SWELLABLE ANTIMICROBIAL FIBRE

Abstract

A swellable biocompatible material and method of making the same. The material comprises a water-absorbing swellable polymer infused with povidone-iodine and a water-soluble control compound configured to control a release of iodine form the material. Example swellable polymers includes polysaccharides and hydrocolloid forming compounds.

Claims

1. A swellable biocompatible material formed by a method of contacting a water-absorbing swellable polymer with a solution containing an antimicrobial to allow the antimicrobial to be absorbed by the swellable polymer, the solution comprising: water; povidone-iodine; and a water-soluble control compound configured to control a release of iodine from the material.

2. The material as claimed in claim 1 wherein the swellable polymer comprises: a polysaccharide; a polysaccharide based material; or a hydrocolloid forming compound.

3. The material as claimed in claim 1 wherein the water-absorbing swellable polymer comprises any one or a combination of: an alginate; chitosan; chitin; pectin; carboxymethyl cellulose; hydroxypropyl methylcellulose; gellan; konjac; psyllium; or a synthetic polymers.

4. The material as claimed in claim 1 wherein the water-soluble control compound comprises a polyether, an alkyl ether, a glycol, a polyol or a compound having a C—O—C linkage.

5. (canceled)

6. The material as claimed in claim 1 wherein the solution further comprises a polar organic solvent.

7. (canceled)

8. (canceled)

9. A swellable biocompatible material comprising: a water-absorbing swellable polymer; povidone-iodine; and a water-soluble control compound configured to control a release of the iodine from the swellable polymer.

10. The material as claimed in claim 9 wherein the swellable control compound comprises any one or a combination of: a polysaccharide; a polysaccharide based material; a hydrocolloid forming compound; an alginate; chitosan; chitin; pectin; carboxymethyl cellulose; hydroxypropyl methylcellulose; gellan; konjac; psyllium; or a synthetic polymers.

11. The material as claimed in claim 9 wherein the water-soluble control compound comprises a polyether, an alkyl ether, a glycol, propylene glycol, a polyol or a compound having a C—O—C linkage, polypropylene glycol or polyethylene glycol.

12. The material as claimed in claim 9 wherein the material comprises the water-soluble control compound in an amount of 5 to 40 wt based on a total weight of the material.

13. The material as claimed in claim 9 wherein the material comprises the povidone-iodine in an amount of 0.5 to 40 wt % based on a total weight of the material.

14. (canceled)

15. (canceled)

16. A method of forming a swellable biocompatible material comprising: providing a solution comprising: water; povidone-iodine; a water-soluble control compound configured to control a release of iodine from the material; and optionally a polar organic solvent; contacting a water-absorbing swellable polymer with the solution to enable at least the povidone-iodine to be absorbed by the swellable polymer; and removing the water and/or allowing the swellable polymer to dry.

17. (canceled)

18. The method as claimed in claim 16 wherein the step of contacting the swellable polymer with the solution comprises soaking said polymer in the solution.

19. The method as claimed in claim 16 wherein the step of contacting the swellable polymer with the solution comprises spraying the solution onto the swellable polymer.

20. The method as claimed in claim 19 wherein: the swellable polymer is moved or conveyed relative to at least one spray nozzle or head to spray the solution onto the swellable polymer; or the at least one spray nozzle or head is moved or conveyed relative to the swellable polymer to spray the solution onto the swellable polymer.

21. The method as claimed in claim 16 wherein the step of contacting the swellable polymer with the solution comprises contacting said polymer with said solution within a pressure vessel and applying a pressure to the solution to facilitate the absorption of the povidone-iodine into the swellable polymer.

22. The method as claimed in claim 16 wherein the swellable polymer comprises any one or a combination of: a polysaccharide; a polysaccharide based material; a hydrocolloid forming compound; an alginate; chitosan; chitin; pectin; carboxymethyl cellulose; hydroxypropyl methylcellulose; gellan; konjac; psyllium; or a synthetic polymers.

23. The method as claimed in claim 16 wherein the water-soluble control compound comprises any one or a combination of polyether, an alkyl ether, a glycol, a polyol or a compound having a C—O—C linkage.

24. The method as claimed in claim 16 wherein the material is fibre-based, sliver, roving and/or a non-woven material or the material is a woven or knitted material.

25. A wound dressing comprising the material as claimed in claim 1.

26. The material as claimed in claim 1 further defined as any one of the following: a nasal packing material; a dental packing material; a suture; or a seton.

