Active agents, such as antimicrobial agents, have been used in conjunction with many products. In particular, since viral outbreaks such as SARS, bird flu and norovirus have been widely publicized, consumers have an increased interest in a wide array of products having an antimicrobial agent applied thereto; products such as wipes, shoe inserts, athletic clothing, personal care products, hospital equipment, sports equipment, etc. Products such as absorbent articles meant for bodily fluids (e.g. disposable diapers, pads and incontinence garments) may offer an odor-control benefit when an antimicrobial agent is applied thereto.
Currently, the application of an antimicrobial agent onto a select portion of an absorbent personal-care article is achieved by applying it as a lotion, cream, or spray formulation. However, due to the application method, and/or the incompatibility and/or poor solubility of the antimicrobial agent(s) in the formulation, getting effective concentrations of the active agents onto the personal care product is challenging.
There remains a need for a better way to apply an active agent such as an antimicrobial agent to an absorbent personal-care product. For instance, there is a desire for an application method that does not require several additional steps in the manufacture of such a product (e.g. spraying, slot-coating, or the like). There is also a desire for a method of applying an active agent to such a product so that it demonstrates higher efficacy than is currently available.
A first aspect of the present disclosure is an extruded water-soluble article made from a homogeneous material that includes a water-soluble polymer having an extrusion temperature of 50 to 150° C. Thematerial further includes between 0.1% to 50% active agent by article weight.
Another aspect of the present disclosure is a personal absorbent article comprising an absorbent member disposed between a water-impermeable backsheet and a water-permeable liner. An extruded water-soluble article described in the first aspect of the disclosure, in the form of a film and, is disposed between the liner and the absorbent member or on top of the liner.
Other features and aspects of the invention will become apparent by consideration of the detailed description and accompanying drawings.
The foregoing and other features and aspects of the present invention and the manner of attaining them will become more apparent, and the invention itself will be better understood by reference to the following description, appended claims and accompanying drawings, where;
It is to be understood by one of ordinary skill in the art that the present disclosure is a description of exemplary aspects of the present invention only, and is not intended as limiting the broader aspects of the present invention.
The term “laminate” refers to a material where a film structure is adhesively or non-adhesively bonded to a web such as a nonwoven or tissue material.
The term “meltblown fibers” refers to fibers formed by extruding a molten thermoplastic material through a plurality of fine, usually circular, die capillaries as molten threads or filaments into a high velocity, usually heated, gas (e.g., air) stream which attenuates the filaments of molten thermoplastic material to reduce their diameter. In the particular case of a coform process, the meltblown fiber stream intersects with one or more material streams that are introduced from a different direction. Thereafter, the meltblown fibers and other optional materials are carried by the high velocity gas stream and are deposited on a collecting surface. The distribution and orientation of the meltblown fibers within the formed web is dependent on the geometry and process conditions. Exemplary meltblown processes are described in various patents and publications, including NRL Report 4364, “Manufacture of Super-Fine Organic Fibers” by V. A. Wendt, E. L. Boone and C. D. Fluharty; NRL Report 5265, “An Improved Device For the Formation of Super-Fine Thermoplastic Fibers” by K. D. Lawrence, R. T. Lukas and J. A. Young; and U.S. Pat. No. 3,849,241 to Butin et al. and U.S. Pat. No. 5,350,624 to Georger et al., each of which is incorporated herein by reference in a manner that is consistent herewith.
The terms “nonwoven” and “nonwoven web” refer to materials and webs of material having a structure of individual fibers or filaments which are interlaid, but not in an identifiable manner as in a knitted fabric. The terms “fiber” and “filament” are used herein interchangeably. Nonwoven fabrics or webs have been formed from many processes such as, for example, meltblown processes, spunbond processes, air laying processes, wet layering processes and bonded-carded-web processes.
The term “personal care absorbent articles” or “absorbent articles” in the context of this disclosure includes, but is not limited to diapers, diaper pants, training pants, absorbent underpants, incontinence products, and urinary shields; and the like.
