SLOW-RELEASE COMPOSITION FOR ABATING ACID WATER FORMATION, AND METHOD OF MAKING THE SAME

Abstract: Various chemolithotrophic bacteria such as Thiobacillus ferrooxidans by direct or indirect mechanisms catalyze the oxidation of metal sulfides and produce acid, i.e. suilfuric acid and soluble metal salts at a much faster rate than chemical oxidation. Elimination of such bacteria would inhibit the formation of the acid. The natural production of such acids is particularly troublesome in mines e.g. coal mines, since acid water is produced which is damaging to the environment. An effective method of abating or eliminating such acid water production is to apply a bactericide such as a biodegradable organic surfactant which at low pH values are bactericides and hence inhibit the bacteria from catalyzing the metal sulfides. The affected acid water site can thus be treated with the surfactant which provides a temporary or short term result usually for a few months. A long term solution, that is 1 year to several years, is provided through the use of a slow release composition of the present invention in which a heterogeneous matrix contains a thermoplastic domain and an organic surfactant domain. A suitable porosity is created when proper amounts of surfactant are utilized so that a long term slow release composition is formed. A method of making the heterogeneous matrix or slow release composition involves the dry blending of a thermoplastic compound and various processing aids, subsequently adding a bactericide thereto and mixing under shear and heat the resulting molten composition. A suitable slow release article can be formed such as pellets.

Description: FIELD OF THE INVENTION This invention relates to a composition as well as to a method for providing slow release compositions containing an organic surfactant which inhibits acid producing bacteria from catalyzing metal sulfides such as iron sulfide. BACKGROUND OF THE INVENTION U.S. Patent No. 4,314,966 to Kleinmann relates to a rubber matrix containing a surfactant therein to inhibit the bacteria Thiobacillus ferrooxidans . "Developments in Controlled Release Technology and Its Application in Acid Mine Drainage", by L. A. Fox and Vijay Rastogi, 1983 Symposium on Surface Mining, Hydrology, Sedimentology and Reclamation, November 27-December 2, 1983, relates to controlling acid mine drainage wherein rubber matrix as well as a thermoplastic matrix, for example polyethylene, were utilized in association with anionic detergents such as sodium lauryl sulfate. "Laboratory Methods for Determining the Effects of Bactericides on Acid Mine Drainage", by Mark A. Shellhorn and Vijay Rastogi, 1984 Symposium on Surface Mining, Hydrology, Sedimentology, and Reclamation, December 2-7, 1984, relates to laboratory tests wherein surfactants were utilized to control acid-producing bacteria. "Use of Controlled Release Bactericides for Reclamation and Abatement of Acid Mine Drainage", by Andrew A. Sobek, Mark A. Shellhorn, and Vijay Rastogi, preprint of Presentation to the International Mine Water Congress, Granada, Spain, September 17-21, 1985, relates to tests controlling acid mine drainage through the use of surfactants as well as control release compositions. "The Effects of Particle Size Distribution on the Rate of Mine Acid Formation and its Mitigation by Bacterial Inhibitors", by Mark A. Shellhorn, Andrew A. Sobek, and Vijay Rastogi, American Society of Surface Mining & Reclamation, Denver, CO., October 8-10, 1985, relates to the effect of particle size of metal sulfide refuse on acid water production. "Effect of Bactericide Treatments on Metalliferrous Ore Tailings", by Andrew A. Sobek, Vijay Rastogi, and Mark A. Shellhorn, Society for Surface Mining & Reclamation, March 17-20, 1986, Jackson, Mississippi, relates to bactericide treatments of uranium, copper, nickel, etc. tailings. "ProMac Systems for Reclamation and Control of Acid Production in Toxic Mine Waste" by Vijay Rastogi, Richard Krecic, and Andrew Sobek, Surface Mine Drainage Task Force Symposium, March 31 - April 1, 1986, relates to a system utilizing surfactants to treat a reclaimed area. GB-A-2 080 687 teaches that by incorporating a porosigen into the device one can control the release rate of the active components. The porosigen generally has two functions: 1) it creates pores which later in the product's lifetime allow dissolution of the active component through them, 2) it controls the release rate independently