Description

BRIEF DESCRIPTION OF DRAWINGS

[0038] A specific implementation of the present subject matter will now be described, by way of example only, and with reference to the accompanying drawings in which:

[0039] FIG. 1 illustrates schematically apparatus for introducing povidone-iodine (PVP-I) to a swellable biocompatible material including a perforated drum and a solution dispensing container;

[0040] FIG. 2 illustrates schematically a variation of the apparatus of FIG. 1 further comprising a pump located between the perforated drum and the pressure vessel;

[0041] FIG. 3 illustrates schematically selected components for the introduction of PVP-I to the swellable material using a pressurized reaction vessel;

[0042] FIG. 4 illustrates schematically apparatus for introducing PVP-I to the swellable polymer comprising a conveyer system to laterally translate the swellable material adjacent spray heads adapted to spray the PVP-I solution onto the conveyed swellable material; and

[0043] FIG. 5 illustrates schematically apparatus for introducing povidone-iodine (PVP-I) to a swellable biocompatible material or non-swellable material comprising an impregnation trough containing a solution, dipping guide rollers and a pair of mangling rollers;

[0044] FIG. 6 illustrates schematically apparatus for introducing povidone-iodine (PVP-I) to a swellable biocompatible material or non-swellable material comprising an impregnation trough containing a solution, dipping guide rollers and a pair of mangling rollers, according to a further specific implementation;

[0045] FIG. 7 illustrates schematically apparatus for introducing povidone-iodine (PVP-I) to a swellable biocompatible material or non-swellable material comprising an impregnation trough containing a solution, dipping guide rollers and a pair of mangling rollers, according to a further specific implementation;

[0046] FIG. 8 illustrates schematically apparatus for introducing povidone-iodine (PVP-I) to a swellable biocompatible material or non-swellable material comprising an impregnation trough containing a solution, dipping guide rollers and a pair of mangling rollers, and a drying enclosure according to a further specific implementation;

[0047] FIG. 9 is a graph of zone of inhibition versus available iodine present within the swellable material using bacteria types Staphylococcus and Klebsiella.

DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS OF THE INVENTION

[0048] The present antimicrobial swellable fibre is suitable for the manufacture of a non-woven felt-like material, a woven or knitted material that, in turn, may be utilised as a wound dressing for the treatment of a variety of different types of wound from cuts and grazes to more serious burns, ulcers and the like where exudate management is critical. The present material is conveniently formed from an infusing, soaking, immersing or dyeing process in which the fibres, sliver, roving, a woven, a non-woven or a knitted material is introduced to a generally aqueous solution containing povidone-iodine (PVP-I). The present materials and processes provide processing parameters to produce highly swellable materials incorporating ‘available’ iodine within the fibre/yarn core and at the fibre/yarn surface. The iodine is in a form of an iodine complex and included at a concentration level sufficient to provide antimicrobial activity. Such concentration levels may be of the order of greater than 1 wt % ‘free’ iodine within a total weight of fibre. The present materials and processes are specifically designed to provide a material having a desired moisture vapour transmission rate (MVTR), physical integrity—so as not to degrade when exposed to exudate and in a moisture absorbed swollen configuration, in addition to providing controlled and sustained antimicrobial release at the wound.

[0049] The present materials and methods may utilise a variety of different primary polymers including natural or synthetic materials. Such primary polymers are moisture absorbing swellable polymers and include for example polysaccharides or polysaccharide based materials, hydrocolloids, biopolymers. Preferred forms of primary polymers are water-soluble polymers such as but not limited to a polysaccharide alginate.

[0050] The present fibre and methods may utilise additional compounds to further control the release of iodine from the fibre. Such additional components may include secondary water-soluble control compounds such as polyethers, alkyl ethers, a glycol such as propylene glycol (PG), a polyol or a compound having a C—O—C linkage such as polypropylene glycol (PPG) or polyethylene glycol (PEG).

[0051] The present examples describe procedures developed to incorporate PVP-I into alginate and similar biomaterials in various forms such as fibres, sliver, roving, non-woven, woven or knitted. The present methods all include providing a solution containing solvated PVP-I and then contacting a moisture absorbing swellable polymer with the solution to allow at least the PVP-I to be absorbed by the polymer. As will be appreciated, the resulting materials include a swellable polymer having PVP-I absorbed within the fibres of the material and also PVP-I adsorbed at the fibre surfaces. This dual presence of PVP-I provides at least two mechanisms of release. For example, the PVP-I adsorbed at the fibre surfaces may be released quickly and/or immediately as the wound dressing is brought into contact with the wound whilst absorbed PVP-I (incorporated at the fibre/yarn core) may be adapted for slower more sustained release over time. The water-soluble control compound also present within the fibres/yarn of the material provides further control of the release of ‘free’ iodine to promote a sustained release.

EXAMPLES

[0052] Various example methods may be used in the manufacture of a swellable biocompatible material according to the present invention. Such methods may in i) batchwise processing using for example an open or pressurised chamber, or ii) continuous manufacture for example using a rotatable drum at ambient or elevated pressure or a conveyor system, or iii) batch or continuous manufacture system using an impregnation trough and mangling rollers.