The terms “spunbond” and “spunbond fiber” refer to fibers which are formed by extruding filaments of molten thermoplastic material from a plurality of fine, usually circular, capillaries of a spinneret, and then rapidly reducing the diameter of the extruded filaments.
The term “% by weight,” “weight %,” “wt %” or derivative thereof, when used herein, is to be interpreted as based on the dry weight, unless otherwise specified.
These terms may be defined with additional language in the remaining portions of the specification.
The present disclosure is generally directed to an extruded, water-soluble, thermoplastic article into which an active agent has been incorporated. The thermoplastic water-soluble, polymer from which the article is made has an extrusion temperature of 90° C. to 150° C. The combination of the polymer and active agent(s) is a homogeneous blend having an extrusion temperature of 50° C. to 125° C. The articles made from the homogeneous blend include films, fibers, pellets, or other extruded shapes.
The materials from which the water-soluble, thermoplastic material of the present disclosure is made generally include a polymer and one or more active agents. Other optional materials that improve the performance, look, feel and/or durability may be added to the thermoplastic material.
Polymer: Generally, the polymer used in the present disclosure is polyvinyl alcohol (PVOH), polyethylene oxide (PEO), polyethylene glycol (PEG), polyacylate (acid), polyacylamide, polyester, or a combination of one or more of these polymers. Suitable polymers have an extrusion temperature of 90° C. to 150° C.
One desirable polymer is a highly amorphous vinyl alcohol polymer, sold as “NICHIGO G-POLYMER,” available from Soarus L.L.C., Arlington Heights, Ill. This particular polymer has a molecular weight of 10,000 to 50,000, and a relatively low crystallinity of 5 to 25%.
In one aspect, a copolymer such as ethylene vinyl acetate (EVA) may be combined with the base polymer. It is contemplated that the article of the present disclosure may include up to 30% by weight EVA. EVA aids in extrusion process, provides a means to control the water dissolution speed, and lowers the overall cost if the extruded material.
Active Agent: In one aspect, the active agent is made from one or more antimicrobial agents. Suitable antimicrobials include biocides such as benzoalkonium chloride (“BAC”), didecyl dimethyl ammonium chloride (“DDAC”), and zeolite (“CWT-A”). Other possible active agents include: isothiazolone, alkyl dimethyl ammonium chloride, a triazine, 2-thiocyanomethylthio benzothiazol, methylene bis thiocyanate, acrolein, dodecylguanidine hydrochloride, a chlorophenol, a quaternary ammonium salt, gluteraldehyde, a dithiocarbamate, 2-mercatobenzothiazole, para-chloro-meta-xylenol, silver, chlorohexidine, polyhexamthylene biguanide, a n-halamine, triclosan, a phospholipid, an alpha hydroxyl acid, 2,2-dibromo-3-nitrilopropionamide, 2-bromo-2-nitro-1,3-propanediol, farnesol, iodine, bromine, hydrogen peroxide, chlorine dioxide, a botanical oil, a botanical extract, benzalkonium chloride, chlorine, sodium hypochlorite, or combinations thereof.
The amount of active agent that is loaded into an article is limited due to the integrity of the resulting article structure. If there is too much active agent in an article, it may be unduly weakened. In one aspect, the sum of the active agent(s) is present in a total amount of 0.1% to 50% by weight of the article, or a total amount of 1% to 20% by weight of the article. In another aspect, the sum of the active agent(s) is present in a total amount of 2% to 10% by weight of the article.
Optional Materials: Besides the components noted above, still other additives may also be incorporated into the composition, such as fragrances, melt stabilizers, dispersion aids (e.g., surfactants), processing stabilizers, heat stabilizers, light stabilizers, UV stabilizers, antioxidants, heat aging stabilizers, whitening agents, antiblocking agents, antistatic agents, bonding agents, lubricants, colorants, etc.
In one aspect of the present disclosure, the extruded water-soluble article includes up to 50% thermoplastic starch by weight. The starch acts as a filler to reduce the overall cost of the extruded article. The extruded article may contain as much as 30% starch. One desirable water-soluble thermal starch is a cellulose-based starch obtained from various plant sources, hemicelluloses, modified cellulose (hydroxylalkyl cellulose, cellulose ethers, cellulose esters, etc.), and the like. When a starch is employed, the amount of such additional material may range from about 0.1 wt. % to about 50 wt. % of the homogeneous blend, in some embodiments from about 0.5 wt. % to about 40 wt. %, and in some embodiments, from about 1 wt. % to about 30 wt. %.