of the solubility of the active component by dissolving at a rate unique to the porosigen. Thus, it teaches that you put the polymer, active ingredient, and porosigen in a mixer, heat to above the softening point, and then blend them. This solvation process of the porosigen controls the release rate of the active component. SUMMARY OF THE INVENTION Accordingly, it is an aspect of the present invention to provide a method of making and a controlled release surfactant bactericide composition to control acid production in active and/or reclaimed mines. It is yet another aspect of the present invention to provide a controlled release surfactant bactericide, as above, wherein said surfactant is generally a biodegradable organic anionic surfactant. It is a further aspect of the present invention to provide a controlled release surfactant bactericide, as above, wherein said controlled release surfactant bactericide is contained in a thermoplastic matrix having a low softening point. It is a still further aspect of the present invention to provide a controlled release surfactant bactericide, as above, wherein the slow release bactericide is a heterogeneous blend of the thermoplastic compound and the surfactant bactericide. It is yet another aspect of the present invention to provide a controlled release surfactant bactericide, as above, wherein said thermoplastic matrix has a suitable porosity so that release of said surfactant bactericide is over an extended period of time. It is yet another aspect of the present invention to provide a controlled release surfactant bactericide, as above, wherein the slow release thermoplastic matrix is formed by dry blending the thermoplastic and at least one compounding agent, and subsequently mixing and shearing a molten mass thereof containing the surfactant bactericide therein. It is yet another aspect of the present invention to provide said slow release thermoplastic matrix in the form of pellets by extruding said molten mass and pelletizing the same. These and other aspects of the present invention will become apparent from the following detailed description. Thus, the present invention provides a slow release composition for reducing acid water formation from a metallic sulfide material exposed to water, oxygen, and acid catalyzing bacteria, comprising: a uniform, immiscible, thoroughly mixed heterogeneous composition containing a thermoplastic domain and a surfactant domain, said thermoplastic domain made from a thermoplastic compound having a softening point of 210 °C or less, said uniform, immiscible, thoroughly mixed heterogeneous composition formed from an effective concentration of an organic surfactant inhibiting acid forming bacteria shear blended in the presence of heat with said thermoplastic compound so that said uniform, immiscible, thoroughly mixed heterogeneous composition has a porosity capable of extended slow release of at least one year upon contact with water, and wherein said effective extended slow release concentration of said organic surfactant is from 5 parts by weight to 150 parts by weight per 100 parts by weight of said thermoplastic material. It further provides a method of making a slow release thermoplastic article for inhibiting acid producing bacteria comprising the steps of, adding and mixing under heat a thermoplastic compound and an effective amount of a porosity forming surfactant inhibiting acid forming bacteria for forming a slow release heterogeneous composition, and applying shear and mixing said thermoplastic compound and said porosity forming surfactant at a temperature below the degradation temperature of said surfactant, and forming a thermoplastic article having an extended porosity slow release surfactant. DETAILED DESCRIPTION OF THE INVENTION The controlled release composition of the present invention comprises a blend of thermoplastic compound with an immiscible surfactant bactericide so that the resultant thermoplastic matrix has a porosity capable of extended long term release of the surfactant. By "controlled release" it is meant that the release rate and/or duration of release of the surfactant can be varied. The thermoplastic compound utilized to form the matrix can generally be any thermoplastic polymer which is not degraded at processing temperatures and is compatible, that is accepts the surfactant. Inasmuch as many surfactant bactericides degrade at temperatures at about 211°C or even less, the Vicat softening