US20180071419A9 - High efficiency polymeric sterilant container assembly - Google Patents
High efficiency polymeric sterilant container assembly Download PDFInfo
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- US20180071419A9 US20180071419A9 US14/074,058 US201314074058A US2018071419A9 US 20180071419 A9 US20180071419 A9 US 20180071419A9 US 201314074058 A US201314074058 A US 201314074058A US 2018071419 A9 US2018071419 A9 US 2018071419A9
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- container
- fiber
- heating
- insert
- container according
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- 239000000835 fiber Substances 0.000 claims abstract description 50
- 229920006324 polyoxymethylene Polymers 0.000 claims abstract description 33
- 229930040373 Paraformaldehyde Natural products 0.000 claims abstract description 29
- 230000001954 sterilising effect Effects 0.000 claims abstract description 24
- 238000000034 method Methods 0.000 claims abstract description 21
- 229920001577 copolymer Polymers 0.000 claims abstract description 9
- -1 polyoxymethylene Polymers 0.000 claims abstract description 9
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims description 78
- 238000010438 heat treatment Methods 0.000 claims description 32
- 239000000155 melt Substances 0.000 claims description 17
- 239000000463 material Substances 0.000 claims description 14
- 238000003776 cleavage reaction Methods 0.000 claims description 9
- 230000007017 scission Effects 0.000 claims description 9
- 230000005855 radiation Effects 0.000 claims description 4
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 claims description 2
- 229920012196 Polyoxymethylene Copolymer Polymers 0.000 claims description 2
- 238000007664 blowing Methods 0.000 claims description 2
- 238000013268 sustained release Methods 0.000 claims 1
- 239000012730 sustained-release form Substances 0.000 claims 1
- 238000004659 sterilization and disinfection Methods 0.000 description 13
- 229920000642 polymer Polymers 0.000 description 8
- 238000012360 testing method Methods 0.000 description 8
- 239000004033 plastic Substances 0.000 description 6
- 229920003023 plastic Polymers 0.000 description 6
- 238000005452 bending Methods 0.000 description 4
- 230000036512 infertility Effects 0.000 description 4
- 230000006870 function Effects 0.000 description 3
- 229940127554 medical product Drugs 0.000 description 3
- 239000013641 positive control Substances 0.000 description 3
- 241000193385 Geobacillus stearothermophilus Species 0.000 description 2
- 229930182556 Polyacetal Natural products 0.000 description 2
- 230000000845 anti-microbial effect Effects 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000011888 foil Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000013642 negative control Substances 0.000 description 2
- 241000193830 Bacillus <bacterium> Species 0.000 description 1
- GUTLYIVDDKVIGB-OUBTZVSYSA-N Cobalt-60 Chemical compound [60Co] GUTLYIVDDKVIGB-OUBTZVSYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000000090 biomarker Substances 0.000 description 1
- 239000007853 buffer solution Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000001066 destructive effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000010128 melt processing Methods 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 125000005704 oxymethylene group Chemical group [H]C([H])([*:2])O[*:1] 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 229920006298 saran Polymers 0.000 description 1
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- 239000000243 solution Substances 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000002459 sustained effect Effects 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
Images
Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
- A61L2/16—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using chemical substances
- A61L2/20—Gaseous substances, e.g. vapours
- A61L2/204—Formaldehyde
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
- A61L2/02—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using physical phenomena
- A61L2/08—Radiation
- A61L2/081—Gamma radiation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65B—MACHINES, APPARATUS OR DEVICES FOR, OR METHODS OF, PACKAGING ARTICLES OR MATERIALS; UNPACKING
- B65B55/00—Preserving, protecting or purifying packages or package contents in association with packaging
- B65B55/02—Sterilising, e.g. of complete packages
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D33/00—Details of, or accessories for, sacks or bags
- B65D33/16—End- or aperture-closing arrangements or devices
- B65D33/25—Riveting; Dovetailing; Screwing; using press buttons or slide fasteners
- B65D33/2508—Riveting; Dovetailing; Screwing; using press buttons or slide fasteners using slide fasteners with interlocking members having a substantially uniform section throughout the length of the fastener; Sliders therefor
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2202/00—Aspects relating to methods or apparatus for disinfecting or sterilising materials or objects
- A61L2202/10—Apparatus features
- A61L2202/18—Aseptic storing means
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2202/00—Aspects relating to methods or apparatus for disinfecting or sterilising materials or objects
- A61L2202/10—Apparatus features
- A61L2202/18—Aseptic storing means
- A61L2202/181—Flexible packaging means, e.g. permeable membranes, paper
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2202/00—Aspects relating to methods or apparatus for disinfecting or sterilising materials or objects
- A61L2202/20—Targets to be treated
- A61L2202/24—Medical instruments, e.g. endoscopes, catheters, sharps
Definitions
- the present invention relates to sterilized packages and containers.
