Patent Publication Number: US-2019169055-A1

Title: Method for reducing cyanuric acid in recreational water systems

Description:
RELATED APPLICATIONS 
     This application is a continuation application of U.S. application Ser. No. 15/522,170, filed on Apr. 26, 2017 (now allowed), which is a national stage entry of PCT Application No. PCT/US2015/058593, filed on Nov. 2, 2015, which is a continuation of U.S. application Ser. No. 14/633,664, filed on Feb. 27, 2015, now U.S. Pat. No. 9,302,924, which claims priority to and benefit of U.S. Provisional Application No. 62/073,335, filed in Oct. 31, 2014 and U.S. Provisional Application No. 62/101,741, filed on Jan. 9, 2015, the contents of each of which are hereby incorporated by reference in their entireties. 
    
    
     INCORPORATION-BY-REFERENCE OF SEQUENCE LISTING 
     The contents of the text file named “BIOW-013-001WO-Sequence Listing-ST25.txt”, which was created on Oct. 30, 2015 and is 3 KB in size, are hereby incorporated by reference in their entireties. 
     FIELD OF THE INVENTION 
     The present invention relates to a method for treating recreational water systems with compositions comprising an oxidizable carbon source and micro-organisms, in order to reduce cyanuric acid levels in said water systems. 
     BACKGROUND OF THE INVENTION 
     Recreational water systems such as swimming pools, spas, hot tubs, and jetted tubs, are commonly treated with chlorinated derivatives of cyanuric acid (1,3,5-triazine-2,4,6(1H,3H,5H)-trione) in order to disinfect the water and maintain sanitary conditions. The action of these chlorinated cyanuric acid derivatives, typically referred to by the trade names di- or trichlor, is attributed to the generation of free chlorine as HOCl and OCl-arising from the hydrolytic equilibria of the various chlorinated species (O&#39;Brien et al., 1974). When used in this way there is a gradual accumulation of residual cyanuric acid in the water (Downes et al., 1984). As the level of cyanuric acid rises, free chlorine&#39;s ability to act as a disinfectant is weakened due to increased complexation of chlorine. Above about 50 ppm cyanuric acid, the time it takes to kill bacteria in chlorinated water increases versus similarly treated water without cyanuric acid. In heated systems, such as hot tubs and spas, at even moderate levels of cyanuric acid the amount of time it takes chlorine to kill a common pathogen such as  pseudomonas aeruginosa  can be as much as one hundred times as long as similar systems without cyanuric acid. 
     A 2007 study by the United States Centers for Disease Control and Prevention (Shields et al., 2007) revealed that cyanuric acid significantly diminishes chlorine&#39;s ability to inactivate chlorine-resistant porotozoan and  cryptosporidium . Based on these findings several state and local Departments of Health have issued recommendations to the recreational water industry that cyanuric acid levels not exceed 30 ppm. 
     It is a common practice in the recreational water industry to reduce excess cyanuric acid levels by partially draining pools, tubs, spas, holding tanks, etc., and refilling with fresh water. This is a labor intensive and costly solution, particularly in areas affected by prolonged drought such as Southern California where the cost to replenish a typical 20,000 gallon swimming pool with fresh water is prohibitively high. Accordingly, a need exists in the recreational water industry for compositions and methods to reduce excess cyanuric acid levels that do not require a draining and replenishing SUMMARY OF THE INVENTION 
     The invention provides compositions comprising a mixture of  Bacillus  bacterial species and a mixture of  Lactobacillus  bacterial species. The compositions can further comprise an oxidizable carbon source such as dextrose (e.g., anhydrous or monohydrate) or maltodextrin. The compositions of the invention can be used to reduce cyanuric acid in, e.g., recreational water systems. 
     In some embodiments, the mixture of  Bacillus  bacterial species in the composition includes  Bacillus subtilis, Bacillus licheniformis, Bacillus amyloliquefaciens , and  Bacillus pumilus . In some embodiments, the  Bacillus subtilis  can include one or more subspecies such as  Mojavensis  and  Bacillus subtilis  34 KLB. In some embodiments, each of the  Bacillus  species are individually fermented aerobically, dried and ground, e.g., to an average particle size of about 200 microns. In some embodiments, the bacterial concentration of the  Bacillus  mixture is at least 1×10 6  colony forming units (CFU) per gram. 
     In some embodiments, the mixture of  Lactobacillus  bacterial species can include  Pediococcus acidilactici, Pediococcus pentosaceus , and  Lactobacillus plantarum . In some embodiments, each of the  Lactobacillus  species are fermented anaerobically, dried, and ground, e.g., to an average particle size of about 200 microns. In some embodiments, the bacterial concentration the  Lactobacillus  mixture is at least 1×10 6  colony forming units (CFU) per gram. 