point of the thermoplastic compound is generally 210°C or less, desirably 150°C or less, and preferably 110°C or less. Various suitable thermoplastic compounds include polypropylene, polystyrene, styrene-butadiene-styrene triblock copolymers such as the various Kraton® block copolymers manufactured by Shell, polyester, polyurethane, nylon®, polyvinyl chloride, ethylene-vinylacetate copolymers and polyethylene. While the ethylene-vinylacetate copolymers are a desired thermoplastic, the various low melting point polyethylenes are preferred such as those that have a Vicat softening point at a temperature of from about 60°C to about 90°C. The various other components of the present invention are generally based upon 100 parts by weight of the thermoplastic material. In the reclamation or treating of various metal sulfides, and especially iron sulfide, acid forming bacteria such as Thiobacillus ferrooxidans catalyze the oxidation of metal sulfides and produce acids as well as soluble metals. Over a period of time, a considerable acid content can build up. Such buildup is usually in association with various earth disturbance activities including earth mines as well as surface mines since large amounts of the various sulfides are available. Such acid buildup is undesirable in that it is damaging to the ecology in that it prevents vegetation from sprouting and growing as well as killing existing vegetation, causing erosion and sedimentation problems down stream, and the acid itself causing destruction of aqueous life. The production of the acid must generally be prevented for at least three years or more to break the acid production cycle and to permit three main natural biological processes to occur; that is 1) a healthy root system which competes for both oxygen and moisture with the acid producing bacteria, 2) populations of beneficial heterotrophic soil bacteria and fungi are reestablished, resulting in the formation of organic acids which are inhibitory to Thiobacillus ferrooxidans , and 3) the action of plant-root respiration and the heterotrophic bacteria which increase CO₂ levels in the soil resulting in an unfavorable microenvironment for growth of Thiobacillus ferrooxidans . In order to permit ground cover to continue to grow or reestablish itself, a surfactant bactericide, that is a biodegradable organic surfactant inhibitory to acid producing bacteria such as Thiobacillus ferrooxidans , is utilized in the thermoplastic matrix. Generally, cationic and especially anionic surfactants are very effective biocides with regard to acid producing bacteria. Considering the cationic surfactants, examples of such suitable surfactants include cocodimethylbenzylammonium chloride and N(acylocolaminoformylmethyl)pyridinium chloride. The anionic surfactants and salts thereof, especially sodium, are preferred. A group of preferred anionic surfactants are the various linear alkylbenzene sulfonates (LAS) as for example dodecylbenzene sulfonate, and the like. Especially preferred compounds of the present invention are the sodium salts of alkylbenzene sulfonic acid containing a combination of different alkyl chain lengths having a typical average of approximately 11.8 or 12, such salts having an alkyl average length of approximately 13 and such sodium salts having approximately an average alkyl chain length of 14. Generally the alkyl chain can have from 9 to 18 carbon atoms. Another group of suitable anionic surfactants which function as effective bactericides are the various alkyl sulfates and sodium salts thereof wherein the alkyl group has from 12 to 18 carbon atoms. Another suitable anionic surfactant is the various alpha olefin sulfonates wherein the total number of carbon atoms is from 16 to 20, and the sodium salts thereof. Yet another suitable surfactant bactericide is the various secondary alkane sulfonates having a total number of 14 to 18 carbon atoms. The various alcohol ethoxy sulfates constitute another suitable anionic surfactant bactericide wherein the total number of carbon atoms is from 12 to 22 carbon atoms. Another suitable bactericide is the various alkylphenol ethoxylates having a total number of from 18 to 72 carbon atoms. The various alcohol ethoxylates can also be utilized as suitable surfactant bactericides containing a total number of from 14 to 58 carbon atoms. It is to be understood that various salts of the above surfactants and especially sodium salts can be utilized. The various alkyl sulfates