[0053] Generally and with reference to Table 1 for the concentrations and amounts of materials used, the solutions were prepared using various percentages (based on the weight of biomaterial to be treated) of PVPI, water, IPA (and/or acetone), PEG (and/or PG). The required PVPI was weighed into water or water/PEG or PG and either dissolved manually or with a Greaves small high shear mixer. This was then followed by the addition of the rest of substances required and mixing until a homogeneous bulk solution was obtained for dyeing.

Initial Example—Batchwise

[0054] The swellable moisture-absorbing material may be prepared via a simple ‘dyeing’ of the material with the PVP-I. In such a method, a vessel, chamber or tank may be used to contain the PVP-I solution. In certain examples, a polymer based non-woven felt-like material may then be dipped, placed or soaked in the solution according to a conventional dyeing process. Such a process may be undertaken at ambient pressure and temperature.

[0055] In particular, an alginate felt having the dimensions 65 cm×130 cm was folded carefully without stretching to fit into a dyeing vessel containing half of the dyeing solution. The felt now folded (e.g. 20 cm×20 cm dimension) was transferred into the vessel (e.g. a 10-litre bucket) and pressed into the solution using a paddle or any non-sticky device with a flat bottom. The second half of the solution was then poured on top of the felt and the felt pressed down gently until all the surface covered uniformly with the solution. The gentle pressing down and moving the material around in the vessel continued until all the solution was absorbed into the material-. The dyed material was taken out, placed on top of a flat polyethene black bag and gently unfolded and left under extraction system in the fume cupboard to dry for at least 4 hours. During drying, the materials was turned so that both sides were equally dried. After drying properly, the material was folded and put inside a sealed silver coated bag and stored for analysis. On occasions, portions of the dyed material were cut, left exposed in the lab without cover and observed for colour changes to determine the stability of PVI in the materials.

[0056] Various thicknesses or widths of non-wovens were produced from the single layer treated material. To produce a double layer treated felt, two single layer treated felts of the same size or a single layer treated felt folded in half was used. One side of the felt was placed on a clean flat surface and the other side of the same felt (top side) was uniformly smeared thinly with 1-3% w/w solution of high G alginate containing the same amount of PVPI and PEG or PG as used for the single layer treatment. The felt was then folded into half with the smeared faces together or if using two separate single layer treated felts, the second layer was then carefully placed symmetrically on the smeared top and a uniform pressure applied to binder the felts together. Such pressure was achieved by placing a flat plate of slightly bigger dimension and containing uniformly distributed weights on top of the combined felt and leaving it in this position for at least 2 h. At end, the felts (now combined) was removed, hung together with foldback clips (paper clamp binder clips) to prevent excessive shrinkage and dried properly under extraction system for at least 5 h.

[0057] To produce a triple layer treated felt, three equal separate layers of a treated single layer felt were used. One layer was smeared on both sides with high G alginate/PVPI/PEG solution described above, then sandwiched between the other two layers and treated as above.

[0058] For fibres, they could be dyed stuck together and continuous as would be the case for roving, but best results were obtained when the fibres were in staple form, properly separated and opened. Some fibres contained spin finish such as Tween 20 (up to 3.5%) and treated without problem. The solution preparation and material treatment were as described above for non-woven. During treatment, before and after drying, some of the staple fibres were observed to roll into little balls. But after drying, they were soft and easily opened.

