CH2)3—N—CO—. Such a coating may be achieved by using (3-aminopropyl)triethoxysilane (APTES) monomers.
In one embodiment, the linker is —O—(CH2)3—N—CO—. Such a coating may be achieved by using cyclopropylamine monomers.
In one embodiment, the surface density of rhamnolipids is more than 4.5×1015 rhamnolipids per cm2, such as more than 5×1015 rhamnolipids per cm2, such as more than 6×1015 rhamnolipids per cm2, such as more than 7×1015 rhamnolipids per cm2, such as more than 8×1015 rhamnolipids per cm2. Such surfaces are particularly resistant to the formation of biofilms.
Preferably, the surface density of rhamnolipids is more than 6×1015 rhamnolipids per cm2.
The medical device may be a voice prosthesis, a tracheostomy speaking valve, a holder for tracheostomy speaking valve, a silicone tube for the nasolacrimal duct, a tympanic ear tube, a breast implant, a nasal implant, a gastric band, a joint implant, a gluteal implant or a pelvic mesh, or urinary catheter; preferably wherein the medical device is a voice prosthesis, a tracheostomy speaking valve, a holder for tracheostomy speaking valve.
Specifically, the medical device may be a silicone voice prosthesis 100 comprising a voice prosthesis valve, preferably wherein the surface coated with rhamnolipids comprise the at least one of the sealing surfaces 108 of the voice prosthesis valve.
In one specific embodiment, the medical device is a voice prosthesis 100, preferably a silicone voice prosthesis, comprising a voice prosthesis valve, wherein at least one of the sealing surfaces 108 of the voice prosthesis valve are silicone surfaces coated with rhamnolipids. The rhamnolipids are covalently attached to the surfaces via linker comprising an amide bond. The linker may be —O—Si—(CH2)3—N—CO— or —O—(CH2)3—N—CO—. Preferably, the rhamnolipids comprise 70-85% (weight/weight), preferably 75% (weight/weight), mono-rhamnolipids and 15-30% (weight weight), preferably 25% (weight/weight), di-rhamnolipids. The total amount of mono-rhamnolipids and di-rhamnolipids is 100% (weight/weight). Preferably, the rhamnolipids have a purity of at least 85%, more preferably a purity of at least 90%.
In another specific embodiment, the medical device is a voice prosthesis 100, preferably a silicone voice prosthesis, wherein at least one of the retaining flanges 102, 103 of the voice prosthesis are silicone surfaces coated with rhamnolipids. The rhamnolipids are covalently attached to the surfaces via linker comprising an amide bond. The linker may be —O—Si—(CH2)3—N—CO— or —O—(CH2)3—N—CO—. Preferably, the rhamnolipids comprise 70-85% (weight/weight), preferably 75% (weight/weight), mono-rhamnolipids and 15-30% (weight weight), preferably 25% (weight/weight), di-rhamnolipids. The total amount of mono-rhamnolipids and di-rhamnolipids is 100% (weight/weight). Preferably, the rhamnolipids have a purity of at least 85%, more preferably a purity of at least 90%. Coating at least one retaining flange 102, 103 can prevent microbial growth affecting the strength of the retaining flange 102, 103 negatively.
In yet another specific embodiment, the medical device is a voice prosthesis 100, preferably a silicone voice prosthesis, comprising a voice prosthesis valve, wherein at least one of the sealing surfaces 108 of the voice prosthesis valve and/or at least one of the retaining flanges 102, 103 are silicone surfaces coated with rhamnolipids. The rhamnolipids are covalently attached to the surfaces via linker comprising an amide bond. The linker may be —O—Si—(CH2)3—N—CO— or —O—(CH2)3—N—CO—. Preferably, the rhamnolipids comprise 70-85% (weight/weight), preferably 75% (weight/weight), mono-rhamnolipids and 15-30% (weight weight), preferably 25% (weight/weight), di-rhamnolipids. The total amount of mono-rhamnolipids and di-rhamnolipids is 100% (weight/weight). Preferably, the rhamnolipids have a purity of at least 85%, more preferably a purity of at least 90%.
The methods disclosed herein are for coating a medical device having irregular and/or curved silicone surfaces with rhamnolipids.
General features applicable to the method disclosed herein as well as specific examples of such methods are described below.
The method comprises the steps of 1) activating the silicone surfaces that are to be coated by introducing free amino-groups; and 2) covalently attaching rhamnolipids to said silicone surfaces.
As demonstrated in the experiments below, a coating with rhamnolipid shows a significant ability to attach to silicone elastomer surfaces and to counteract biofilm formation of silicone elastomers compared to for example AC7BS (a lipopeptide from Bacillus subtilis AC7).
In one embodiment of the method, step 1) comprises subjecting the surface that is to be coated to (3-aminopropyl)triethoxysilane (APTES) monomers or cyclopropylamine monomers. By using such a step, the rhamnolipids will be covalently attached to the silicone surface via a linker comprising an amide-bond. APTES linkers have been demonstrated (see Experimental Section below) to be a good strategy in order to covalently graft biosurfactants on a silicone surface. The attachment of the APTES molecules on the silicone surface allows to expose amino groups (—NH2), that can be exploited to form an amide-bond with the carboxyl group (—COOH) of biosurfactants. The physico-chemical and biological results demonstrated the efficacy of APTES coating to covalently graft R89. Cyclopropylamine is an alternative monomer to obtain a polymeric linker, exposing NH2, to graft biosurfactants.