constitute a desired group such as sodium lauryl sulfate with the linear alkylbenzene sulfonates constituting a preferred group. Still other anionic surfactants include a 1 to 18 carbon atom alkyl-phenoxy benzene disulfonic acid; an alkyl- or alkenyl phenoxy benzene disulfonic acid where the alkyl-and alkenyl-groups are C₈ -C₁₆; naphthalene sulfonic acid, alkyl-naphthalene sulfonic acid, or alkenyl-naphthalene sulfonic acid, especially where the alkyl- or alkenyl- groups have relatively short chain lengths, of C₈ or below and preferably C₁- C₄. A list of various other cationic as well as anionic surfactants can be found in the 1978 annual edition or the 1983 annual edition of McCutcheon's Detergents and Emulsifiers, North American Edition. The surfactants are blended with the thermoplastic compounds at specific concentrations to produce a slow release composition or matrix at temperatures below the degradation point of the surfactant and yet at temperatures above the softening point of the thermoplastic compound. That is, a matrix is formed having distinct phases therein, a continuous thermoplastic phase or domain and a surfactant phase. The surfactants are generally immiscible with the thermoplastic compound and hence release of the surfactant occurs through elution, that is through solubility and hydrostatic pressure. A heterogeneous matrix is thus formed having a pore structure therein formed by the surfactant bactericide. The resulting porosity, that is the amount of pore structure formed within the thermoplastic matrix by the surfactant bactericide is important and critical to effective slow release rates in order to achieve release over an extended period of time. In other words, long term leaching of the surfactant is achieved upon contact with water with a surfactant filled porous network within the thermoplastic matrix. Naturally, the thermoplastic matrix is formed by mixing the thermoplastic compound and the surfactant compound in a manner as described hereinbelow and forming an article therefrom such as a pellet. According to the concepts of the present invention, it has been found that a suitable porosity for long term release, that is generally at least 1 or 2 years, desirably at least 3 to 5 years, and preferably at least 5 years, can be achieved by the utilization of desired amounts of the surfactant. Thus, a maximum amount of surfactant is approximately about 150 parts by weight or less for every 100 parts by weight of a thermoplastic compound. The concentration of the surfactant can vary to approximately 5 parts by weight based upon 100 parts by weight of the thermoplastic compound. A desired range is from 25 parts to 120 parts by weight, and preferably from 35 parts to 50 parts by weight per 100 parts by weight of the thermoplastic compound. Generally, the slow release will vary with the type of thermoplastic compound utilized and especially with the concentration of the surfactant. Smaller amounts or concentrations of the surfactants form a smaller porous network or porosity and result in longer release periods. Generally, approximately 50 parts by weight of surfactant will result in a release period of 2 to 5 years whereas smaller amounts such as 25 to 35 parts by weight will result in release periods of approximately 5 to 10 years. The slow release composition of the present invention is added to a particular environment to effectively control, that is to retard the formation of acid water. Naturally, the amount of acid water varies with the amount of metal sulfide present such as iron sulfide, and the like, the amount of water drainage, oxygen, bacteria, and the like. An effective amount of slow release material added to a specific site area is site specific and based upon hydrology, topography, climatic factors, and physical and chemical parameters of the site material. Such effective amounts can be from 3.7 to 156.3 g surfactant/m³ (10 lbs. to 425 lbs. by weight of surfactant per acre foot) and more desirably from 33.1 to 73.6 g surfactant/m³ (90 lbs. to 200 lbs. per acre foot). The application of the slow release thermoplastic composition of the present invention will retard or substantially eliminate acid water for extended periods of time such that ground cover or vegetation can commence growth and take a sufficient foothold whereby the natural biological processes of the vegetation will break the acid production cycle, as noted hereinabove. In order to aid in initially abating or