Dispersion aids may also be employed to help create a uniform dispersion of the active agent/plasticizer. When employed, the dispersion aid(s) typically constitute from about 0.01 wt. % to about 10 wt. % of the homogeneous blend, in some embodiments from about 0.1 wt. % to about 5 wt. %, and in some embodiments, from about 0.5 wt. % to about 4 wt. %.
The composition may also contain a preservative or preservative system to inhibit the growth of microorganisms over an extended period of time. Suitable preservatives may include, for instance, alkanols, disodium EDTA (ethylenediamine tetraacetate), EDTA salts, EDTA fatty acid conjugates, isothiazolinone, benzoic esters (parabens) (e.g., methylparaben, propylparaben, butylparaben, ethylparaben, isopropylparaben, isobutylparaben, benzylparaben, sodium methylparaben, and sodium propylparaben), benzoic acid, propylene glycols, sorbates, urea derivatives (e.g., diazolindinyl urea), and so forth. Other suitable preservatives include those sold by Sutton Labs, such as “Germall 115” (amidazoiidinyl urea), “Germall II” (diazolidinyl urea), and “Germall Plus” (diazolidinyl urea and iodopropynyl butylcarbonate). Another suitable preservative is Kathon CG.®, which is a mixture of methylchloroisothiazolinone and methylisothiazoiinone available from Rohm & Haas; Mackstat H 66 (available from McIntyre Group, Chicago, Ill.). Still another suitable preservative system is a combination of 56% propylene glycol, 30% diazolidinyl urea, 11% methylparaben, and 3% propylparaben available under the name GERMABEN.® H from International Specialty Products of Wayne, N.J.
To better enhance the benefits to consumers, other optional ingredients may also be used. For instance, some classes of ingredients that may be used include, but are not limited to: antioxidants (for product integrity); astringents-cosmetic (for inducing a tingling sensation on skin); colorants (for imparting color to the product); deodorants (for reducing or eliminate unpleasant odor and protect against the formation of malodor on body surfaces); fragrances (for consumer appeal); skin conditioning agents; and skin protectants (a drug product which protects injured or exposed skin or mucous membrane surface from harmful or annoying stimuli).
In one aspect of the disclosure, a method of making an extruded article may include the following steps. First, a homogenous blend is formed by combining the polymer with at least one active agent and possibly, one or more of the optional ingredients described herein. In one desired embodiment, the polymer is an amorphous, water-soluble vinyl alcohol as described herein. Second, the homogeneous blend is extruded to form an article.
The homogeneous blend has an extrusion temperature of 50° C. to 125° C., or possibly, 90° C. to 125° C. This low extrusion-temperature profile is desirable because some active agents of interest have poor thermal stability. By using a low extrusion-temperature, a wider variety of active agents may be incorporated into the homogenous blend.
Exemplary manufacturing equipment, a method of making articles, and exemplary articles are described herein.
Extrusion Method: The composition of the present disclosure is formed by processing the components together in a melt-blending device (e.g., extruder). The mechanical shear and heat provided by the device allows the components to be blended together in a highly efficient manner without the use of a solvent. Batch and/or continuous melt blending techniques may be employed in the present disclosure. For example, a mixer/kneader, Banbury mixer, Farrel continuous mixer, single-screw extruder, twin-screw extruder, roll mill, etc., may be utilized. One particularly suitable melt-blending device is a twin-screw extruder (e.g., PRISM USALAB ×16, available from Thermo Electric Co., Inc., N.J.).
The polymer and the active agent(s), along with any optional ingredients, form a homogeneous blend. For example, the materials may be blended at a shear/pressure and temperature sufficient to ensure adequate mixing (e.g., at or above the softening point of the polymer), but without adversely impacting the physical properties of the active agent. For example, melt-blending typically occurs at a temperature of from about 50° C. to about 150° C., in some embodiments, from about 90° C. to about 130° C., and in some embodiments from about 110° C. to about 125° C. These lower processing temperatures prevent degradation of the active agent.