In one embodiment of the method, step 1) comprises the steps of a) subjecting the silicone surface that is to be coated to atmospheric or vacuum plasma discharge; and b) subjecting the silicone surface that is to be coated to a solution of (3-aminopropyl)triethoxysilane (APTES) monomers or cyclopropylamine monomers. Atmospheric or vacuum argon plasma discharge enhances the surface functionalization process. Subjecting the silicone surface that is to be coated to atmospheric or vacuum plasma discharge before covalent grafting of rhamnolipids such as rhamnolipids results in a high amount of rhamnolipids attached to the surface.
Typically, such a process comprising the steps of a) subjecting the silicone surface that is to be coated to atmospheric or vacuum plasma discharge; and b) subjecting the silicone surface that is to be coated to a solution of (3-amino-propyl)triethoxysilane (APTES) monomers or cyclopropylamine monomers, yields a surface having more than 6×1015 amino-groups per cm2, such as more than 7×1015 amino-groups per cm2, such as more than 8×1015 amino-groups per cm2. In turn, this leads to a high surface density of the rhamnolipids attached to the surface.
The atmospheric plasma discharge may for example be atmospheric plasma discharge of argon, oxygen or hydrogen. The atmospheric plasma discharge may be of a mixture of any of these. For example, the atmospheric plasma discharge may be of a mixture of oxygen and hydrogen plasma discharge. In one preferred embodiment, the atmospheric plasma discharge is an argon plasma discharge. The parameters for the atmospheric plasma discharge may be power 10 to 100 W, such as 20 to 90 W, such as 30 to 80 W, such as 40 to 70 W, such as 50 to 60 W; flow rate 5 to 20 sccm (standard cubic centimetre per minute), such as 10 to 15 sccm; time 10 seconds (s) to 10 minutes (min), such as 20 s to 5 min, such as 30 s to 3 min; such as 1 to 2 minutes. The distance from the outlet of the plasma nozzle to the sample may be 0.5 to 2.5 cm, such as 1 to 2 cm, such as 1.2 to 1.8 cm, such as 1.4 to 1.6 cm, preferably 1.5 cm.
The process may be optimized by changing the plasma parameters (power, flow rate, time and distance).
One suitable combination of parameters for the atmospheric plasma discharge may be power 10 W, flow rate 20 sccm (standard cubic centimetre per minute), time 20 s and distance 5 mm. A further suitable combination of parameters may be power 100 W, flow rate 15 sccm (standard cubic centimetre per minute), time 5 min. Another suitable combination of parameters may be e.g. power 20 W, flow rate 10 sccm (standard cubic centimetre per minute), time 20 s and distance 15 mm.
The vacuum plasma discharge may for example be vacuum plasma discharge of argon, oxygen or hydrogen. The vacuum plasma discharge may be of a mixture of any of these. For example, the vacuum plasma discharge may be of a mixture of oxygen and hydrogen plasma discharge. In one preferred embodiment, the vacuum plasma discharge is an argon plasma discharge.
Preferably, the plasma discharge is vacuum plasma discharge.
The solution of (3-aminopropyl)triethoxysilane (APTES) monomers is a 2 to 10% (volume/volume, preferably 3 to 7% (volume/volume, such as 4 to 6% (volume/volume), even more preferred a 5% (volume/volume) APTES solution with ethanol as solvent.
The solution of cyclopropylamine monomers is a 2 to 10% (volume/volume), preferably 3 to 7% (volume/volume, such as 4 to 6% (volume/volume), even more preferred a 5% (volume/volume) cyclopropylamine solution with an organic solvent, such as ethanol.
The silicone surface that is to be coated may be subjected to the solution of (3-aminopropyl)triethoxysilane (APTES) monomers or cyclopropylamine monomers through immersion. The immersion may take place for 15 to 60 minutes, such as 20 to 40 minutes, preferably 30 minutes. Preferably, the immersion takes place at room temperature. After immersion, the silicone surface may be rinsed, preferably rinsed with ethanol.
The silicone surface that is to be coated may be subjected to the solution of (3-aminopropyl)triethoxysilane (APTES) monomers or cyclopropylamine monomers at room temperature.
Optionally, step b) above is followed by a step of subjecting the silicone surface that is to be coated to a temperature of 50 to 150° C., such as 70 to 130° C., such as 80 to 120° C., preferably 90 to 110° C., such as 95 to 105° C., even more preferred around 100° C., for a time period of 5 to 45 minutes, preferably, 10 to 30 minutes, such as 15 to 25 minutes, even more preferred around 20 minutes. Subjecting the silicone surface that is to be coated to a high temperature contributes to the stabilization of the APTES or cyclopropylamine coating.