eliminating the production of the acid producing bacteria such as Thiobacillus ferrooxidans , an initial application of only a surfactant, is applied to the specific site, area, etc. The amount of such surfactant bactericide which is generally the same type of surfactant set forth hereinabove, is an amount of matrix containing from 2.6 to 110.3 g surfactant/m³ (7 lbs. of surfactant to 300 lbs. of surfactant per acre foot), and desirably from 16.5 to 55.2 g surfactant/m³ (45 lbs. to 150 lbs. of surfactant per acre foot). In other words, an amount of matrix material is utilized such that the weight of surfactant therein is generally within the above ranges. The method of application of the raw surfactant can be in any conventional manner as by spraying a solution and/or spreading in a wet or dry form. The slow release composition of the present invention is made by mixing the various ingredients in a manner as set forth hereinbelow. The composition is then generally extruded and pelletized. Accordingly, various compounding ingredients can be used to aid in the mixing and extruding of the slow release composition. Such compounding aids are generally known to the compounding and extruding art and can be used in conventional amounts. Thus, various antioxidants can be utilized such as hindered phenols to aid in preventing degradation of the polymer matrix and the surfactant. Various conventional types of pigments such as titanium dioxide, carbon black, and the like can be utilized in small amounts in order to achieve a desired color or hue so as to color code various concentrations or porosities. Processing aids such as lubricants, silicas, and fluxing agents are utilized to optimize mixing and processing operations. Suitable lubricants which also control dust problems include high grade mineral oils, polymer processing oil, and the like. The amount thereof is usually quite small, as 1 or 2 parts by weight per 100 parts by weight of thermoplastic compound. Examples of suitable silicas include amorphous silica, and the like, and are utilized in sufficient amounts to provide processing control and usually from 1 to 20 parts by weight per 100 parts by weight of the thermoplastic compound. Examples of suitable fluxing agents include stearic acid, calcium stearate, or other lubricants, and the like in suitable amounts to provide for release of compounds from metal surfaces of processing equipment as from about a total of 1 to 4 parts by weight per 100 parts by weight of the thermoplastic compound. The slow release thermoplastic composition of the present invention is prepared in the following manner. The thermoplastic such as polyethylene is added to a mixer such as a ribbon blender along with all of the miscellaneous ingredients or compounding agents to form a preblend. Thus, the various pigments, lubricants, antioxidants, and processing aids such as stearic acid and talc are added to the ribbon blender. The various components are added dry in that it is imperative that dry blending occur to enable efficient mixing of the ingredients. The preblend is desirably mixed at ambient temperature. The preblend is subsequently added to a temperature controlled mixer such as a Banbury. The surfactant of the present invention along with any silica is also added and mixed under heat at approximately 87.8°C (190°F) to 137.8°C (280°F), such as 104.4°C (220°F). High temperatures are avoided to minimize thermal degradation and permit better process control. The temperature controlled mixer incorporates the added ingredients into the preblend. Mixing continues until completed whereupon the composition is dumped or added to a two-roll mill or extruded. To obtain additional mixing, typically one of the rolls, for example the back roll, turns at a high rate of speed but is cool, that is has a temperature of from 10°C (50°F) to 37.8°C (100°F) with approximately 21.1°C (70°F) being preferred. The remaining roll turns at a lower or slow rate of speed, for example the front roll, but is heated to a higher temperature as from 60°C (140°F) to 93.3°C (200°F) with approximately 71.1°C (160°F) being preferred. Alternatively, the back roll can be hot and the front roll can be cool. The milling ensures that the various components are thoroughly mixed together albeit separate and distinct phases, that is different domains exist inasmuch as the surfactant is immiscible in the thermoplastic compound. After sufficient mixing has occurred, a portion of the