- the present invention relates to sterilized packaging containing a highly efficient formaldehyde releasing composition.
- gaseous sterilization is very effective, the handling and long periods of time needed to diffuse and remove the sterilant gas from the chamber containing large pallets of heavy cardboard boxes/packages is a problem. Because of the long contact times and purge cycles required for gaseous sterilization, most gaseous sterilizations take place mainly in industrial settings where the requirement for expensive equipment is more cost effective and careful control can take place during the sterilization cycle by someone experienced in the sterilization process. Also, high energy irradiation methods require expensive radiation facilities and certified personnel skilled in the use of radiation isotopes for the purpose of sterilization of medical products. Plastic components of medical products are often embrittled or damaged by the destructive nature of the irradiation process.
- thermoplastic polyoxymethylenes were only commercially available as extremely viscous melts (low melt flow rates between 0.3 to 5.0 g/10 min as determined by ASTM D1238E) that limited the thermoformability into simple geometries, such as films, slabs, and rods, which required prolonged crystallization times that caused even further embrittlement and degradation of the material.
- Relatively thin fibers are impossible to form with these low melt flow rate polymers since spin blown fibers require higher melt flows. Severe plastic embrittlement caused by the combination of thicker part limitations and higher irradiation doses required to achieve sufficient gas release resulted in the prior art never being adopted commercially.
- the present invention relates to the discovery that if a low melt viscosity and melt formable (such as by melt blowing) polyoxymethylene or copolymer of polyoxymethylene is formed into a relatively thin fiber with a sufficient high surface to mass ratio and irradiated, it can be included in a package for purposes of sterilization of the contents of the container by low heat release of formaldehyde without becoming too brittle yet still releasing sufficient formaldehyde to sterilize the article.
- the thin fiber is achieved by utilizing a polyoxymethylene or a co-polymer thereby having a melt flow rate of between about 20-1200 g/10 minutes at 230° C. as determined by ASTM D1238E.
- one embodiment of the present invention relates to a container of a selected volume on the inside, suitable for low heat sterilizing a selected article positioned in the inside of the container comprising a container insert on the inside of the container comprising a fiber of a diameter 0.5mm or less of polyoxymethylene or co-polymer of polyoxymethylene having a melt flow rate of between about 20-1200 g/10 minutes at 230° C. that has been irradiated sufficient to cause chain cleavage without depolymerization or brittleness of the insert such that formaldehyde is released upon subsequent application of low heat to the insert by any manner.
- a process for producing a container of a selected volume on the inside suitable for low heat sterilizing a selected article positioned on the inside of the container comprising positioning in the inside of the container, a fiber having a diameter of 0.5 mm or less comprising a polyoxymethylene or co-polymer having a melt flow rate of between about 20-1200 g/10 minutes at 230° C. and has been irradiated sufficient to cause chain cleavage without depolymerization or brittleness such that formaldehyde is released upon subsequent application of low heat to the insert.
- FIG. 1 is a medical device in a container with the polymer insert of the present invention.
- the terms “a” or “an”, as used herein, are defined as one or as more than one.
- the term “plurality”, as used herein, is defined as two or as more than two.
- the term “another”, as used herein, is defined as at least a second or more.
- the terms “including” and/or “having”, as used herein, are defined as comprising (i.e., open language).
- the term “coupled”, as used herein, is defined as connected, although not necessarily directly, and not necessarily mechanically.
- Melt Flow Rate is defined as the amount of polymer flowing through a hole in g/10 minutes at 230° C. as determined by ASTM D1238E, incorporated herein by reference.
- the term “container” refers to any package, bag, or the like in which a desired item for sterilization can be enclosed and sealed and having a selected volume on the inside.
- the container must be capable of withstanding the low heat of the present invention and be essentially impermeable to formaldehyde to prevent its leakage during the sterilization process.
- the humidity on the inside of the container is about 5-100 percent relative humidity.
- the containers are plastic bags made of polyethylene, polypropylene, Saran, aluminum foil or foil coated plastic, and the like. In one embodiment, they are essentially flat bags of the shape and style of food sandwich bags with an appropriate closure (sandwich zip lock).
- the flat bags will have a selected length and width with an area defined by the product of the length times the width.
- the bags can be sealed, for example, by an adhesive seal, zipper lock seal, or other methods for sealing the bag.
- the article is placed in the bag and the bag heat sealed shut, thus making the bag a one-time disposable bag since the bag must be torn, cut open, or the like to obtain the enclosed sterilized item.
- a combination of zip lock and heat seals are used as tamper-proof seal configurations.
- a chevron seal is provided at the opposite end of the bag to maintain sterility when opening in a sterile field, such as an operating room.
- the container of the present invention can be any size necessary to contain the item to be sterilized. Accordingly, most any size container can be utilized, but for efficiency sake, the bag would be the minimum size that the article to be sterilized would fit inside the closed portion of the container. For example, a flat, polymeric bag for sterilizing a scalpel would only need to be 4 or 5 inches long and 3 or 4 inches wide while surgical instruments might need to be several feet long.