TABLE-US-00001 TABLE 1 Incorporation of PVPI into biomaterials through ‘dyeing’ process. Quantity (%, g on the weight of sample or material, OWM for treatment Amount of IPA Example Batch No. Sample form sample g PVPI Water PG PEG (IPA:Fibre) Acetone (Ace:Fibre) 1 P-170510-HM/ High M-Alg.- 120 6.7%, 16.7%, 8.3%, — — (3.33:1) 400 g PVPI/PG/Dyed psyllium staple fibres ~8 g 20 g 10 g (opened) 2 P-170602-HM/ High M-Alg.- 120 3.3%, 25%, — — (3.33:1) 400 g — PVPI/ Dyed psyllium staple fibres 4 g 30 g (opened) 3 P-170323-HM/ High M-Alg.- 106 8.5%, 49%, — — (3.77:1) 400 g — PVPI/Dyed psyllium staple fibres 9 g ~52 g (opened) 4 P-170512-HM/ High M-Alg.- 89 10%, 51% — 14.6%, (3.37:1) 300 g — PVPI/PEG/Dyed psyllium staple fibres 8.85 13 g (opened) 5 AMS-14-2AP/ High G-Alg./CMC 68 10%, 53%, 15%, (3.38:1) — PVPI/PEG/Dyed staple fibre 6.8g 36 g 10.2 230g 6 HM-181030/ PVPI/ High M alginate 107 10% 188% — 15% (3.5:1) 375g — PEG/Dyed/l fibres (opened) 10.7 g 201 g 16.05 g 7 HM-181030/ PVPI/ High M alginate 108 15% 53% — 15% (3.5:1) 378 g — PEG/Dyed/2 fibres (opened) 16.2 g 57.2 g 16.2 g 8 HG-181107/PVPI/ High G alginate 111 10% 50% — 15% (4:1) 444 g — PEG/Dyed/l fibres (opened) 11.1 g 55.5 g 16.6 g 9 HG-181107/PVPI/ High G alginate 111 15% 50% — 15% (4.2:1) 471 g — PEG/Dyed/2 fibres (opened) 16.65 g 55.5g 16.65 g 10 P-181128 -HM/ Single layer High M 1.5 22.7% 40.7% 20.7% (3.6:1) 31 g PVPI/PEG/Dyed Alg./psyllium felt 0.34 g 0.61g 0.31 g (XIRAMS21S) produced by AMS from Xiros fibres (XIRAMS 21) 11 XIRAMS-181204/ XIRAMS 21 85 15.3% 53% — 15.3% (3.53:1) — PVPI/PEG/Dyed/1 13.0 g 45 g 13 g 300 g (XIRAMS21S) 12 XIRAMS-190819/ XIRAMS 21 PVPI/PEG/Dyed/1 (XIRAMS 2 IS) 13 XIRAMS-190819/ XIRAMS 21 2 pieces of a single layer High M Alginate/psyllium felt producedby AMS from Xiros fibres PVPI/PEG/Dyed/2 and dyed with PVPI (XIRAMS-PVPI/PEG/Dyed/l) were taken, each smeared thinly on one (XIRAMS 21D) side with Alg./PVPI/PEG solution, stuck together and left under pressure for at 2 h to properly bind and then dried well under extraction system. 14 XIRAMS-181204/ XIRAMS 21 As above in example 13 except that 3 pieces of the single layer dyed felt (XIRAMS S21) were PVPI/PEG/Dyed/3 used and two sides of the middle layer smeared thinly with Alg./PVPI/PEG solution before (XIRAMS 2IT) sandwiching between the other two layers.

TABLE-US-00002 TABLE 2 Some examples of fluid absorbency and retention properties of some alginate, alginate/psyllium fibres or felt dyed with PVPI containing PG or PEG. Absorbency, g/g (Retention, %) Solution A Saline Example/Batch No. 1 min 30 min 1 min 30 min 1/ 25.06 33.38 30.68 30.80 P-170510-HM/PVPI/PG/Dyed (74) (67) (74) (69) 2/ 26.81 25.80 29.54 29.69 P-170602-HM/PVPI/Dyed (74) (75) (87) (84) 3/ 22.45 21.92 24.43 26.04 P-170323-HM/PVPI/Dyed (76) (75) (73) (68) 4/ 30.52 25.56 31.72 28.76 P-170512-HM/PVPI/PEG/Dyed (70) (67) (76) (73) 5 20.28 21.95 25.18 21.38 AMS-14-2AP/PVPI/PEG/Dyed (54) (51) (51) (59) 6 31.17 28.17 30.79 33.92 HM-181030/PVPI/PEG/Dyed/1 (80) (76) (84) (70) 7 22.60 24.32 25.83 27.48 HM-181030/PVPI/PEG/Dyed/2 (85) (78) (82) (88) 8 10.75 20.46 18.99 22.14 HG-181107/PVPI/PEG/Dyed/1 (45) (33) (65) (58) 9 13.85 14.59 17.00 22.81 HG-181107/PVPI/PEG/Dyed/2 (58) (54) (48) (54) 10 P-181128-HM/PVPI/PEG/Dyed (XIRAMS 21S) 11 23.66 15.74 12.06 27.55 XIRAMS-181204/PVPI/PEG/Dyed/1 (55) (64) (60) (69) (XIRAMS 21S) 12 XIRAMS-190819/PVPI/PEG/Dyed/1 (XIRAMS 21S) 13 XIRAMS-190819/PVPI/PEG/Dyed/2 (XIRAMS 21D) 14  9.69  8.40 10.04  9.98 XIRAMS-181204/PVPI/PEG/Dyed/3 (36) (31) (66) (60) (XIRAMS 21T)

[0059] Accordingly, the present method provides a versatile processing route for the incorporation of PVPI into fibre, yarn, sliver, roving etc -based materials (including wovens, non-wovens and knitted structures). The present processes and materials are advantageous in that: [0060] PVPI can be dissolved homogeneously and applied to a substrate completely and easily. [0061] the solvent(s) used are miscible to any extent with water and other additives such as diols (e.g. propylene glycol) or polyols (e.g. polyethylene glycol) that may be in the composition [0062] the main liquid(s) used are PVPI carrier(s) only and do not react with PVPI or other chemicals in the composition [0063] the main media are volatile solvents that are easily removed from the substrate/PVPI/additives composition or system after application by simple extraction.