material from the first two-roll mill, for example a ribbon of material is fed to a second two-roll mill which is operating under the same conditions as the initial two-roll mill. Hence, the second mill has a fast roll and a slow roll with one roll being operated at a lower temperature than the remaining roll. After a sufficient amount of time on the second mill to obtain uniformity, the heterogeneous immiscible but thoroughly mixed composition is fed as a ribbon of material into an extruder. The majority portion of the extruder is operated at a relatively low temperature as from 26.7°C (80°F) to 65.6°C (150°F) with 37.8°C (100°F) being preferred which is approximately the incoming temperature of the ribbon. Upon entering the extruder, the temperature of the composition is gradually heated as it passes therethrough until it reaches a face plate. In the preferred embodiment of the present invention, a hot melt die face plate pelletizer is utilized which is operated at a temperature of 121.1°C (250°F), although it can be from 82.2°C (180°F) to 148.9°C (300°F). Upon passing through the die face plate pelletizer, it is sheared by rotating blades whereby pellets are formed. The pellet size is a function of the diameter of the apertures in the face plate, the ejection pressure of the extrudate, the flow rate of the extrudate, the extruder temperature, the rotational speed of the shearing blades, as well as the slow release formulation. The formed pellets are cooled and conveyed by water at a temperature of from 15.6°C 60°F to 65.6°C 150°F with approximately 29.5°C (85°F) being preferred The preferred method of cooling however is by air. The size of the pellets can generally range from 2.54mm (0.1 inch) to 25.4mm (1.0 inch). A desirable pellet size with regard to slow release properties and sufficient surface area is a cylinder approximately (6.35mm) (1/4") in diameter and 6.35mm (1/4") in length. Another or alternative method of forming a slow release thermoplastic composition is to generally add all of the various components together and mix in the presence of heat at a temperature above the softening point of the thermoplastic compound and then to subsequently form a desired article. Thus, a porosity forming surfactant as set forth hereinabove in a suitable or effective amount can be added to a mixer such as a Banbury along with a thermoplastic compound, as noted hereinabove, along with the various compounding agents. It is noted that only one compounding agent need be utilized which is a lubricant processing aid such as stearic acid, calcium stearate, and the like. The temperature of the mixer, as noted, is above the softening point of the thermoplastic compound. Mixing under heat generally continues a suitable amount of time such that a uniformity of the various components is achieved. Thus, a porous forming network is formed by the surfactant throughout the thermoplastic matrix upon cooling of the mixture. That is, upon use of the thermoplastic composition, the surfactant will be removed thereby leaving a porous thermoplastic matrix. The molten mass from the mixer is then generally formed into a convenient article by any suitable forming apparatus. For example, the heated composition can be dropped or added to a compression molding machine wherein bricketts, pellets, and the like are formed. The amounts of the various components is as set forth hereinabove as is the desired release times of the formed article. The invention will be better understood by reference to the following examples: EXAMPLE I Example I had the following formulation: MATERIAL AMOUNT Sodium dodecylbenzene sulfonate; carbon chain C₉-C₁₃ 17.03 kg (37.5 lbs.) For example, NACCONOL® 90G, from The Stepan Co. Polyethylene 45.3 6 kg (100.0 lbs.) For example, PETROTHENE® NA270-00, from U.S. Industrial Chem. Co. 1,2-Bis(3,5-Di-Tert-Butyl-4-Hydroxyhydrocinn-amoyl)Hydrazine 0.23 kg (0.5 lb.) For example, IRGANOX® MD-1024, from Ciba-Geigy Corp. Petroleum Oil 0.45 kg (1.0 lb.) For example, SHELLFLEX® 371, from Shell Oil Co. Amorphous Silica 3.63 kg (8.0 lb.) For example SYLOX® 2, from W. R. Grace & Co. TALC 0.91 kg (2.0 lb.) For example, MISTRON VAPOR TALC® from Cyprus Mineral Co. Stearic Acid 0.45 kg (1.0 lb.) For example, EMERSOL®-132, from Emery Chem. Yellow Pigment 0.09 kg (0.2 lb.) For example, LR 6475, 80% yellow 42, 20% polyethylene, from Lancer Dispersion, Inc. The above formulation was prepared in pellets of approximately 6.35mm (1/4 inch) by 