- low heat refers to the ability to apply heat to the insert in the range of about 20° C. to about 90° C.
- the heat can be applied by any convenient means, such as a gas or electric oven, electric heating wires, heat lamp, chemical reaction, sunlight, or the like.
- the container could be heated in order to heat the insert in one embodiment.
- Other embodiments of heating include heating the insert prior to placement in the container incorporating a heating device (e.g. heating wires) inside the insert, internal, or external heating packs (wire heaters or hand warmers).
- the insert can be accessed through the container (e.g. a tube that extends through the container wall that can contain a heating element). The exact heat will vary but will depend on the size of the article and the time at the particular heat.
- the time period of heating is from about 5 minutes to 600 minutes and in another embodiment it is about an hour.
- the heating could be at room temperature and could be sustained over an extended period of time (days to weeks).
- the “selected article” as used herein, is the article that one wishes to sterilize. Since the maximum heat is in the ranges noted above, the article can be made of plastic or other materials that normally would not handle higher heats. Once again, if an article would not survive say, 90° C., the article can be heated at a lower temperature for a longer time and achieve the same result of sterilization though a longer time would be necessary.
- a “polyoxymethylene (POM)” or “co-polymer of polyoxymethylene” are any polymers which can be melt blown or otherwise melt formable into thin fibers.
- the fibers will have a diameter of less than about 0.5 mm and in one embodiment less than about 0.1 mm diameter.
- the POM polymeric materials of the present invention have a very high melt flow rate and consequently are very fluid in the molten state, unlike historical POM's that were extremely viscous in the melt.
- the high melt flow rate POM's as defined herein are necessary in order to form the high surface area thin fibers without severe thermal degradation of the POM as found historically with low melt flow rate POM's.
- High melt flow rate polymers are generally used in industry for forming high surface area fibers or melt processing and forming into non-woven fabric or mat type articles.
- Thermal flow rate of the present invention is tested by ASTM D1238E.
- the polymer, in order to be spun into fibers of the desired diameter have a melt flow rate of 20-1200 g/10 minutes at 230° C. and another embodiment at about 40-1200 g/10 minutes at 230° C. and 20-500 g/10 minutes at 230° C.
- the radiation dosage to accomplish the proper chain cleavage without depolymerization or brittleness, such that formaldehyde is released upon subsequent heating of the insert is from about 1 to about 200 kGy. In one embodiment the insert is irradiated from about 35 to about 70 kGy.
- a “fiber” is a piece of high melt flow POM melt formed copolymer that has been irradiated sufficiently to cause chain cleavage without depolymerization or brittleness, but sufficiently that formaldehyde is released upon the subsequent low heat sterilizing of the insert for a select period of time.
- Fiber (with a high surface area) can be formed into a non-woven mat.
- the fiber needs to be of a sufficient weight and surface area that upon low heat application the container the insert will release sufficient formaldehyde to reach a concentration of at least 0.1 mg/L in the container volume inside. In one embodiment it is of at least 0.3 mg/L formaldehyde. This can be determined by one skilled in the art.
- the fiber can be a loose piece inside the container, or in other embodiments, it can be attached to or part of the inside surface of the container, for example, by layering the POM co-polymer fiber on the inside of the container especially where the container is a polymeric bag.
- the POM co-polymer can be mixed with other polymers or substances to create a multi-component insert for particular additional purposes.
- a thermochromic material is added to the POM co-polymer so that when it is heated it will change color at the end of the sterilization heating. The fiber is placed in the container prior to the heating or at the time of heating, as necessary or desired.
- the process of sterilizing an article at low heat in a container comprises placing the irradiated fiber and article to be sterilized (in any order) inside the container.
- the insert is heated to a temperature of about 25° C. to about 90° C. for a time sufficient to release formaldehyde from the container insert and sterilize the article either before placing in the container or afterwards.
- the container is sealed after fiber placement therein.
- the package can then be opened and if resealable, reused.
- the article is then sterilized and ready for the desired sterilized use.
- FIG. 1 is an embodiment of the present invention.
- a container 11 suitable for low heat sterilizing.
- a high surface area fiber 12 Inside container 11 is a high surface area fiber 12 .
- a surgical tool 13 In this embodiment the container 11 is a zip lock 14 closable container made from a clear polyester material.
- a 10 mil thick sample of POM dense film and an equivalent weight of fiber melt blown POM of the present invention were gamma irradiated to a nominal dose of 70 kGy followed by heating both samples at 70° C. for a period of 60 minutes in a convection oven.
- the thick film yielded a 0.18% formaldehyde release while the melt blown sample of the present invention yielded a 2.12% release of formaldehyde which is over a ten-fold increase compared to the thick film.
- the same level of sterility could be achieved with one-tenth the weight of melt blown material compared to thick film.