     In one aspect, the invention relates to a composition comprising (a) between 75-99% w/w of anhydrous dextrose or dextrose monohydrate; (b) a mixture of  Bacillus  bacterial species comprising  Bacillus subtilis, Bacillus licheniformis, Bacillus amyloliquefaciens , and  Bacillus pumilus  having a bacterial concentration of at least 1×10 6  colony forming units (CFU) per gram of the mixture, wherein each of the  Bacillus  species are individually fermented aerobically, dried and ground to an average particle size of about 200 microns, and wherein the  Bacillus subtilis  comprises  Mojavensis  and  Bacillus subtilis  34 KLB; and (c) a mixture of  Lactobacillus  bacterial species comprising  Pediococcus acidilactici, Pediococcus pentosaceus , and  Lactobacillus plantarum  having a bacterial concentration of at least 1×10 6  colony forming units (CFU) per gram of the mixture, wherein each of the  Lactobacillus  species are fermented anaerobically, dried, and ground to an average particle size of about 200 microns. 
     In another aspect, the invention relates to a composition comprising (a) between 75-95% w/w of anhydrous dextrose or dextrose monohydrate; (b) at least 1% w/w of a mixture containing  Bacillus  bacterial species comprising  Bacillus subtilis, Bacillus licheniformis, Bacillus amyloliquefaciens , and  Bacillus pumilus , wherein each of the  Bacillus  species are individually fermented aerobically, dried and ground to an average particle size of about 200 microns, and wherein the  Bacillus subtilis  comprises  Mojavensis  and  Bacillus subtilis  34 KLB; and (c) at least 4% w/w of a mixture containing  Lactobacillus  bacterial species comprising  Pediococcus acidilactici, Pediococcus pentosaceus , and  Lactobacillus plantarum , wherein each of the  Lactobacillus  species are fermented anaerobically, dried, and ground to an average particle size of about 200 microns. 
     In a preferred embodiment the invention provides a composition comprising at least 0.4% w/w/ of a first  Bacillus  mixture comprising  Bacillus subtilis  subsp  mojavensis, Bacillus licheniformis, Bacillus amyloliquefaciens , and  Bacillus pumilus ; at least 0.4% w/w/of a second  Bacillus  mixture comprising  Bacillus subtilis, Bacillus licheniformis, Bacillus amyloliquefaciens , and  Bacillus pumilus ; at least 0.4% w/w/ of a mixture o  Bacillus subtilis  34 KLB; and at least 4% w/w of a  Lactobacillus  mixture comprising  Pediococcus acidilactici, Pediococcus pentosaceus , and  Lactobacillus plantarum . The remainder of the composition comprise an oxidizable carbon source such as anhydrous dextrose or dextrose monohydrate. The  Lactobacillus  in the  Lactobacillus  mixture are present in equal proportions by weight. The  Bacillus subtilis  subsp  mojavensis , the  Bacillus amyloliquefaciens , and the  Bacillus pumilus  in the first  Bacillus  mixture are present in equal proportions by weight.′ 
     In yet another aspect, the invention relates to a method of reducing cyanuric acid concentration on recreational water systems comprising contacting a pool&#39;s filtration system with the composition of the invention. 
     In some embodiments of any one of the aforementioned aspects, the bacterial species are non-pathogenic. 
     In some embodiments of any one of the aforementioned aspects, at least 15% of the  Bacillus  bacterial species are  Bacillus subtilis  34 KLB. 
     In some embodiments of any one of the aforementioned aspects, each of the  Lactobacillus  bacterial species is present in equal amounts by weight. 
     In some embodiments of any one of the aforementioned aspects, the composition further comprises an inorganic mineral that stimulates bacterial respiration and growth. Non-limiting examples of inorganic minerals include disodium hydrogen phosphate, dipotassium hydrogen phosphate, sodium dihydrogen phosphate, potassium dihydrogen phosphate, sodium chloride, potassium chloride, magnesium sulfate, calcium sulfate, magnesium chloride, calcium chloride, and iron(III) chloride. 
     Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention pertains. Although methods and materials similar or equivalent to those described herein can be used in the practice of the present invention, suitable methods and materials are described below. All publications, patent applications, patents, and other references mentioned herein are expressly incorporated by reference in their entirety. In cases of conflict, the present specification, including definitions, will control. In addition, the materials, methods, and examples described herein are illustrative only and are not intended to be limiting. 
     Other features and advantages of the invention will be apparent from and encompassed by the following detailed description and claims. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         FIG. 1  is a graph showing significant denitrification was observed within the first 24 hours of dosing the water with the composition of the invention. 
         FIG. 2  is a series of figures showing increased water clarity after dosing the water with the composition of the invention. 
         FIG. 3  is a graph showing decreased cyanuric acid with the composition of the invention. 
         FIG. 4  shows results from MS-MS analysis of in-vitro samples of cyanuric acid treated with the compositions of the invention. 
         FIG. 5  are growth curves showing that organisms can use cyanuric acid as a nitrogen source for growth. 
         FIG. 6  illustrate that Composition B from Example 1 degrades cyanuric acid. 
         FIG. 7  illustrates that with Composition B from Example 1 degrades cyanuric acid in water from public swimming pools 
         FIG. 8  illustrates that pools from southern California treated with Composition B from Example 1 have a drop in cyanuric acid concentration over time after treatment. 
         FIG. 9  shows the results from Florida field trials using Composition B from Example 1. 
         FIG. 10  shows the results comparing Compositions A, B, and C from Example 1 in actual swimming pools. 
     