Once formed, the homogeneous blend of the present disclosure may be used to create a variety of forms, such as films, fibers, rods, bars or other shapes.
Films: In one particular embodiment, the homogeneous blend is formed into a film, either alone or in conjunction with an additional film-forming material. The film may be used in a wide variety of applications, such as a carrier of active agents for medical products, garments, absorbent articles, etc. The film may have a mono- or multi-layer configuration. Any known technique may be used to form a film from the compounded material such as extrusion coating, coextrusion of the layers, or any conventional layering process.
The process to make the antimicrobial reservoir film is relatively fast considering the high amounts of active agent that can be added to the extrusion process. In one particular embodiment, the film may be formed by flat die extrusion technique. Processes for producing such extrusions are described, for instance, in U.S. Pat. No. 7,666,337 to Yang et al.; U.S. Pat. No. 5,091,228 to Fuji et al; and U.S. Pat. No. 4,136,145 to Fuchs et al.; all of which are incorporated herein in their entirety by reference thereto for all purposes.
In yet another embodiment, however, the film is formed using a casting or blowing technique.
Regardless of how the film is formed, it may be optionally oriented in one or more directions to further improve film uniformity and reduce thickness. For example, the film may be immediately reheated to a temperature below the melting point of one or more polymers in the film, but high enough to enable the composition to be drawn or stretched. In the case of sequential orientation, the “softened” film is drawn by rolls rotating at different speeds or rates of rotation such that the sheet is stretched to the desired draw ratio in the longitudinal direction (machine direction). The film may be made into thicknesses ranging from 0.01 mm up to about 1 mm, or in other aspects, from 0.05 mm to 0.20 mm.
The multi-layer film may contain from two (2) to nine (9) layers, and in some embodiments, from three (3) to five (5) layers. In one example, the multi-layer film has one base layer and one skin layer. The base layer and/or skin layer may contain the active agent(s). The ratio between the layers may range from 1 to 20.
In another example, there is a three-layered film having a core layer “C” that is contains an active agent as described herein. The outer skin layers “S” may act as a protective layer to the core. The ratio between the layers may range from 2% to 98% of the core layer and from 10% to 90% of the two combined skin layers. For instance, the core layer may be up to about 30%, up to about 40%, up to about 50%, up to about 60%, or up to about 70% of the total thickness of the multi-layer film. Each skin layer may be up to about 15%, or up to about 25%, or up to about 35% of the total thickness of the multi-layer film.
The film, either mono- or multi-layered, may be wound and stored on a take-up roll. Various additional potential processing and/or finishing steps known in the art, such as slitting, treating, aperturing, printing graphics may be performed.
In one aspect, the extruded water-soluble film has a basis weight of 5 gsm to 500 gsm. In another aspect, the water-soluble film has a basis weight of 20 gsm to 200 gsm.
In one aspect, the extruded water-soluble film has a tensile strength of 0.5 MPa to 50 MPa according to the Tensile Test of the present disclosure. In another aspect, the film has a tensile strength of 1 MPa to 25 MPa according to the same test.
In one aspect, the extruded water-soluble film has a water dissolution speed from 5 seconds to 30 minutes as determined by the Water Dissolution Test of the present disclosure. In another aspect, the extruded water-soluble article film has a water dissolution speed of 30 seconds to 5 minutes as determined by the same test.
In one aspect, the extruded water-soluble film has an elongation of 5% to 500% according to the Tensile Test of the present disclosure. In another aspect, the film has an elongation of 10% to 100% according to the same test.
Articles: The homogeneous blend of the present invention may also be used to form other types of articles. In one aspect, the extruded water-soluble article is a rod having a circular- or elliptical-shaped extrusion profile. In another aspect, the extruded water-soluble article is a rod having the geometric extrusion profile of a polygon with three to ten sides (e.g. a triangle to a decagon). The rod may be cut into pellets for later processing.