- a 10 mil thick sample of POM film and an equivalent weight fiber of melt blown POM of the present invention were both gamma irradiated to a nominal dose of 30 kGy followed by heating both samples at 70° C. for a period of 60 minutes in a convection oven.
- the film yielded 0.6 mg of formaldehyde while the melt blown sample of the present invention yielded 3.1 mg of formaldehyde or over five-fold more sterilant for equal sample comparison.
- the same level of sterility could be achieved with one-fifth the weight of melt blown material compared to thick film.
- melt blown samples of high melt flow rate POM (Melt Flow Rate of 40 g/10 minutes at 230° C. as determined by ASTM D1238E) were prepared on a melt-blown processing line at the University of Tennessee with average weights per square meter (GSM) of 100, 150, and 200 GSM. Fibers were formed into a mat configuration. All melt blown mats had average fiber diameters of 10 microns. Stock rolls of the melt blown mats were irradiated to 20, 35, and 50 kGy in a cobalt-60 gamma facility.
- POM Melt Flow Rate of 40 g/10 minutes at 230° C. as determined by ASTM D1238E
- Bag Volume Bag Size 35kGy mg of insert mg insert at 70kGy 4′′ ⁇ 6′′ 200 20 5 6′′ ⁇ 9′′ 700 70 17.5 7′′ ⁇ 12′′ 1600 160 40
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- Health & Medical Sciences (AREA)
- Animal Behavior & Ethology (AREA)
- Epidemiology (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Chemical & Material Sciences (AREA)
- Apparatus For Disinfection Or Sterilisation (AREA)
Abstract
Description
- This application is a continuation-in-part of U.S. non-provisional application Ser. No. 13/372,883 filed on Feb. 14, 2012 which is a continuation-in-part of U.S. non-provisional application Ser. No. 12/881,273 filed on Sep. 14, 2010 which claims priority to provisional application No. 61/276,944 filed on Sep. 18, 2009. All applications are incorporated herein in their entirety by reference.
- A portion of the disclosure of this patent contains material that is subject to copyright protection. The copyright owner has no objection to the reproduction by anyone of the patent document or the patent disclosure as it appears in the Patent and Trademark Office patent files or records, but otherwise reserves all copyright rights whatsoever.
- 1. Field of the Invention
- The present invention relates to sterilized packages and containers. In particular, the present invention relates to sterilized packaging containing a highly efficient formaldehyde releasing composition.
- 2. Description of Related Art
- There is a wide array of medical devices that must be sterilized prior to their use. In the medical field it is common to have articles that can be re-sterilized or disposable articles that are only used one time but are provided to the user already sterilized. The art uses a wide variety of methods to sterilize or re-sterilize medical articles including, ethylene oxide, formaldehyde, low temperature steam-formaldehyde, gamma/e-beam irradiation, steam autoclave, dry heat, and the like.
- While gaseous sterilization is very effective, the handling and long periods of time needed to diffuse and remove the sterilant gas from the chamber containing large pallets of heavy cardboard boxes/packages is a problem. Because of the long contact times and purge cycles required for gaseous sterilization, most gaseous sterilizations take place mainly in industrial settings where the requirement for expensive equipment is more cost effective and careful control can take place during the sterilization cycle by someone experienced in the sterilization process. Also, high energy irradiation methods require expensive radiation facilities and certified personnel skilled in the use of radiation isotopes for the purpose of sterilization of medical products. Plastic components of medical products are often embrittled or damaged by the destructive nature of the irradiation process. In the non-industrial setting, such as a hospital or physician's office, historically one of the most widely used methods for sterilization is the use of high temperature steam autoclaves. Unfortunately, the temperature of an autoclave is not conducive for use with many of today's plastics or other heat sensitive medical products which are commonplace in the medical environment of today. Accordingly, many medical offices throw away reusable medical devices because there are currently no techniques that are suitable for the non-industrial setting that are both cost effective and easy to use in small medical facilities.
- Some twenty-five years ago an attempt to solve the problem was made in U.S. Pat. No. 4,050,576 to Williams et al. In that patent a sterilant package included a relatively thick piece of poly acetal (which contains oxymethylene groups and stabilizing groups) which had been irradiated to effect chain cleavage of the polymer without depolymerization. The package, upon subsequent heating, caused the poly acetal to slightly depolymerize which caused a release of trace amounts of formaldehyde gas. Unfortunately, the irradiation doses required to achieve sufficient gas release for sterilization using this method were so high that the insert became very brittle and difficult to manage as indicated by low film breaking angles in embrittlement tests.
- During the prior art timeframe, thermoplastic polyoxymethylenes were only commercially available as extremely viscous melts (low melt flow rates between 0.3 to 5.0 g/10 min as determined by ASTM D1238E) that limited the thermoformability into simple geometries, such as films, slabs, and rods, which required prolonged crystallization times that caused even further embrittlement and degradation of the material. Relatively thin fibers are impossible to form with these low melt flow rate polymers since spin blown fibers require higher melt flows. Severe plastic embrittlement caused by the combination of thicker part limitations and higher irradiation doses required to achieve sufficient gas release resulted in the prior art never being adopted commercially.