[0064] The organic solvents used are preferably non-toxic alcohols, ketones, acetates or mixtures. Such solvents may be incorporated at 2:1 to 5:1 ratio relative to the substrate. Similarly, as described herein, the dyeing process could also be achieved by spraying the substrates from a pressurised vessel or can filled with a solution of PVPI/PEG (or PG)/IPA/water.

[0065] As shown in Table 2, based on the materials of the initial examples, the process improved significantly the fibre and felt strength, absorbency and iodine retention across all examples especially those containing high G alginates.

TABLE-US-00003 TABLE 3 Examples of iodine contents of some alginate, alginate/psyllium fibres or felt dyed with PVPI containing PG or PEG. Iodine Content Amount of In-house PVPI titration % used Available (on the External iodine weight of results (after fibre or Total samples felt, owf) Iodine extracted Example/Batch No. (%) (mg/Kg) overnight) Commercia product, Inadine ™ n/a 1600 1.0 1/ 6.7 Not 0.1 P-170510-HM/PVPI/PG/Dyed Tested 2/ 3.3 1200 0.8 P-170602-HM/PVPI/Dyed 3/ 8.5 Not 1.2 P-170323-HM/PVPI/Dyed Tested 4/ 10 2100 1.2 P-170512-HM/PVPI/PEG/Dyed 5 10 1200 1.3 AMS-14-2AP/PVPI/PEG/Dyed 6 10 Not 0.8 HM-181030/PVPI/PEG/Dyed/1 Tested 7 15 Not 2.1 HM-181030/PVPI/PEG/Dyed/2 Tested 8 10 Not 1.5 HG-181107/PVPI/PEG/Dyed/l Tested 9 15 Not 1.7 HG-181107/PVPI/PEG/Dyed/2 Tested 10 22.7 Not 3.0 P-181128-HM/PVPI/PEG/Dyed Tested (XIRAMS 21S) 11 15.3 Not 3.0 XIRAMS-181204/PVPI/PEG/Dyed/1 Tested (XIRAMS 21S) 12 Not Not XIRAMS-190819/PVPI/PEG/Dyed/1 Tested Tested (XIRAMS 21S) 13 Not Not XIRAMS-190819/PVPI/PEG/Dyed/2 Tested Tested (XIRAMS 21D) 14 Not 4.0 XIRAMS-181204/PVPI/PEG/Dyed/3 Tested (XIRAMS 21T)

[0066] Table 3 shows the iodine contents (iodide+titratable iodine) in some of the samples that were tested. The results obtained were all encouraging as they showed comparative contents (1200-2100 mg/kg) with a commercial product, Inadine™ (1600 mg/kg). The percentage available iodine (iodine that can be titrated with sodium thiosulphate) appeared also to meet all commercial requirements. Table 3 also illustrates that the use of 3-10% PVPI in the dyeing bath achieved the commercial target of 1% available iodine in the sample.

[0067] As detailed with reference to FIG. 6 and Table 4, the examples appeared to demonstrate a correlation between the amount of available iodine in the sample and its effectiveness against bacteria especially Staphylococcus. The effect on Klebsiella appeared less marked.

TABLE-US-00004 TABLE 4 Zone of inhibition and antimicrobial efficacy of some selected samples. % Available Iodine (after Zone of inhibition (mm) Examples Batch no. extract overnight) Staphyloccus Klebsiella HM-181024-PVP-I/PEG/1 SPUN 0.9 3 1  4 P-170512-HM-PVP-I/PEG DYED 1.2 5 1  6 AMS-14-2AP PVPI/PEG DYED 1.3 4 1 Inadine ™ 1.0 2 2 Blank—HM-180704-PVP (beginning) 0.0 0 0 Alg-181030-HM PVP-I/PEG/1 (10% PVPI) DYED 0.8 3 0  7 Alg-181030-HMPVP-I/PEG/2 (15% PVPI) DYED 1.3 4.5 1  8 HG-181107-PVP-I/PEG/1 (10% PVPI) DYED 1.5 4 1  9 HG-181107-PVP-I/PEG/2 (15% PVPI) DYED 1.7 3.5 2 HM-181116-PVP-I/PEG/1 SPUN 0.4 2 0 HM/HG-180910-PVP-I/PG-10/2 SPUN 0.7 2.5 0 HM/HG-180831-PVP-I/PG-4 SPUN 0.9 3 0 11 XIRAMS-181204—felt/PVP-I/PEG/DYED/1 3.0 6.5 2 (XIRAMS 21S—single layer) 14 XIRAMS-181204—felt/PVP-I/PEG/DYED/3 4.0 7.5 0 (21T—triple layer) P-181128-HM/PVPI/PEG/DYED (XIRAMS 21S) 3.0 7 2 HG-181204-PVP-I/PEG SPUN 0.4 3.5 1 Blank—Activeheal ™ (Ca/Na-Alginate) 0.0 0 0 #23394 AF-14-140730-HM (batch 1) 0.0 0 0 HM-180207 PVPI 1.0 0 0 HM-180212-P-PVPI 0.1 0 0 HG-180214-PVP-I 0.1 2 0 HG-180216-PVP-I 1.8 2 0