In a specific embodiment, step 1) comprises the steps of a) subjecting the silicone surface that is to be coated to atmospheric or vacuum plasma discharge, preferably wherein the vacuum plasma discharge is performed using the following parameters: power 20 W, flow rate 10 sccm (standard cubic centimetre per minute), time 20 s and distance 15 mm, followed b) subjecting the silicone surface that is to be coated to a solution of (3-aminopropyl)-triethoxysilane (APTES) monomers in ethanol, preferably 5% (vol/vol) APTES, for a time period of 30 minutes. Optionally, step b) is followed by a step of subjecting the silicone surface that is to be coated to a temperature of 50 to 150° C., such as 70 to 130° C., such as 80 to 120° C., preferably 90 to 110° C., such as 95 to 105° C., even more preferred around 100° C., for a time period of 5 to 45 minutes, preferably, 10 to 30 minutes, such as 15 to 25 minutes, even more preferred around 20 minutes. Preferably, the silicone surface is thereafter cured at around 100° C., for a time period of 20 minutes.
Typically, such a process yields a surface having more than 6×1015 amino-groups per cm2, such as more than 7×1015 amino-groups per cm2, such as more than 8×1015 amino-groups per cm2. In turn, this leads to a high surface density of the rhamnolipids attached to the surface.
According to another embodiment of the method, step 1) comprises the steps of: i) subjecting the silicone surface that is to be coated to atmospheric or vacuum plasma discharge of argon in combination with (3-aminopropyl)-triethoxysilane (APTES) monomers or of argon in combination with cyclopropylamine monomers. The monomers are directly polymerized on the silicone surface during the plasma treatment. This results in the generation of amino groups on the silicone surface by polymerizing monomers. Surface functionalization using plasma technique can be used to apply either APTES monomers or cyclopropylamine monomers. An advantage of using plasma discharge for this type of direct application of monomers creating the surface functionalization is that it increases the precision and allows selection of which surfaces to treat and what surfaces to leave out. Another advantage is that, by direct application of surface functionalization through plasma discharge, the amount of monomers can be controlled by adjustment of plasma discharge process parameters (e.g. discharge power, gas flow, process times). Furthermore, precise application can be achieved by optimizing the angle of the plasma stream to local variations in surface angle of irregular silicone surfaces. Suitable angles are between 0° and 30°, such as 10° to 20°, such as 15°. Further, the distance from the outlet of the plasma nozzle to the sample may be 0.5 to 2.5 cm, such as 1 to 2 cm, such as 1.2 to 1.8 cm, such as 1.4 to 1.6 cm, preferably 1.5 cm.
Further parameters for the atmospheric plasma discharge may be power 10 to 100 W, such as 20 to 90 W, such as 30 to 80 W, such as 40 to 70 W, such as 50 to 60 W; flow rate 5 to 20 sccm (standard cubic centimetre per minute), such as 10 to 15 sccm; time 10 seconds (s) to 10 minutes (min), such as 20 s to 5 min, such as 30 s to 3 min; such as 1 to 2 minutes.
The process may be optimized by changing the plasma parameters (power, flow rate, time and distance).
One suitable combination of parameters for the atmospheric plasma discharge may be power 10 W, flow rate 20 sccm (standard cubic centimetre per minute), time 20 s and distance 5 mm. A further suitable combination of parameters may be power 100 W, flow rate 15 sccm (standard cubic centimetre per minute), time 5 min. Another suitable combination of parameters may be e.g. power 20 W, flow rate 10 sccm (standard cubic centimetre per minute), time 20 s and distance 15 mm.
Furthermore, a method as described above allowing for the polymerization of aminopropyl)-triethoxysilane (APTES) monomers or of cyclopropylamine monomers on the silicone surface is less time-consuming and more reproducible. In addition, the method is solvent-free. Furthermore, such a method is scalable to industry level. The monomer may be in a carrier gas. The carrier gas may be O2 or H2.
Optionally, step i) above is followed by a step of subjecting the silicone surface that is to be coated to a temperature of 50 to 150° C., such as 70 to 130° C., such as 80 to 120° C., preferably 90 to 110° C., such as 95 to 105° C., even more preferred around 100° C., for a time period of 5 to 45 minutes, preferably 10 to 30 minutes, such as 15 to 25 minutes, even more preferred around 20 minutes. Subjecting the silicone surface that is to be coated to a high temperature contributes to the stabilization of the APTES or cyclopropylamine coating.
In another specific embodiment, step 1) comprises the steps of a) subjecting the silicone surface that is to be coated to vacuum plasma discharge, preferably wherein the vacuum plasma discharge is performed using the following parameters: power 20 W, flow rate 30 sccm (standard cubic centimetre per minute), time 1 minute and distance 15 mm, followed by b) subjecting the silicone surface that is to be coated to a vapour of aminopropyl)-triethoxysilane (APTES) monomers in the vacuum chamber via a vacuum plasma discharge. The resulting plasma polymerization of APTES uses plasma sources to generate a gas discharge that provides energy to activate or fragment gaseous or liquid monomers in order to initiate polymerization. The amount of monomers can be controlled by adjustment of the process parameters. Further, compared to the method described above in which the surface to be coated is subjected to a solution of (3-aminopropyl)triethoxysilane (APTES) monomers in ethanol for a period of time, this method is more precise and less time-consuming. Thus, this process is suitable for series production, since it is more scalable to industry level. Moreover, this method does not necessitate the use of any solvents, which produce potentially hazardous chemical waste.