- The present invention relates to the discovery that if a low melt viscosity and melt formable (such as by melt blowing) polyoxymethylene or copolymer of polyoxymethylene is formed into a relatively thin fiber with a sufficient high surface to mass ratio and irradiated, it can be included in a package for purposes of sterilization of the contents of the container by low heat release of formaldehyde without becoming too brittle yet still releasing sufficient formaldehyde to sterilize the article. The thin fiber is achieved by utilizing a polyoxymethylene or a co-polymer thereby having a melt flow rate of between about 20-1200 g/10 minutes at 230° C. as determined by ASTM D1238E.
- Accordingly, one embodiment of the present invention relates to a container of a selected volume on the inside, suitable for low heat sterilizing a selected article positioned in the inside of the container comprising a container insert on the inside of the container comprising a fiber of a diameter 0.5mm or less of polyoxymethylene or co-polymer of polyoxymethylene having a melt flow rate of between about 20-1200 g/10 minutes at 230° C. that has been irradiated sufficient to cause chain cleavage without depolymerization or brittleness of the insert such that formaldehyde is released upon subsequent application of low heat to the insert by any manner.
- In yet another embodiment of the present invention, there is a process for producing a container of a selected volume on the inside suitable for low heat sterilizing a selected article positioned on the inside of the container comprising positioning in the inside of the container, a fiber having a diameter of 0.5 mm or less comprising a polyoxymethylene or co-polymer having a melt flow rate of between about 20-1200 g/10 minutes at 230° C. and has been irradiated sufficient to cause chain cleavage without depolymerization or brittleness such that formaldehyde is released upon subsequent application of low heat to the insert.
- In yet another embodiment of the present invention there is a method of sterilizing an article at low heat in a container of a selected volume on the inside comprising:
-
- a) positioning the article in the container;
- b) positioning a fiber in the container which comprises a fiber of a diameter of 0.5 mm or less of polyoxymethylene or polyoxymethylene co-polymer having a melt flow rate of between about 20-1200 g/10 minutes at 230° C. that has been irradiated sufficient to cause chain cleavage without depolymerization or brittleness such that formaldehyde is released upon subsequent heating of the insert; and
- c) heating the fiber to a temperature of about 20° C. to about 90° C. for a time sufficient to release formaldehyde and sterilize the article.
-
FIG. 1 is a medical device in a container with the polymer insert of the present invention. - While this invention is susceptible to embodiment in many different forms, there is shown in the drawings and will herein be described in detail specific embodiments, with the understanding that the present disclosure of such embodiments is to be considered as an example of the principles and not intended to limit the invention to the specific embodiments shown and described. In the description below, like reference numerals are used to describe the same, similar or corresponding parts in the several views of the drawings. This detailed description defines the meaning of the terms used herein and specifically describes embodiments in order for those skilled in the art to practice the invention.
- The terms “a” or “an”, as used herein, are defined as one or as more than one. The term “plurality”, as used herein, is defined as two or as more than two. The term “another”, as used herein, is defined as at least a second or more. The terms “including” and/or “having”, as used herein, are defined as comprising (i.e., open language). The term “coupled”, as used herein, is defined as connected, although not necessarily directly, and not necessarily mechanically.
- The terms “about” and “essentially” mean ±10 percent.
- Reference throughout this document to “one embodiment”, “certain embodiments”, and “an embodiment” or similar terms means that a particular feature, structure, or characteristic described in connection with the embodiment is included in at least one embodiment of the present invention. Thus, the appearances of such phrases or in various places throughout this specification are not necessarily all referring to the same embodiment. Furthermore, the particular features, structures, or characteristics may be combined in any suitable manner in one or more embodiments without limitation.
- The term “or” as used herein is to be interpreted as an inclusive or meaning any one or any combination. Therefore, “A, B or C” means any of the following: “A; B; C; A and B; A and C; B and C; A, B and C”. An exception to this definition will occur only when a combination of elements, functions, steps or acts are in some way inherently mutually exclusive.
- The drawings featured in the figures are for the purpose of illustrating certain convenient embodiments of the present invention, and are not to be considered as limitation thereto. Term “means” preceding a present participle of an operation indicates a desired function for which there is one or more embodiments, i.e., one or more methods, devices, or apparatuses for achieving the desired function and that one skilled in the art could select from these or their equivalent in view of the disclosure herein and use of the term “means” is not intended to be limiting.
- The term Melt Flow Rate, as used herein, is defined as the amount of polymer flowing through a hole in g/10 minutes at 230° C. as determined by ASTM D1238E, incorporated herein by reference.