6.35mm (1/4 inch) in a manner as set forth hereinabove, which is hereby fully incorporated. That is, all of the ingredients with the exception of the silica and the sodium dodecylbenzene sulfonate were added to a ribbon blender and blended. Subsequently, the silica and the sodium dodecylbenzene sulfonate were added and mixed. The pellets produced were added to distilled water and the number of hours to 50% extraction of the surfactant contained in the slow release composition is set forth in Table I as is the expected pellet life. The actual life in the earth's environment is much longer since release occurs at a much slower rate. EXAMPLE II Example II contained the following formulation: MATERIAL AMOUNT Sodium dodecylbenzene sulfonate; carbon chain C₉-C₁₃ 21.91 kg (48.31 lb.) For example, NACCONOL® 90G, from The Stepan Co. Polyethylene 45.36 kg (100.00 lb.) For example, PETROTHENE® NA270-00, from U.S. Industrial Chem. Co. 1,2-Bis(3,5-Di-Tert-Butyl-4-Hydroxyhydrocinn-amoyl)Hydrazine 0.23 kg (0.5 lb.) For example, IRGANOX® MD-1024, from Ciba-Geigy Corp. Petroleum Oil 0.45 kg (1.00 lb.) For example, SHELLFLEX® 371, from The Shell Oil Co. Amorphous Silica 3.63 kg (8.00 lb.) For example, SYLOX® 2, from The W. R. Grace & Co. TALC 0.91 kg (2.00 lb.) For example, MISTRON VAPOR TALC® from Cyprus Minerals Co. Stearic Acid 0.453 kg (1.00 lb.) For example, EMERSOL®-132, from Emery Chemicals Phthalocyanine 0.024 kg (0.052 lb.) For example, Q-5755 MUPCO® 50% PHTHALO® Blue RS, from Ciba-Geigy Corp. This above formulation was made into a slow release thermoplastic composition in a manner as set forth in Example I. When subjected to distilled water, the hours to 50% extraction of the surfactant and the expected release life are set forth in Table I. RUBBER CONTROL In a manner as set forth in U.S. Patent No. 4,314,966 to Kleinmann, a rubber matrix was prepared having the following formulation: MATERIALS PARTS BY WEIGHT Natural Rubber 50 parts SBR 50 parts Carbon Black 10 parts Sodium Lauryl Sulfate 40 parts The above rubber formulation when prepared into a slow release composition was tested in distilled water in the same manner as Examples I and II. The time to 50% extraction as well as expected life is set forth in Table I. EXAMPLE CONCENTRATION-PARTS OF SURFACTANT PER 100 PARTS OF POLYETHYLENE HOURS TO 50% EXTRACTION OF SURFACTANT EXPECTED LIFE I 37.5 478 hours Greater than 10 years II 48.3 85 hrs. 3-5 years Rubber Control 40 25 hrs. 6 mos.-1 year As readily apparent from Table I, the slow release compositions of the present invention containing a thermoplastic matrix and having a surfactant porosity network therein resulted in much slower release times. That is, release times of anywhere from at least 3 times to about 19 times as long as the rubber control. Moreover, from actual experience, it has been shown that a rubber matrix will not have a release life much beyond 6 months to 1 year since it substantially degrades, whereas the thermoplastic matrixes of the present invention can last up to 100 years or more. Thus, the porosity-forming network of the present invention within the thermoplastic matrix provides a much greater release life.

Claims: A slow release composition for reducing acid water formation from a metallic sulfide material exposed to water, oxygen, and acid catalyzing bacteria, comprising: a uniform, immiscible, thoroughly mixed heterogeneous composition containing a thermoplastic domain and a surfactant domain, said thermoplastic domain made from a thermoplastic compound having a softening point of 210 °C or less, said uniform, immiscible, thoroughly mixed heterogeneous composition formed from an effective concentration of an organic surfactant inhibiting acid forming bacteria shear blended in the presence of heat with said thermoplastic compound so that said uniform, immiscible, thoroughly mixed heterogeneous composition has a porosity capable of extended slow release of at least one year upon contact with water, and wherein said effective extended slow release concentration of said organic surfactant is from 5 parts by weight to 150 parts by weight per 100 parts by weight of said thermoplastic material. A slow release composition according to claim 1, wherein the softening point of said thermoplastic compound is 150°C or less, wherein said thermoplastic is polyethylene, a copolymer of ethylene and vinyl acetate, polypropylene, polystyrene, a styrene-butadiene-styrene triblock