The APTES monomer vapours may be obtained by heating liquid APTES monomer close to the boiling point.
Preferably, the APTES monomer vapours are obtained by flushing argon gas through liquid APTES monomer.
Preferably, step 2) is performed using the following parameters: 20 W, 30 sccm argon flow-rate and 20 sccm APTES monomer vapours flow-rate, 1 minute.
Typically, such a process, especially when the APTES monomer vapours are obtained by flushing argon gas through liquid APTES monomer, yields a surface having more than 6×1015 amino-groups per cm2, such as more than 7×1015 amino-groups per cm2, such as more than 8×1015 amino-groups per cm2. In turn, this leads to a high surface density of the rhamnolipids attached to the surface.
Thus, in some embodiments, after step 1), the surface density of amino-groups is more than 6×1015 amino-groups per cm2, such as more than 7×1015 amino-groups per cm2, such as more than 8×1015 amino-groups per cm2.
In some embodiments, step 2) above is performed using carbodiimide chemistry. An advantage of this method is a stronger and more stable attachment of biosurfactant compared to coating through physical adsorption.
In one specific embodiment of the method, step 2 comprises the steps of 2a) mixing an aqueous solution of rhamnolipids with an aqueous solution comprising N-ethyl-N′-(3-dimethylaminopropyl) carbodiimide (EDC) and N-hydroxysuccinimide (NHS) at pH 4.5 to 6, preferably pH 5.5; 2b) increasing the pH to neutral pH, such as pH 7 to 7.5, preferably around pH 7.3 to 7.4, even more preferred pH 7.4 by the addition of NaOH; and 2c) subjecting the silicone surface that is to be coated to the mixture obtained in step 2b) for 1 to 24 h, preferably for 8 to 16 h, more preferred 10 to 14 h, such as around 12 h, at a temperature of 4 to 25° C.
In 2a) above, the ratio of rhamnolipid solution to the aqueous solution containing N-ethyl-N′-(3-dimethylaminopropyl) carbodiimide and N-hydroxy-succinimide may be between 1:1 to 10:1, such as 2:1 to 9:1, such as 3:1 to 8:1, such as 4:1 to 7:1, such as 6:1 to 5:1. Preferably, the ratio is 2:1 to 6:1, such as 3:1 to 5:1. In one preferred embodiment, the ratio is 4:1.
The step of mixing 2a) may be performed for 1 hour at 4° C.
The ratio of EDC to NHS in the aqueous solution used in step 2a) may be from 2:1 to 10:1, preferably around 4:1. A ratio of more than 1:1 is especially advantageous since this accelerates the reaction.
The aqueous solution of rhamnolipids may for example be a 4 mg/ml solution.
The NaOH added in step 2b) is preferably 1N NaOH.
For optimization of the covalent grafting process, the ratio between EDC and NHS and the concentration of rhamnolipids can be further optimized between 1:1 to 10:1, such as 2:1 to 9:1, such as 3:1 to 8:1, such as 4:1 to 7:1, such as 6:1 to 5:1. Preferably, the ratio is 2:1 to 6:1, such as 3:1 to 5:1. In one preferred embodiment, the ratio is 4:1.
Step 2c) can be carried out by immersing the silicone parts to be grafted with rhamnolipids, for example in 1 mL activated rhamnolipid solution, for 24 h at 4° C.
The methods described above may further comprise the step of washing the coated silicone surface obtained after step 2). The step of washing can for example comprise the steps of 3) rinsing the coated silicone surface obtained after step 2) with distilled water; and 4) drying the coated silicone surface under vacuum at room temperature.
The rhamnolipids used in the methods described above preferably comprise 70-85% (weight/weight), preferably 75% (weight/weight), mono-rhamnolipids and 15-30% (weight/weight), preferably 25% (weight/weight) di-rhamnolipids. The total amount of mono-rhamnolipids and di-rhamnolipids is 100% (weight/weight).
In one specific embodiment, the rhamnolipids comprise 75% (weight/weight) mono-rhamnolipids and 25% (weight/weight), di-rhamnolipids.
The rhamnolipids may have a purity of at least 85%, more preferably a purity of at least 90%.
In one embodiment of the method, the medical device is a voice prosthesis, a tracheostomy speaking valve, a holder for tracheostomy speaking valve, a silicone tube for the nasolacrimal duct, a tympanic ear tube, a breast implant, a nasal implant, a gastric band, a joint implant, a gluteal implant or a pelvic mesh, or urinary catheter; preferably wherein the medical device is a voice prosthesis, a tracheostomy speaking valve, or a holder for tracheostomy speaking valve; more preferably wherein the medical device is a silicone voice 100 prosthesis comprising a voice prosthesis valve, even more preferably wherein the surface coated with rhamnolipids comprise at least one of the sealing surfaces 108 of the voice prosthesis valve and/or at least one of the retaining flanges 102, 103 of the voice prosthesis. Coating at least one of the retaining flanges 102, 103 may prevent microbial growth that affect the strength of the retaining flanges negatively.