- As used herein, the term “container” refers to any package, bag, or the like in which a desired item for sterilization can be enclosed and sealed and having a selected volume on the inside. The container must be capable of withstanding the low heat of the present invention and be essentially impermeable to formaldehyde to prevent its leakage during the sterilization process. In one embodiment the humidity on the inside of the container is about 5-100 percent relative humidity. In one embodiment, the containers are plastic bags made of polyethylene, polypropylene, Saran, aluminum foil or foil coated plastic, and the like. In one embodiment, they are essentially flat bags of the shape and style of food sandwich bags with an appropriate closure (sandwich zip lock). The flat bags will have a selected length and width with an area defined by the product of the length times the width. The bags can be sealed, for example, by an adhesive seal, zipper lock seal, or other methods for sealing the bag. In another embodiment, the article is placed in the bag and the bag heat sealed shut, thus making the bag a one-time disposable bag since the bag must be torn, cut open, or the like to obtain the enclosed sterilized item. In still another embodiment, a combination of zip lock and heat seals are used as tamper-proof seal configurations. In still another embodiment, a chevron seal is provided at the opposite end of the bag to maintain sterility when opening in a sterile field, such as an operating room. The container of the present invention can be any size necessary to contain the item to be sterilized. Accordingly, most any size container can be utilized, but for efficiency sake, the bag would be the minimum size that the article to be sterilized would fit inside the closed portion of the container. For example, a flat, polymeric bag for sterilizing a scalpel would only need to be 4 or 5 inches long and 3 or 4 inches wide while surgical instruments might need to be several feet long.
- As used herein “low heat” refers to the ability to apply heat to the insert in the range of about 20° C. to about 90° C. The heat can be applied by any convenient means, such as a gas or electric oven, electric heating wires, heat lamp, chemical reaction, sunlight, or the like. The container could be heated in order to heat the insert in one embodiment. Other embodiments of heating include heating the insert prior to placement in the container incorporating a heating device (e.g. heating wires) inside the insert, internal, or external heating packs (wire heaters or hand warmers). In another embodiment, the insert can be accessed through the container (e.g. a tube that extends through the container wall that can contain a heating element). The exact heat will vary but will depend on the size of the article and the time at the particular heat. In view of the present disclosure, one could easily match the exact heat temperature and time to obtain a sufficient time for heating to release formaldehyde. In one embodiment, the time period of heating is from about 5 minutes to 600 minutes and in another embodiment it is about an hour. In one embodiment the heating could be at room temperature and could be sustained over an extended period of time (days to weeks).
- The “selected article” as used herein, is the article that one wishes to sterilize. Since the maximum heat is in the ranges noted above, the article can be made of plastic or other materials that normally would not handle higher heats. Once again, if an article would not survive say, 90° C., the article can be heated at a lower temperature for a longer time and achieve the same result of sterilization though a longer time would be necessary.
- As used herein, a “polyoxymethylene (POM)” or “co-polymer of polyoxymethylene” are any polymers which can be melt blown or otherwise melt formable into thin fibers. The fibers will have a diameter of less than about 0.5 mm and in one embodiment less than about 0.1 mm diameter. The POM polymeric materials of the present invention have a very high melt flow rate and consequently are very fluid in the molten state, unlike historical POM's that were extremely viscous in the melt. The high melt flow rate POM's as defined herein are necessary in order to form the high surface area thin fibers without severe thermal degradation of the POM as found historically with low melt flow rate POM's. High melt flow rate polymers are generally used in industry for forming high surface area fibers or melt processing and forming into non-woven fabric or mat type articles. Thermal flow rate of the present invention is tested by ASTM D1238E. The polymer, in order to be spun into fibers of the desired diameter have a melt flow rate of 20-1200 g/10 minutes at 230° C. and another embodiment at about 40-1200 g/10 minutes at 230° C. and 20-500 g/10 minutes at 230° C. Generally, the radiation dosage to accomplish the proper chain cleavage without depolymerization or brittleness, such that formaldehyde is released upon subsequent heating of the insert, is from about 1 to about 200 kGy. In one embodiment the insert is irradiated from about 35 to about 70 kGy.
- As used herein a “fiber” is a piece of high melt flow POM melt formed copolymer that has been irradiated sufficiently to cause chain cleavage without depolymerization or brittleness, but sufficiently that formaldehyde is released upon the subsequent low heat sterilizing of the insert for a select period of time. Fiber (with a high surface area) can be formed into a non-woven mat. The fiber needs to be of a sufficient weight and surface area that upon low heat application the container the insert will release sufficient formaldehyde to reach a concentration of at least 0.1 mg/L in the container volume inside. In one embodiment it is of at least 0.3 mg/L formaldehyde. This can be determined by one skilled in the art. The fiber can be a loose piece inside the container, or in other embodiments, it can be attached to or part of the inside surface of the container, for example, by layering the POM co-polymer fiber on the inside of the container especially where the container is a polymeric bag. In some embodiments, the POM co-polymer can be mixed with other polymers or substances to create a multi-component insert for particular additional purposes. In one embodiment, a thermochromic material is added to the POM co-polymer so that when it is heated it will change color at the end of the sterilization heating. The fiber is placed in the container prior to the heating or at the time of heating, as necessary or desired.