Production of Alginate-Iodine-Glycol Fibres and Felts

[0068] The potential controlling effects of the glycols (PG and PEG) on the ‘leaching-out’ of PVPI from fibres was investigated by incorporating non-complex iodine into fibres and felts through: [0069] Extrusion of dopes containing dissolved iodine crystals [0070] Dyeing fibres or non-woven with solutions containing dissolved iodine crystals.

[0071] The samples preparations were as described in example 1 for alginate-PVPI fibres except that 0.5% w/w iodine crystals (supplied by Alfa Aesar, mp 183-1860C, mol. wt (or FW253.81, density 4.930 g/cm3) were used in place of PVPI. Small amounts of PG or PEG were used to ground the iodine crystals using mortal/pestle before adding to the solution and mixing homogeneously to give very dark solutions.

[0072] Fibres produced had deep iodine colour initially, but this faded very quickly on exposure to air and even after sealing, the iodine gradually vaporised out of the fibres leaving it colourless. Addition of PG or PEG retarded evaporation but did not stop it.

Further Examples—Batchwise

[0073] Referring to FIG. 3, a non-woven felt 19 may be combined with the PVP-I (and additives) solution 31 using a pressure vessel 18. In particular, nitrogen or compressed air may be introduced into vessel 18 via inlet 17. Vessel 18 further comprises a pressure relief valve 22 and an outlet/outlet 30 connected to drain 20 that may in turn be coupled to a return pipe system (not shown). A pump 21 drives introduction of the PVP-I solution 31 from a mixing tank 25. Solution 31 may be stirred using mixer 24. Solution 31 is pumped into the pressure vessel 18 by conduits 32, 33 and into spray heads 23 for delivery onto substrate 19. Increased pressure within vessel 18 drives the solution into the fibres of the swellable material which may then be extracted from the vessel 18 and dried.

Further Examples—Continuous

[0074] Referring to FIG. 1, a non-woven felt-like substrate may be treated with the PVP-I solution according to continuous processing in which the antimicrobial containing solution is applied or delivered to the substrate in a non-batchwise manner. Referring to FIG. 1, the non-woven substrate material 19 may be rolled onto a rotatable drum 13 mounted on axle 34 and rotatably driveable by motor 15. Drum 13 comprises perforations 14. The rotating drum assembly 13, 34, 14 is mountable within an extraction chamber or system (not shown). A connection conduit 12 provides a coupling between drum 13 and a supply tank 11 housing the PVP-I (and additives) solution 31. In operation, solution 31 is supplied to drum 13 via conduit 12. The solution 31 flows from the drum interior via perforated holes 14 onto the substrate 19 that is continuously wound around the drum external surface. Pressure may be applied to the solution 31 to force it through perforations 14 to drive absorption of the PVP-I into the swellable polymer of the substrate 19.

[0075] FIG. 2 illustrates a variation of the embodiment of FIG. 1 further comprising a pump 16 to further drive solution 31 under pressure into drum 13. The extent of absorption and adsorption of the PVP-I at the fibres of the swellable material may be controlled by controlling the applied pressure 10 and/or pump 16.

Example 4—Continuous

[0076] Referring to FIG. 4, the non-woven swellable material 19 may be saturated or infused with PVP-I via a conveyer system. In particular, the non-woven substrate 19 is delivered onto a conveyor system 27 that provides lateral translation of the substrate 19 below a plurality of spray heads 29 mounted at different positions relative to the various conveyers 36. At least some of the conveyors 36 pass within a fume extraction and drying chamber 28. The PVP-I (and additives) solution 31 is sprayed onto the moving substrate 19 via spray heads 29 as a continuous process. A winding roller 37 may be positioned at a terminal end of the conveyer 36 to collect the infused substrate ready for down-stream processing i.e. cutting, stamping and the like.