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
     The invention provides compositions and methods for augmenting the treatment of commercial, public, and private recreational water systems such as swimming pools, spas, hot tubs, jetted tubs or the like. The composition and methods can result in increased clarity of the water, decreased nitrate concentrations, decreased cyanuric acid levels, decreased biological oxygen demand (BOD), decreased total suspended solids (TSS), decreased total Kjeldahl nitrogen (TKN) and decreased fats, oils and grease (FOG) in the water. In specific embodiments, the compositions and methods are used to reduce cyanuric acid levels in recreational water systems where cyanuric acid stabilized chlorine is used as part of the routine disinfection and sanitization protocol. 
     The microbes used in the product according to the present invention may be any conventional mesophilic bacteria. It is preferred that the bacteria are selected from the Lactobacillacae and Bacillaceae families. More preferably the bacteria selected from the genre  Bacillus  and  Lactobacillus  are included in the compositions of the invention. 
     In some aspects the compositions are microbial compositions. The microbial compositions are in powdered, dried form. Alternatively, the microbial compositions are in liquid form. For example, the composition includes non-pathogenic bacteria with the ability to degrade cyanuric acid. 
     In certain embodiments the bacteria are derived from the genus  Bacillus, Lactobacillus, Pseudomonas , or  Moorella . In other aspects the microbial compositions contain a mixture of  Bacillus  and  Lactobacillus  bacteria. In various aspects the mixture contains at least one to seven different strains of  Bacillus . The mixture contains at least one to four different strains of  Lactobacillus . Optionally, the microbial compositions further include an oxidizable carbon source and/or a mixture of inorganic minerals commonly used to stimulate microbial growth. 
     Preferred strains of  Bacillus  include for example,  Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus licheniformis, Bacillus pumilus, Bacillus megaterium, Bacillus coagulans , or  Paenibacillus polymyxa . Preferred  Lactobacillus  strains include for example,  Pediococcus acidilactici, Pediococcus pentosaceus, Lactobacillus plantarum , or  Bifidobacterium animalis.    
     In a preferred embodiment the  Bacillus  is subspecies  Mojavenis . In particularly preferred embodiments, the  Bacillus  is  Bacillus subtilis  strain 34KLB (SEQ ID NO: 1): 
     