- In general, the process of sterilizing an article at low heat in a container comprises placing the irradiated fiber and article to be sterilized (in any order) inside the container. The insert is heated to a temperature of about 25° C. to about 90° C. for a time sufficient to release formaldehyde from the container insert and sterilize the article either before placing in the container or afterwards. The container is sealed after fiber placement therein. The package can then be opened and if resealable, reused. The article is then sterilized and ready for the desired sterilized use.
- Now referring to the drawing.
FIG. 1 is an embodiment of the present invention. There is shown acontainer 11 suitable for low heat sterilizing. Insidecontainer 11 is a highsurface area fiber 12. Also, incontainer 11 is an article to be sterilized, asurgical tool 13. In this embodiment thecontainer 11 is azip lock 14 closable container made from a clear polyester material. - A 10 mil thick sample of POM dense film and an equivalent weight of fiber melt blown POM of the present invention were gamma irradiated to a nominal dose of 70 kGy followed by heating both samples at 70° C. for a period of 60 minutes in a convection oven. The thick film yielded a 0.18% formaldehyde release while the melt blown sample of the present invention yielded a 2.12% release of formaldehyde which is over a ten-fold increase compared to the thick film. In separate experiments, the same level of sterility could be achieved with one-tenth the weight of melt blown material compared to thick film.
- Comparative embrittlement bending tests indicated that the thick film failed at a 21 degree bending angle while the melt blown sample could undergo a full 180 degree bend without failure.
- A 10 mil thick sample of POM film and an equivalent weight fiber of melt blown POM of the present invention were both gamma irradiated to a nominal dose of 30 kGy followed by heating both samples at 70° C. for a period of 60 minutes in a convection oven. The film yielded 0.6 mg of formaldehyde while the melt blown sample of the present invention yielded 3.1 mg of formaldehyde or over five-fold more sterilant for equal sample comparison. In separate experiments, the same level of sterility could be achieved with one-fifth the weight of melt blown material compared to thick film.
- Comparative embrittlement bending tests indicated that the thick film failed at a 20 degree bending angle while the melt blown sample could undergo a full 180 degree bend without failure.
- Three melt blown samples of high melt flow rate POM (Melt Flow Rate of 40 g/10 minutes at 230° C. as determined by ASTM D1238E) were prepared on a melt-blown processing line at the University of Tennessee with average weights per square meter (GSM) of 100, 150, and 200 GSM. Fibers were formed into a mat configuration. All melt blown mats had average fiber diameters of 10 microns. Stock rolls of the melt blown mats were irradiated to 20, 35, and 50 kGy in a cobalt-60 gamma facility. Following irradiation, 4″×6″ samples of each weight melt blown mat were placed into separate 5″×8″ zip-lock bags along with a strip of a biological indicator inoculated with either 105 Geobacillus Stearothermophilus or 106 Bacillus Atrophoeous. All samples after heating to 70° C. for 15 minutes were found to be sterile as shown below:
-
Example GSM Dose (kGy) G. Stearothermophilus B. Atrophoeous 3 100 20 Sterile Sterile 4 100 35 Sterile Sterile 5 100 50 Sterile Sterile 6 150 20 Sterile Sterile 7 150 35 Sterile Sterile 8 150 50 Sterile Sterile 9 200 20 Sterile Sterile 10 200 35 Sterile Sterile 11 200 50 Sterile Sterile
Even the lowest weight 100 GSM mat yielded sufficient sterilant to render the contents of the bag sterile even at the lowest dose of 20 kGy. -
TABLE 1 Antimicrobial effectiveness of the test material with indirect contact with microbial contamination. Test Sample S. aureus P. aeruginosa 1) Inoculated lens on antimicrobial material S S 2) Inoculated lens on material with S S multipurpose lens solution 3) Inoculated lens on material with sterile S S buffer solution 4) Negative control 1 S S 5) Negative control 2 S S 6) Positive control 1 NS NS 7) Positive control 2 NS NS Sterility Test Results: S = sterile, NS = non-sterile with positive growth of the test organism
All test samples (1-5) were sterile in 24 hours or less with the exception of the positive controls (6-7). - The following bags were heated for 60 minutes at 70° C. where the insert was irradiated at 35 kGy-70 KGy.
-
Bag Volume Bag Size (mL) 35kGy mg of insert mg insert at 70kGy 4″ × 6″ 200 20 5 6″ × 9″ 700 70 17.5 7″ × 12″ 1600 160 40 - Those skilled in the art to which the present invention pertains may make modifications resulting in other embodiments employing principles of the present invention without departing from its spirit or characteristics, particularly upon considering the foregoing teachings. Accordingly, the described embodiments are to be considered in all respects only as illustrative, and not restrictive, and the scope of the present invention is, therefore, indicated by the appended claims rather than by the foregoing description or drawings. Consequently, while the present invention has been described with reference to particular embodiments, modifications of structure, sequence, materials and the like apparent to those skilled in the art still fall within the scope of the invention as claimed by the applicant.