In another specific embodiment of the method, the medical device is a silicone voice prosthesis, wherein at least one of the retaining flanges of the voice prosthesis are coated with rhamnolipids. The rhamnolipids are covalently attached to the surfaces via linker comprising an amide bond. The linker may be —O—Si—(CH2)3—N—CO— or —O—(CH2)3—N—CO—. Preferably, the rhamnolipids comprise 70-85% (weight/weight), preferably 75% (weight/weight), mono-rhamnolipids and 15-30% (weight weight), preferably 25% (weight/weight), di-rhamnolipids. The total amount of mono-rhamnolipids and di-rhamnolipids is 100% (weight/weight). Preferably, the rhamnolipids have a purity of at least 85%, more preferably a purity of at least 90%. Coating one or more of the retaining flanges can prevent microbial growth affecting the strength of the retaining flanges negatively.
A specific method according to the present disclosure is shown in
Another specific method according to the present disclosure is shown in
General features applicable to the vice prosthesis disclosed herein as well as specific examples of such voice prostheses are described below.
Disclosed herein is a voice prosthesis for mounting in a fistula between trachea and esophagus, wherein at least a part of the voice prosthesis 100 comprises silicone and at least a part of said silicone being coated with rhamnolipids. The voice prosthesis is for mounting in a fistula or puncture of the tracheoesophageal party wall P.
The voice prosthesis 100 for mounting in a fistula between trachea T and esophagus E, comprises a tubular body 101 having a lumen; a valve disc 105 and a valve seat 106, arranged in the lumen of the tubular body 101, said valve disc 105 and said valve seat 106 controlling the communication through said lumen by interaction between said valve disc 105 and said valve seat 106; wherein at least a part of the voice prosthesis 100 comprises silicone and at least a part of said silicone being coated with rhamnolipids.
The rhamnolipids may comprise 70-85% (weight/weight), preferably 75% (weight/weight), mono-rhamnolipids and 15-30% (weight/weight), preferably 25% (weight/weight), di-rhamnolipids. The total amount of mono-rhamnolipids and di-rhamnolipids is 100% (weight/weight). Preferably, the rhamnolipids comprise 75% (weight/weight) mono-rhamnolipids and 25% (weight/weight), di-rhamnolipids.
The rhamnolipids may have a purity of at least 85%, more preferably a purity of at least 90%.
The rhamnolipids may be covalently attached to at least a part of the irregular and/or curved silicone surfaces. One advantage of such a coating is that the rhamnolipid coating is stable for a longer period of time than a rhamnolipid coating that is not covalently attached to the silicone surface.
The rhamnolipids may be covalently attached to the surface via a linker comprising an amide-bond.
The linker may be —O—Si—(CH2)3—N—CO— or —O—(CH2)3—N—CO—.
In one embodiment, the tubular body 101 comprises a distal and a proximal axial end, wherein the proximal end is provided with a esophageal retention flange 102 and the distal end is provided with a tracheal retention flange 103, and wherein at least a part of the tubular body 101, the esophageal retention flange 102 and/or the tracheal retention flange 103 comprises silicone and at least a part of said silicone being coated with rhamnolipids.
In another embodiment, the tubular body 101, the esophageal retention flange 102 and/or the tracheal retention flange 103 is made of silicone and said silicone being coated with rhamnolipids.
In another embodiment, at least a part of the valve disc 105 and/or the valve seat 106 comprises silicone and at least a part of said silicone being coated with rhamnolipids.
In yet another embodiment, the valve disc 105 and/or the valve seat 106 comprises silicone and said silicone being coated with rhamnolipids.
In one specific embodiment, the tubular body 101 comprises a distal and a proximal axial end, wherein the proximal end is provided with a esophageal retention flange 102 and the distal end is provided with a tracheal retention flange 103, and wherein at least a part of the tubular body 101, the esophageal retention flange 102 and/or the tracheal retention flange 103 comprises silicone and at least a part of said silicone being coated with rhamnolipids. The rhamnolipids are covalently attached to the surface via a linker comprising an amide-bond. The linker is preferably —O—Si—(CH2)3—N—CO— or —O—(CH2)3—N—CO—.
In another specific embodiment, the tubular body 101, the esophageal retention flange 102 and/or the tracheal retention flange 103 is made of silicone and said silicone being coated with rhamnolipids. The rhamnolipids are covalently attached to the surface via a linker comprising an amide-bond. The linker is preferably —O—Si—(CH2)3—N—CO— or —O—(CH2)3—N—CO—.
In another specific embodiment, at least a part of the valve disc 105 and/or the valve seat 106 comprises silicone and at least a part of said silicone being coated with rhamnolipids. The rhamnolipids are covalently attached to the surface via a linker comprising an amide-bond. The linker is preferably —O—Si—(CH2)3—N—CO— or —O—(CH2)3—N—CO—.
In another specific embodiment, the valve disc 105 and/or the valve seat 106 comprises silicone and said silicone being coated with rhamnolipids. The rhamnolipids are covalently attached to the surface via a linker comprising an amide-bond. The linker is preferably —O—Si—(CH2)3—N—CO— or —O—(CH2)3—N—CO—.
A voice prosthesis according to the present disclosure is shown in
The valve member 104 comprises a valve disc 105 and a valve seat 106. The valve disc 105 and the valve seat 106 are arranged in the tubular body 101. The valve disc 105 is arranged on a valve hinge 107, which in turn connects the valve disc 105 to the tubular body 101.