Example 5—Continuous

[0077] With reference to FIG. 5, the substrate 53 in form of non-woven, tow, sliver or yarn from a processing line or reel is impregnated by means of immersion rollers 58 in PVP-I solution 55 contained in a trough 54. The PVP-I laden substrate is pulled slowly through the solution and guided over the guiding rollers 56 and passed between the pair of smooth mangle rollers 57 with variable pressure system, where the PVP-I is gently pressed into the substrate and excess solution pressed out and returned to the trough. The level of solution in the trough is monitored and kept constant by replenishment from the tank 51 by opening valve 52. The mixer 50 is used to prepare the PVP-I solution and for occasional stirring when necessary. The treated substrate 59 is then passed through a drying chamber (not shown) and dried before further processing.

[0078] With reference to FIG. 6, the substrate 53 in form of non-woven positively driven to a delivery conveyor 61 is impregnated by means of immersion conveyor 62 in PVP-I solution 55 contained in a bath 54. The PVP-I laden substrate is gently laid on the feed conveyor 64 and moved slowly through the solution and then fed between a pair of variable speed smooth mangle rollers 57 with variable pressure system 65, where the PVP-I is gently pressed into the substrate and excess solution pressed out and returned to the impregnation bath 54. The level of solution in the trough is monitored and kept constant by replenishment from the tank 51 by opening valves 52. The mixer 50 is used to prepare the PVP-I solution and for occasional stirring when necessary. The treated substrate 59 goes through a drying chamber 28 on a second feed conveyor 64 (not shown in FIG. 6 but described referring to FIGS. 4 and 8) and dried before winding onto a reel if necessary, for further processing.

[0079] With reference to FIG. 7, the substrate positively driven to the feed conveyor 61 is fed straight into the variable speed mangle rollers under variable pressure, but just before entry into the mangles, the PVP-I solution from tank 51 is fed at a constant rate using a peristaltic pump and delivered through a suitable nozzle onto the substrate. The PVP-I laden substrate gently passes between the rollers where the PVP-I solution is pressed into the substrate and excess solution if any, pressed out into a trough 54 for reuse. As before, the treated substrate is then led onto a conveyor through a drying chamber, dried and wound onto a reel for further processing. This method is simple, avoids excessive use of conveyors and PVP-I solution and avoids also, excessive loss of PVP-I solution through evaporation.

[0080] With reference to FIG. 8, the substrate positively driven from the reel is gently laid on top of conveyor 62, where it is sprayed with PVP-I solution monitored at a controlled rate from a shower-like system 29. The PVP-I laden substrate then gently passes between the mangle rollers where the PVP-I solution is pressed into the substrate and excess solution if any, pressed out into a trough 54 for reuse. As before, the treated substrate is then led onto a conveyor through a drying chamber, dried and wound onto a reel 67 for further processing.

Antimicrobial Activity Testing

[0081] From a preliminary investigation and as detailed in FIG. 6 and Table 4, selected of the above examples appeared to demonstrate a correlation between the amount of available iodine in the sample and its effectiveness against bacteria especially Staphylococcus. The effect on Klebsiella appeared less marked. The antimicrobial activity performance of various of the above examples were then tested further according to AATCC test method 100.

[0082] In particular, Staphylococcus aureus (ATCC 6538) and Pseudomonas aeruginosa (ATCC 9027) suspensions were prepared to 1.0×10.sup.6 CFUmL.sup.−1 in Tryptone Soya Broth (TSB). The inoculum was enumerated by performing 10-fold dilutions in TSB and plating out the resulting suspensions onto Tryptone Soya Agar (TSA). A 1 ml aliquot of each bacterial suspension was used to inoculate control and test dressing (dimensions 4.2×4.2 cm). Test dressings were incubated for 24 hours at 37±2° C., following which, dressings were neutralised in 10 mL neutraliser. Test dressing samples were sonicated for 5 minutes to recover microorganisms from the dressing. The resultant suspensions were serially diluted and plated onto TSA to quantify viable organisms. Negative control, positive control and sterility control samples were tested simultaneously. The negative control was the same alginate base material as the test samples but without povidone iodine treatment. The positive control was a commercial carboxymethyl cellulose dressing containing silver. Samples were tested in triplicate.

Performance Results

[0083] Staphylococcus aureus

[0084] An average of 5.61±0.27 log.sub.10CFU per sample S. aureus were recovered from the negative control at 0 hours. No viable S. aureus were recovered following treatment with examples 11 to 14 (XIRAMS 21S and 21T) tested within detection limits (minimum limit of detection was 1 log). This equated to a log reduction of 4.61-5.61±0.27 log.sub.10CFU per sample compared to the negative control.