Claims (21)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US14/074,058 US10092667B2 (en) | 2009-09-18 | 2013-11-07 | High efficiency polymeric sterilant container assembly |
Applications Claiming Priority (4)
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|---|---|---|---|
| US27694409P | 2009-09-18 | 2009-09-18 | |
| US12/881,273 US20110070125A1 (en) | 2009-09-18 | 2010-09-14 | High efficiency polymeric sterilant container assembly |
| US13/372,883 US20120141324A1 (en) | 2009-09-18 | 2012-02-14 | High efficiency polymeric sterilant container assembly |
| US14/074,058 US10092667B2 (en) | 2009-09-18 | 2013-11-07 | High efficiency polymeric sterilant container assembly |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US13/372,883 Continuation-In-Part US20120141324A1 (en) | 2009-09-18 | 2012-02-14 | High efficiency polymeric sterilant container assembly |
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| US20140056761A1 US20140056761A1 (en) | 2014-02-27 |
| US20180071419A9 true US20180071419A9 (en) | 2018-03-15 |
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| US13/372,883 Abandoned US20120141324A1 (en) | 2009-09-18 | 2012-02-14 | High efficiency polymeric sterilant container assembly |
| US14/074,058 Active 2032-02-14 US10092667B2 (en) | 2009-09-18 | 2013-11-07 | High efficiency polymeric sterilant container assembly |
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| US13/372,883 Abandoned US20120141324A1 (en) | 2009-09-18 | 2012-02-14 | High efficiency polymeric sterilant container assembly |
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| US20110070125A1 (en) * | 2009-09-18 | 2011-03-24 | Brighton Development, LLC | High efficiency polymeric sterilant container assembly |
| EP3511461B1 (en) * | 2018-01-11 | 2021-10-13 | Carl Freudenberg KG | Nonwoven sterile packaging |
Family Cites Families (13)
| Publication number | Priority date | Publication date | Assignee | Title |
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| US3027352A (en) * | 1958-02-28 | 1962-03-27 | Celanese Corp | Copolymers |
| US3658749A (en) * | 1970-06-16 | 1972-04-25 | Celanese Corp | Modified oxymethylene polymers |
| US4050576A (en) * | 1976-08-17 | 1977-09-27 | Becton, Dickinson And Company | Polymeric sterilant assembly |
| JP3299966B2 (en) * | 1991-12-23 | 2002-07-08 | ヘキスト・セラニーズ・コーポレーション | High-molecular acetal resistant to mineral deposition |
| US5476616A (en) * | 1994-12-12 | 1995-12-19 | Schwarz; Eckhard C. A. | Apparatus and process for uniformly melt-blowing a fiberforming thermoplastic polymer in a spinnerette assembly of multiple rows of spinning orifices |
| US5594955A (en) * | 1994-12-12 | 1997-01-21 | Kimberly-Clark Corporation | Surgical gown sleeve |
| US5994455A (en) * | 1998-09-08 | 1999-11-30 | Ticonna Gmbh | Process for the preparation of thermally stable polyoxymethylene copolymers |
| US6706218B2 (en) * | 2000-01-11 | 2004-03-16 | The Board Of Governors For Higher Education, State Of Rhode Island And Providence Plantations | Thermochromic polymers for rapid visual assessment of temperature |
| JP4907023B2 (en) * | 2001-09-18 | 2012-03-28 | ポリプラスチックス株式会社 | Method for producing polyoxymethylene fiber |
| DE10251332B4 (en) | 2002-11-05 | 2006-07-27 | Ticona Gmbh | Polyoxymethylene copolymers, their preparation and use |
| US20050288438A1 (en) | 2004-06-25 | 2005-12-29 | Malay Nandi | Stabilized polyoxymethylene compositions with low melt viscosity |
| US7410696B2 (en) * | 2005-01-12 | 2008-08-12 | Ticona Gmbh | Polyoxymethylene fibers, production thereof and use thereof |
| US20110070125A1 (en) * | 2009-09-18 | 2011-03-24 | Brighton Development, LLC | High efficiency polymeric sterilant container assembly |
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2010
- 2010-09-14 US US12/881,273 patent/US20110070125A1/en not_active Abandoned
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2012
- 2012-02-14 US US13/372,883 patent/US20120141324A1/en not_active Abandoned
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| US20110070125A1 (en) | 2011-03-24 |
| US10092667B2 (en) | 2018-10-09 |
| US20120141324A1 (en) | 2012-06-07 |
| US20140056761A1 (en) | 2014-02-27 |
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