       
         
           
               
            
               
                   Bacillus subtilis  strain 34 KLB 
               
               
                 (SEQ ID NO: 1) 
               
               
                 AGCTCGGATCCACTAGTAACGGCCGCCAGTGTGCTGGAATTCGCCCTTAG 
               
               
                   
               
               
                 AAAGGAGGTGATCCAGCCGCACCTTCCGATACGGCTACCTTGTTACGACT 
               
               
                   
               
               
                 TCACCCCAATCATCTGTCCCACCTTCGGCGGCTGGCTCCATAAAGGTTAC 
               
               
                   
               
               
                 CTCACCGACTTCGGGTGTTACAAACTCTCGTGGTGTGACGGGCGGTGTGT 
               
               
                   
               
               
                 ACAAGGCCCGGGAACGTATTCACCGCGGCATGCTGATCCGCGATTACTAG 
               
               
                   
               
               
                 CGATTCCAGCTTCACGCAGTCGAGTTGCAGACTGCGATCCGAACTGAGAA 
               
               
                   
               
               
                 CAGATTTGTGRGATTGGCTTAACCTCGCGGTTTCGCTGCCCTTTGTTCTG 
               
               
                   
               
               
                 TCCATTGTAGCACGTGTGTAGCCCAGGTCATAAGGGGCATGATGATTTGA 
               
               
                   
               
               
                 CGTCATCCCCACCTTCCTCCGGTTTGTCACCGGCAGTCACCTTAGAGTGC 
               
               
                   
               
               
                 CCAACTGAATGCTGGCAACTAAGATCAAGGGTTGCGCTCGTTGCGGGACT 
               
               
                   
               
               
                 TAACCCAACATCTCACGACACGAGCTGACGACAACCATGCACCACCTGTC 
               
               
                   
               
               
                 ACTCTGCCCCCGAAGGGGACGTCCTATCTCTAGGATTGTCAGAGGATGTC 
               
               
                   
               
               
                 AAGACCTGGTAAGGTTCTTCGCGTTGCTTCGAATTAAACCACATGCTCCA 
               
               
                   
               
               
                 CCGCTTGTGCGGGCCCCCGTCAATTCCTTTGAGTTTCAGTCTTGCGACCG 
               
               
                   
               
               
                 TACTCCCCAGGCGGAGTGCTTAATGCGTTAGCTGCAGCACTAAAGGGGCG 
               
               
                   
               
               
                 GAAACCCCCTAACACTTAGCACTCATCGTTTACGGCGTGGACTACCAGGG 
               
               
                   
               
               
                 TATCTAATCCTGTTCGCTCCCCACGCTTTCGCTCCTCAGCGTCAGTTACA 
               
               
                   
               
               
                 GACCAGAGAGTCGCCTTCGCCACTGGTGTTCCTCCACATCTCTACGCATT 
               
               
                   
               
               
                 TCACCGCTACACGTGGAATTCCACTCTCCTCTTCTGCACTCAAGTTCCCC 
               
               
                   
               
               
                 AGTTTCCAATGACCCTCCCCGGTTGAGCCGGGGGCTTTCACATCAGACTT 
               
               
                   
               
               
                 AAGAAACCGCCTGCGAGCCCTTTACGCCCAATAAtTCCGGACAACGCTTG 
               
               
                   
               
               
                 CCACCTACGTATTACCGCGGCTGCTGGCACGTAGTTAGCCGTGGCTTTCT 
               
               
                   
               
               
                 GGTTAGGTACCGTCAAGGTGCCGCCCTATTTGAACGGCACTTGTTCTTCC 
               
               
                   
               
               
                 CTAACAACAGAGCTTTACGATCCGAAAACCTTCATCACTCACGCGGCGTT 
               
               
                   
               
               
                 GCTCCGTCAGACTTTCGTCCATTGCGGAAGATTCCCTACTGCTGCCTCCC 
               
               
                   
               
               
                 GTAGGAGTCTGGGCCGTGTCTCAGTCCCAGTGTGGCCGATCACCCTCTCA 
               
               
                   
               
               