polymer, polyester, polyurethane, nylon®, polyvinylchloride, and combinations thereof, wherein said surfactant is an anionic surfactant, wherein the amount of said surfactant is from 25 parts by weight to 120 parts by weight per 100 parts by weight of said thermoplastic material, and wherein said anionic surfactant is a linear alkylbenzene sulfonate, an alkyl sulfate, an alpha olefin sulfonate, a secondary alkane sulfonate, an alcohol ethoxy sulfate, an alkylphenol ethoxylate, an alcohol ethoxylate, an alkyl phenoxy benzene disulfonic acid, an alkenyl phenoxy benzene disulfonic acid, a naphthalene sulfonic acid, an alkyl-naphthalene sulfonic acid, an alkenyl naphthalene sulfonic acid, or salts thereof. A slow release composition according to claim 2, wherein the softening point of said thermoplastic compound is 110 °C or less, wherein said thermoplastic is polyethylene or a copolymer of ethylene and vinyl acetate, wherein said anionic surfactant is a sodium alkylbenzene sulfonate having an average number of from 11 to 14 carbon atoms in said alkyl group or sodium lauryl sulfate, and wherein the amount of said anionic surfactant is from 35 parts to 50 parts by weight per 100 parts by weight of said thermoplastic compound. A slow release composition for reducing acid drainage in a pyritic sulfide material which is exposed to water, comprising: a uniform, immiscible, thoroughly mixed heterogeneous blend of a thermoplastic compound containing a thermoplastic having a softening point of 210 °C or less and an effective concentration of a shear blended Thiobacillus ferrooxidans inhibiting anionic surfactant whereby a long-term leachable slow release surfactant filled porous network is formed. A slow release composition according to claim 4, wherein the softening point of said thermoplastic is 210°C or less, wherein said surfactant filled porous network releases said surfactant for a period of time of at least 1 year, wherein said thermoplastic is polyethylene, a copolymer of ethylene and vinyl acetate, polypropylene, polystyrene, a styrene-butadiene-styrene triblock polymer, polyester, polyurethane, nylon®, polyvinylchloride, and combinations thereof, and wherein said anionic surfactant is a linear alkylbenzene sulfonate, an alkyl sulfate, an alpha olefin sulfonate, a secondary alkane sulfonate, an alcohol ethoxy sulfate, an alkylphenol ethoxylate, an alcohol ethoxylate, an alkyl phenoxy benzene disulfonic acid, an alkenyl phenoxy benzene disulfonic acid, a naphthalene sulfonic acid, an alkyl-naphthalene sulfonic acid, an alkenyl naphthalene sulfonic acid, or salts thereof. A slow release composition according to claim 5, wherein said surfactant filled porous network releases said surfactant for a period of time of at least 2 years, and wherein the softening point of said thermoplastic is 150°C or less. A slow release composition according to claim 6, wherein said surfactant filled porous network releases said surfactant for a period of time of at least 3 years, and wherein the softening point of said thermoplastic is 110°C or less, wherein said thermoplastic is polyethylene or a copolymer of ethylene and vinyl acetate, and wherein said anionic surfactant is sodium alkylbenzene sulfonate having an average number of from 11 to 14 carbon atoms in said alkyl group or sodium lauryl sulfate. A slow release composition according to claim 6, wherein the amount of said anionic surfactant is approximately 50 parts by weight or less per 100 parts by weight of said thermoplastic compound. A method of reducing acid water formation from a metallic sulfide containing material exposed to water and acid forming bacteria, comprising; adding the composition of anyone of claims 1 to 8 to the metallic sulfide containing material. A method of making a slow release thermoplastic article for inhibiting acid producing bacteria comprising the steps of, adding and mixing under heat a thermoplastic compound and an effective amount of a porosity forming surfactant, inhibitory to acid forming bacteria, for forming a slow release heterogeneous composition, and applying shear and mixing said thermoplastic compound and said porosity forming surfactant at a temperature below the degradation temperature of said surfactant, and forming a thermoplastic article having an extended porosity slow release surfactant.

Inventors: PAUSCH, JERRY B., REUTERN, ERIC, SOBEK, ANDREW A.
Applicants: THE B.F. GOODRICH COMPANY
Application year: 1988
Main classification: A01N25
IPC codes: A01N25