The valve disc 105 and/or the valve seat 106 may be manufactured in a rigid material resistant to bacterial and/or fungal growth, such as a fluorine polymer or a metal. An example of a suitable fluorine polymer is polyvinylidene difluoride (PVDF). Examples materials resistant to bacterial and/or fungal growth are stainless steel and titanium. Alternatively, the valve disc 105 and/or the valve seat 106 are made directly of silicone. The valve seat 106 is arranged circumferentially of the lumen of the valve body 107. The valve seat 106 may also be arranged in a plane that is traversing the lumen of the valve body 107. The valve hinge 107 may be manufactured in a suitable elastic material with good flexibility memory, such that the closing force will be adequately maintained for a long period of time. As suitable such elastic material is silicone.
Silicone surfaces on the voice prosthesis 100 may be coated with rhamnolipids. This is specifically beneficial, since the silicone surfaces on the voice prosthesis 100, such as the valve disc 105 and the valve seat 106 or the tubular body 101 are interacting during use to allow for a closing of the valve disc 105 against the valve seat 106.
Other silicone surfaces of the voice prosthesis 100 that may be coated with rhamnolipids as disclosed herein are one or more of the esophageal retention flange 102, the tracheal retention flange 103, and the at least one sealing surface 108 of the voice prosthesis valve.
The rhamnolipids, on the valve disc 105 and valve seat 106, respectively, especially on at least one of the sealing surfaces 108 of the voice prosthesis valve, will provide for a reduced risk of biofilm formation, which in turn reduces the risk of valve malfunction. However, additionally, the glycosyl head groups on the rhamnolipids, on the valve disc 105 and valve seat 106, respectively, especially on at least one of the sealing surfaces 108 of the voice prosthesis valve, have been found to reducing the risk for the valve disc 105 sticking to the valve seat 106, and therefore also reducing the risk for the valve member 104 to function improperly for this reason.
Although the present invention has been described above with reference to specific embodiments, it is not intended to be limited to the specific form set forth herein. Rather, the invention is limited only by the accompanying claims and other embodiments than the specific embodiments described above are equally possible within the scope of these appended claims.
In the following, examples illustrating the devices and methods of the present disclosure are presented.
The bacteria Pseudomonas aeruginosa 89 is used as the biosurfactant producing strain, cultivated in Siegmund-Wagner (SW) medium, which is a mineral salt medium containing 0.7 g KH2PO4, 0.9 g, 2 g NaNO3, 0.4 g MgSO4.7·7H2O, 0.1 g CaCl2·2H2O and 2 mL of trace elements per 1000 mL distilled water. The trace element solution is prepared by dissolving 2 g FeSO4·7H2O, 1.5 g MnSO4·H2O and 0.6 g (NH4)6Mo7O24 in 1000 mL distilled water. In the final step the pH is adjusted to 6.7 and the medium is sterilized at 121° C. for 15 minutes in an autoclave. Rhamnolipids (R89) are extracted from the acidified (pH 2.4 H2SO4, 6M) cell-free supernatant, using ethyl acetate. The organic phase is evaporated to dryness under vacuum conditions. The composition (i.e. the percentage of mono-rhamnolipids and di-rhamnolipids) of the rhamnolipid crude extracts can be confirmed with ESI-MS (Electrospray Ionization Mass Spectrometry) analysis.
AC7 (a biosurfactant, BS) was extracted from cultures of Bacillus subtilis AC7 and was used as a comparative compound in the examples below. AC7 is mainly composed of surfactin.
Static contact angle measurement was performed by depositing water drops with controlled volume in a controlled way.
In short, the static contact angle analysis was performed using the Attention Theta instrument (Biolin Scientific, Gothenburg, SE), equipped with automatic drop deposition system, and software OneAttension software (Biolin Scientific, Gothenburg, SE). Measurements were carried out in static conditions using water drops with 5 μL volume, at least 3 drops were deposited on each type of samples.
The static contact angle is herein also referred to as contact angle.
Presence of biosurfactants increases the wettability of the silicone surface and thereby lower the contact angle of the surface. High wettability results in difficulty for microbes to adhere to the surface due to the surface being wet and slippery, which is desirable, whereas hydrophobic surfaces enhance bacterial/microbial adherence.
Silicone samples (silicone elastomeric discs, SEDs), uncoated or coated with biosurfactant as described herein, were submerged in 1 mL of S. aureus and C. albicans suspensions at the concentration of 1×107 CFU/mL and incubated at 37° C. for 24, 48, and 72 h. S. aureus was suspended in Tryptic Soy Broth (TSB) supplemented with 1% (weight/volume) glucose. C. albicans was suspended in PBS (phosphate buffered saline) supplemented with 10% (volume/volume) fetal bovine serum.
For C. albicans, after 90 minutes of incubation, SEDs were transferred onto new plates containing fresh medium.
For S. aureus and C. albicans, every 24 h, SEDs were transferred onto new plates containing fresh media. The fresh medium for S. aureus was TSB and for C. albicans Yeast Nitrogen Base Dextrose (YNBD) broth supplemented with 10% (volume/volume) fetal bovine serum. At the end of the incubation period, the medium was removed, and SEDs were washed twice with PBS to remove non-adherent cells.