Referring to
Absorbent Articles: The film of the present invention is particularly suitable for use in an absorbent article. An “absorbent article” generally refers to any article capable of absorbing water or other fluids. Examples of some absorbent articles include, but are not limited to, personal care absorbent articles, such as diapers, training pants, absorbent underpants, incontinence articles, feminine hygiene products (e.g., sanitary napkins, pantiliners, etc.), swim wear, baby wipes, and so forth; medical absorbent articles, such as garments, fenestration materials, underpads, bedpads, bandages, absorbent drapes, and medical wipes; food service wipers; clothing articles; and so forth. Several examples of such absorbent articles are described in U.S. Pat. No. 5,649,916 to DiPalma, et al.; U.S. Pat. No. 6,110,158 to Kielpikowski; U.S. Pat. No. 6,663,611 to Blaney, et al., which are incorporated herein in their entirety by reference thereto for all purposes. Still other suitable articles are described in U.S. Patent Application Publication No. 2004/0060112 Al to Fell et al., as well as U.S. Pat No. 4,886,512 to Damico et al.; U.S. Pat. No. 5,558,659 to Sherrod et al.; U.S. Pat. No. 6,888,044 to Fell et al.; and U.S. Pat. No. 6,511,465 to Freiburger et al., all of which are incorporated herein in their entirety by reference thereto for all purposes. Materials and processes suitable for forming such absorbent articles are well known to those skilled in the art.
The present invention may be better understood with reference to the examples presented herein.
First Exemplary Absorbent Article: Referring to
As described, film 41 is made from materials that include a water-soluble, polymer that may have an extrusion temperature of 90 to 150° C.; a plasticizer; and one or more volatile active agents in a total amount of 0.1% to 50% by weight of the article.
Second Exemplary Absorbent Article: Referring to
Provided is experimental data for three antimicrobial agents that act as biocides, namely, zeolite, benzoalkonium chloride, and didecyl dimethyl ammonium chloride. Tests were performed on the various codes for each biocide to determine dissolution, zone of inhibition, and mechanical properties.
Films containing the various amounts of the antimicrobial agents of Table 1 were made as follows. A twin-screw extruder (PRISM USALAB ×16, available from Thermo Electric Co., Inc.) was used to make co-extruded film samples that contain an antimicrobial agent. The extruder specifications were as follows:
The following extruder set-up was used to manufacture the experimental film:
The extruder feed zone was heated to 110° C., the following extruder zones 2-9 were heated to 125° C., and the die was heated to 130° C. The material was extruded.
Referring to
Materials and Reagents:
Microorganisms: frozen stock of Staphylococcus aureus (ATCC 27660) and Pseudomonas aeruginosa (ATCC 15442).
Mueller-Hinton agar (MHA) plates or equivalent plated media. Prepare following manufacturer's directions. Store at 4±2° C. Alternatively, pre-made plates can be utilized.
Mueller-Hinton broth (MHB) or equivalent liquid media. Prepare following manufacturer's directions. Store at 4±2° C. Alternately, pre-made media can be utilized.
Sterile cotton swabs or equivalent.
Sterile forceps.
Positive control disc: Vanocymicin susceptibility discs (6 mm), 30 μg/disc (BD and Company; Sparks, Md.).
Test material, cut into 8 mm discs.
Calipers or other measuring device.
Other ancillary lab supplies.
Supply Set-up:
1. Label growth media plates appropriately for testing codes.
2. Sterilize test material discs with UV exposure in Laminar flow hood for 15 minutes (both sides of disc), if required.
Inoculum:
1. Take appropriate measures to ensure culture purity.
2. Staphylococcus aureus or Pseudomonas aeruginosa is inoculated from an overnight plate or MHB into 5 ml of sterile MHB in a 35° C. incubator for 18-24 hrs.
3. The overnight culture is then adjusted using MHB to the 0.5 McFarland barium sulphate standards (1×108 CFU/ml) or approximately 0.15 OD with a 0.2 cm light path at 660 nm.