TABLE-US-00005 TABLE 5 Antimicrobial activity results for Staphylococcus aureus Log Recovery Log Reduction (Log.sub.10CFU (Log.sub.10CFU Dressing per sample ± SD) per sample ± SD) Negative control 5.61 ± 0.27 N/A XIRAMS 21S <1.00 4.61-5.61 ± 0.27 XIRAMS 21T <1.00 4.61-5.61 ± 0.27 Positive control <1.00 4.61-5.61 ± 0.27
Pseudomonas aeruginosa

[0085] An average of 6.12±0.05 log.sub.10CFU per sample P. aeruginosa were recovered from the negative control at 0 hours. No viable P. aeruginosa were recovered following treatment with examples 11 to 14 (XIRAMS 21S and 21T) tested within detection limits (minimum limit of detection was 1 log). This equated to a log reduction of 5.12-6.12±0.05 log.sub.10CFU per sample compared to the negative control.

TABLE-US-00006 TABLE 6 Antimicrobial activity results for Pseudomonas aeruginosa Log Recovery Log Reduction (Log.sub.10CFU (Log.sub.10CFU Dressing per sample ± SD) per sample ± SD) Negative control 6.12 ± 0.05 N/A XIRAMS 21S <1.00 4.61-5.61 ± 0.27 XIRAMS 21T <1.00 4.61-5.61 ± 0.27 Positive control <1.00 4.61-5.61 ± 0.27

Testing of Biofilm Disruptions—CDC Bioreactor

[0086] The performance of various of the above examples to disrupt a biofilm was tested using a CDC bioreactor. In particular, cultures of S. aureus (NCTC 8325) and P. aeruginosa (NCIMB 10434) were used to prepare single-species bacterial inoculums (1×10.sup.7±5×10.sup.6 CFUml.sup.−1). The prepared S. aureus and P. aeruginosa bacterial suspensions were used to inoculate separate sterile CDC reactors containing polycarbonate coupons. The CDC reactors were incubated for 72 hours at 37° C.±2° C. in an orbital microbiological incubator to encourage biofilm growth. Following incubation, biofilm-containing coupons were washed in PBS to remove planktonic bacteria and were then treated with wound dressings (2×2 cm) for 24 hours. Negative and positive controls were tested concurrently. The negative control dressing was the same alginate base material as the test samples but without povidone iodine treatment. The positive control dressing was a commercial carboxymethyl cellulose dressing containing silver. Internal negative and positive control treatments were also included, these being PBS+1% TSB and a bleach-based product respectively. Samples were tested in triplicate.

[0087] Following treatment, coupons were transferred to 10 mL of neutraliser and the coupons were sonicated for 5 minutes to recover remaining attached microorganisms. Serial dilutions were carried out on the resultant recovery medium and total viable organisms were quantified.

Performance Results

[0088] Staphylococcus aureus

[0089] Averages of 5.55±0.42 log.sub.10CFUml.sup.−1 and 5.71±0.49 log.sub.10CFUml.sup.−1 viable S. aureus were recovered from the internal negative control and the negative control dressing, respectively. No viable S. aureus were recovered following treatment with examples 11 to 14 (XIRAMS 21S and 21T), internal positive control and positive control dressing. This was a reduction of 5.55 log.sub.10CFUml.sup.−1 compared to the internal negative control.

TABLE-US-00007 TABLE 7 Biofilm Disruptions (CDC Bioreactor results) for Staphylococcus aureus Average Recovery Log Reduction Test Item (Log.sub.10CFUml.sup.−1 ± SD) (Log.sub.10CFUml.sup.−1 ± SD) Internal negative control 5.55 ± 0.42 N/A Negative control 5.71 ± 0.49 N/A XIRAMS 21S 0.00 ± 0.00 5.55 XIRAMS 21T 0.00 ± 0.00 5.55 Internal positive control 0.00 ± 0.00 5.55 Positive control dressing 0.00 ± 0.00 5.55
Pseudomonas aeruginosa

[0090] Averages of 7.09±0.06 log.sub.10CFUml.sup.−1 and 6.43±0.48 log.sub.10CFUml.sup.−1 viable P. aeruginosa were recovered from the internal negative control and the negative control dressing, respectively. No viable P. aeruginosa were recovered following treatment with examples 11 to 14 (XIRAMS 21S and 21T), internal positive control and positive control dressing. This was a reduction of 7.09 log.sub.10CFUml.sup.−1 compared to the internal negative control.

TABLE-US-00008 TABLE 7 Biofilm Disruptions (CDC Bioreactor results) for Pseudomonas aeruginosa Average Recovery Log Reduction Test Item (Log.sub.10CFUml.sup.−1 ± SD) (Log.sub.10CFUml.sup.−1 ± SD) Internal negative control 7.09 ± 0.06 N/A Negative control 6.43 ± 0.48 N/A XIRAMS 21S 0.00 ± 0.00 7.09 XIRAMS 21T 0.00 ± 0.00 7.09 Internal positive control 0.00 ± 0.00 7.09 Positive control dressing 0.00 ± 0.00 7.09