The inhibitory effect of the biosurfactants was studied after 24 h, 48 h and 72 h by Crystal Violet staining (biomass) and MTT assay (metabolic activity) assessments.
Silicone samples (silicone elastomeric discs, SEDs) were cleaned with ethanol and then immersed in a solution of biosurfactant (BS) (2 mg/mL) in PBS (phosphate buffered saline) at pH 7 for 24 h at 37° C., at 180 rpm. The biosurfactant was R89BS or AC7. Control SEDs were immersed in 1 mL of PBS only. The BSs solutions were aspirated and SEDs were dried.
As can be seen in Table 1, a silicone disc coated with physically adsorbed rhamnolipids has a lower contact angle than an uncoated silicone disc. This decrease in contact angel confirms the presence of rhamnolipids since the rhamnolipids influence the wettability of the silicone.
The in vitro evaluation of the anti-biofilm activity of AC7 (a lipopeptide from Bacillus subtilis AC7) and R89 physically adsorbed on silicone elastomeric discs (SEDs) against biofilm-producer pathogenic strains (S. aureus ATCC 6538, C. albicans IHEM 2894) was performed as described above (microbiological evaluation).
The two biosurfactants were able to significantly counteract fungal biofilm formation. In particular, the highest biofilm inhibitory activity was observed with R89 at all incubation times both on biofilm biomass and on cells viability, with values respectively of 61% and 53% at 72 h of incubation (Table 2a).
A significant inhibition was observed on S. aureus biofilms with both biosurfactants. In particular, as also observed on C. albicans, R89 resulted to be the most active in S. aureus inhibition, with biofilm biomass and cells viability inhibitions of respectively 70% and 73% after 72 h incubation (Table 2b).
Thus, even if AC7 gives a slightly lower contact angle value, the results from the biological evaluation as shown in Tables 2a and 2b clearly indicate that R89 (rhamnolipids) prevent the formation of a biofilm of both yeasts (C. albicans (Table 2a)) and bacteria (S. aureus (Table 2b)) to a larger degree than AC7.
To generate reactive sites for subsequent adsorption of the biosurfactants, silicone discs were treated with argon plasma (5 min, flow 15 sccm (standard cubic centimetre per minute), power 100 W). Samples were then dipped into a 0.2% (weight/volume) AC7 or 0.2% (w/v) R89 aqueous solution at 37° C. for 24 h at 140 rpm.
Compared to Experiment A (physical adsorption of biosurfactant only), a lower contact angle value is achieved by pretreating the silicone with plasma before coating with AC7 or R89. This implies that by pretreating the silicone surface with argon plasma, more biosurfactant is attached in the following step.
The in vitro evaluation of the anti-biofilm activity against biofilm-producer pathogenic strains (S. aureus ATCC 6538, C. albicans IHEM 2894) was performed as described above (microbiological evaluation).
Every 24 h, SEDs were transferred onto new plates containing fresh media. At the end of the incubation period, the growth medium was removed, and SEDs were washed twice with PBS to remove non-adherent cells.
As seen in Tables 3a and 3b, silicone/plasma-biosurfactant promoted a significant inhibition of biofilm formation for all the tested strains.
For C. albicans (Table 3a) the highest inhibition of biofilm formation was detected with R89 and the activity was stable at all incubation times. In particular, biomass and cell viability of fungal biofilm were respectively decreased of 71% and 74% at 72 h incubation.
As far as S. aureus is concerned (Table 3b), the highest inhibition of biofilm formation was again detected with R89BS. In particular, biofilm biomass and cell viability were averagely inhibited of 86% at 72 h incubation.
Thus, the results from the biological evaluation as shown in Tables 3a and 3b clearly show that R89 (rhamnolipids) physically adsorbed to an argon plasma treated silicone surface prevent the formation of a biofilm of both yeasts (C. albicans (Table 2a)) and bacteria (S. aureus (Table 2b)) to a larger degree than AC7. This indicates that rhamnolipids are more effective than AC7 in preventing the formation of biofilms on silicone surfaces.
Silicone substrates pretreated with vacuum plasma discharge of argon were immersed in a solution of 3-aminopropyltriethoxysilane (APTES) in ethanol (5% v/v) for 30 min at room temperature, followed by rinsing with ethanol. Subsequently, samples were cured at 100° C. for 20 min. The covalent grafting of BSs on silicone surfaces was obtained via carbodiimide chemistry. Briefly, 1 mL of biosurfactant aqueous solution (4 mg/mL) was mixed with 1 mL of an aqueous solution containing N-ethyl-N′-(3-dimethylaminopropyl) carbodiimide (EDC)/N-hydroxysuccinimide (NHS) (4/1) (pH 5.5) for 1 h at 4° C. Then, the pH was raised to 7.4 by adding drops of 1N NaOH. APTES- (or cyclopropylamine-) modified silicone substrates were immersed in 1 mL biosurfactant activated solution for 24 h at 5° C. and then washed three times using distilled water and dried under vacuum overnight at room temperature.