4. Discard the cell suspension if it is not used within 30 to 60 min after preparation. Zone of Inhibition Bioassay Procedure:
1. Pre-warm the MHA plates to room temperature. The number of plates required per strain will depend on the number of test materials to be tested and their anticipated zone inhibition diameters; discs should be placed on plates so that zones of inhibition do not overlap.
2. The surface of the plates should be dry. If not, dry the plates (with lids ajar) in a 35° C. incubator for 20-30 min just prior to inoculation. There should be no visible droplets of moisture on the surface of the agar or on the lids of the plates when they are inoculated.
3. Moisten a sterile applicator swab in the standardized cell suspension and express any excess moisture by rotating the swab against the glass above the liquid in the tube. Referring to
(It is recommended that cotton swabs with wooden handles be used for this procedure. Swabs made of synthetic materials do not soak up sufficient suspension to inoculate the entire surface of the plate. Swabs with plastic handles bend when excess suspension is being expressed and may splatter liquid out of the tube.)
4. Repeat step 10.3 to inoculate additional plates as needed.
5. Store the inoculated plates at room temperature for 10-15 min to allow the medium to absorb the moisture from the inoculum.
6. Apply discs of test material to the surface of the inoculated medium with a sterile forceps and tap them to ensure that they are in complete contact with the agar surface. A positive control (vancomycin disc) and negative control (uncoated disc) should be used on each plate. All discs should be approximately the same distance from the edge of the plate and from each other (
7. Invert the inoculated plates and incubate them at 35° C. for 18-24 hours.
8. Examine the plates from the back, viewed against a black background and illuminated with reflected light. With calipers, measure the diameter of each zone of inhibition to the nearest whole millimeter.
Calculation: The zone of inhibition is equal to the diameter of the no-growth area minus the diameter of the disc.
The inhibition zone sizes given in this test protocol are derived from test methods used at the Center for Disease Control as well as AATCC Method 147-1998 (19) based on the National Committee for Clinical Laboratory Standards (20-21) and ASTM E2149-01 step 12.2 (22). The diameters of zones of inhibition may vary depending on many factors including medium base, humidity, and the age of the medium. Thus, it is important to follow one protocol as closely as possible to obtain results comparable between labs, personnel, and experiments. It may be necessary to determine zone interpretative sizes for disc diffusion results that are appropriate to local conditions. These criteria may be determined with use of reference strains and known challenge compounds and amounts.
Results:
Tensile Test: Prior to testing, samples were initially conditioned at 75° F./50% relative humidity for 24 hours. Thereafter, the strip tensile strength values were determined in accordance with ASTM Standard D-5034. A constant-rate-of-extension type of tensile tester was employed. The tensile testing system was a Synergie 200 tensile frame. The tensile tester was equipped with TESTWORKS 4.08B software from MTS Systems Corp. to support the testing. An appropriate load cell was selected so that the tested value fell within the range of 10-90% of the full scale load. The film samples were initially cut into dog-bone shapes with a center width of 3.0 mm before testing. The samples were held between grips having a front and back face measuring 25.4 millimeters×76 millimeters. The grip faces were rubberized, and the longer dimension of the grip was perpendicular to the direction of pull. The grip pressure was pneumatically maintained at a pressure of 40 pounds per square inch. The tensile test was run using a gauge length of 18.0 millimeters and a break sensitivity of 40%. Five samples were tested by applying the test load along the machine-direction and five samples were tested by applying the test load along the cross direction. During the test, samples were stretched at a crosshead speed of about 127 millimeters per minute until breakage occurred. The modulus of elasticity, peak load, peak stress, elongation (percent strain at break), and energy per volume at break (total area under the stress-strain curve) were measured.
The tensile test results showed that the films have excellent mechanical properties for high-speed converting processes. This allows the films to easily be placed into articles such as the absorbent articles and laminates described herein.
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This application claims priority as a continuation of Application No. 61/884574, filed on Sep. 30, 2013. The entirety of Application No. 61/884574 is incorporated herein by reference.
Filing Document | Filing Date | Country | Kind |
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PCT/US2014/057798 | 9/26/2014 | WO | 00 |
Number | Date | Country | |
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61884574 | Sep 2013 | US |