While the contact angle value of plasma treated silicone samples (Silicone/P) is lowest, this result is not stable over time but increases within hours. This is shown in
Covalent grafting allows lower amounts of biosurfactant attached compared to physical adsorption. However, the attachment of the covalently grafted R89 is stronger and more stable, as can be seen as the contact angle value of the plasma treated silicone samples coated with APTES and R89 though covalent grafting is lower than that of the silicone samples coated with R89 through physical adsorption (see
The in vitro evaluation of the anti-biofilm activity against biofilm-producer pathogenic strains (S. aureus ATCC 6538, C. albicans IHEM 2894) was performed as described above (microbiological evaluation).
As can be seen in Table 4b, the R89 covalent grafting on APTES modified silicone/P discs allowed to maintain the anti-biofilm activity up to 72 hours of incubation. C. albicans biofilm formation was reduced in term of biomass and metabolic activity by 80% and 78% respectively, at the last time-point (72 h).
Biomass and metabolic activity of S. aureus biofilms were respectively reduced by 98% and 93% at 72 h (see Table 4c).
The effect of these modified surfaces was constant, or even incremental, over time.
In conclusion, the results show a decreased biomass and cell metabolic activity on SEDs with covalently grafted R89 as compared to uncoated controls. Furthermore, the effect of reduced biofilm formation is larger than for silicone surfaces with physically adsorbed rhamnolipids (Tables 2a and 2b) and also for argon plasma treated silicone surfaces with physically adsorbed rhamnolipids (Tables 3a and 3b).
Thus, it is clearly shown that a silicone surface being less prone to biofilm formation can be achieved by covalently grafting rhamnolipids on APTES-modified silicone surfaces pre-treated with argon plasma.
The effect of different methods of introducing amino-groups on a silicone surface was investigated.
Test samples A were prepared by pretreating silicone samples by argon plasma discharge in a vacuum chamber (20 W for 20 seconds) followed by immersion in a solution of (3-aminopropyl)triethoxysilane (APTES) monomers in ethanol (5% (vol/vol) APTES) for a time period of 30 minutes. Thereafter the samples were rinsed with ethanol and cured at 100° C. for a time period of 20 minutes, whereby the APTES coating was stabilized.
Test samples B were prepared by pretreating silicone samples with argon plasma discharge in a vacuum chamber, in continuous wave modality (20 W for 1 minute). While still in the vacuum chamber, the silicone sample were subjected to APTES monomer vapours obtained by heating the liquid monomer close to the boiling point. Polymerisation of APTES monomers on the silicone surface was performed via a vacuum plasma discharge in the pulsed wave modality at 20 W, 30 sccm argon flow-rate and 20 ccm APTES monomer vapours flow-rate for 1 minute.
Test samples C were prepared by pretreating silicone samples with argon plasma discharge in a vacuum chamber, in continuous wave modality (20 W for 1 minute). While still in the vacuum chamber, the silicone sample were subjected to APTES monomer vapours obtained by flushing argon gas through the liquid monomer making it “bubble”. Polymerisation of APTES monomers on the silicone surface was performed via a vacuum plasma discharge in the pulsed wave modality at 20 W, 30 sccm argon flow-rate and 20 ccm APTES monomer vapours flow-rate for 1 minute.
The number of amino-groups on the surface of the silicon samples were measured by an Acid Orange assay. In short, the samples were immersed an acidic aqueous solution (pH=3) of Acid Orange II (Formula I below) with concentration of 0.175 mg/mL overnight. During this time, the amino-groups present on the silicon surface bound to molecules of Acid Orange II (AO) with a 1:1 ratio.
Samples were thereafter rinsed with pH 3 aqueous solution and immersed in a basic detachment solution (aqueous solution at pH=12) for 30 minutes. In this way, all AO molecules that reacted with amino-groups were released into solution. For the quantification of AO, and therefore amino-groups, the detachment solution was sampled into a 96-well microtiter plate and absorbance was measured at 485 nm in Varioskan™ LUX multimode microplate reader. A calibration curve with different AO concentrations (ranging from 0.000313 mg/mL to 0.025 mg/mL) previously performed was used to quantify the amount of AO released from the samples and thereby the number of amino-groups groups present on the samples.
The results are shown in Table 5 below.
Samples A (in which the pretreated silicon surfaces were subjected to a solution of APTES in ethanol) and Samples C (in which the pretreated surfaces were subjected to APTES monomer vapours obtained by passing argon gas through the liquid monomer and a polymerization of the APTES monomers performed via a vacuum plasma discharge) yielded a higher density of amino-groups on the surface as compared to Samples B (in which the pretreated surfaces were subjected to APTES monomer vapours obtained by heating the liquid monomer close to the boiling point and a polymerization of the APTES monomers performed via a vacuum plasma discharge).
Thus, when rhamnolipids are covalently attached to surfaces treated as in Samples A, B or C, a high surface density of rhamnolipids is achieved. Specifically, when rhamnolipids are covalently attached to surfaces treated as in Samples A or C, a particularly high surface density of rhamnolipids is achieved.
Number | Date | Country | Kind |
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2150521-9 | Apr 2021 | SE | national |
Filing Document | Filing Date | Country | Kind |
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PCT/SE2022/050393 | 4/22/2022 | WO |