                 GGTCGGCTACGCATCGTCGCCTTGGTGAGCCGTTACCTCACCAACTAGCT 
               
               
                   
               
               
                 AATGCGCCGCGGGTCCATCTGTAAGTGGTAGCCGAAGCCACCTTTTATGT 
               
               
                   
               
               
                 CTGAACCATGCGGTTCAGACAACCATCCGGTATTAGCCCCGGTTTCCCGG 
               
               
                   
               
               
                 AGTTATCCCAGTCTTACAGGCAGGTTACCCACGTGTTACTCACCCGTCCG 
               
               
                   
               
               
                 CCGCTAACATCAGGGAGCAAGCTCCCATCTGTCCGCTCGACTTGCATGTA 
               
               
                   
               
               
                 TTAGGCACGCCGCCAGCGTTCGTCCTGAGCCATGAACAAACTCTAAGGGC 
               
               
                   
               
               
                 GAATTCTGCAGATATCCATCACACTGGCGGCCGCTCGAGCATGCATCTAG 
               
               
                   
               
               
                 AGGGCCCAATCGCCCTAT 
               
            
           
         
       
     
     In some embodiments, at least 15% of the  Bacillus  bacterial species are  Bacillus subtilis  34 KLB. 
     In some aspects the microbial composition comprises a mixture of  Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus licheniformis , and  Bacillus pumilus . In another aspect the microbial composition comprises a mixture of  Pediococcus acidilactici, Pediococcus pentosaceus , and  Lactobacillus plantarum.    
     Suitable water soluble oxidizable carbon sources include carbohydrates, proteins, polysaccharides or mixtures thereof. In preferred embodiments the water soluble carbon source comprises glucose, dextrose, fructose, erythrose, arabinose, ribose, deoxyribose, galactose, mannose, sucrose, lactose, maltose, dextrin, maltodextrin, glycerol, sorbitol, xylitol, inulin, trehelose, low molecular weight starches, modified starches, cellobiose, modified celluloses, amino acids, water soluble peptides, or mixtures thereof. 
     In another aspect the composition contain containing an oxidizable carbon source and a mixture of inorganic minerals. The oxidizable carbon source is water soluble or water dispersible. 
     In some aspects the composition comprises at least 50%, preferably at least 75%, and most preferably at least 90% by weight of a water soluble or water dispersible oxidizable carbon source. In some embodiments the composition comprises at least 91%, 92%, 93%, 94%, 95%, 96%, 97%, 98%, or 99% by weight of a water soluble or water dispersible oxidizable carbon source. In some embodiments, the composition comprises 50%-99% by weight of a water soluble or water dispersible oxidizable carbon source. In some embodiments, the composition comprises 60%-99% by weight of a water soluble or water dispersible oxidizable carbon source. In some embodiments, the composition comprises 70%-99% by weight of a water soluble or water dispersible oxidizable carbon source. In some embodiments, the composition comprises 75%-99% by weight of a water soluble or water dispersible oxidizable carbon source. In some embodiments, the composition comprises 80%-99% by weight of a water soluble or water dispersible oxidizable carbon source. 
     Suitable water dispersible carbon sources include emulsified fats and oils. In certain preferred embodiments the water dispersible carbon source comprises soy lecithin, emulsified vegetable oil or mixtures thereof. Other embodiments include mixtures of water soluble and water dispersible oxidizable carbon sources. 
     In some embodiments, the composition further comprises an inorganic mineral that stimulates bacterial respiration and growth. Suitable minerals include disodium hydrogen phosphate, dipotassium hydrogen phosphate, sodium dihydrogen phosphate, potassium dihydrogen phosphate, sodium chloride, potassium chloride, magnesium sulfate, calcium sulfate, magnesium chloride, calcium chloride, and iron (III) chloride. The minerals comprise between 1 to 50%, 10 to 50%, 20 to 50%, 30 to 50% or 40 to 50% by weight of the composition. Preferably, the minerals comprise about 1%, 2%, 3%, 4%, 5%, 6%, 7%, 8%, 9%, 10%, 15%, 20%, 25%, 30%, 35%, 40%, 45%, 50% by weight of the composition. 
     A preferred composition according to the invention includes about 50% by weight of a water soluble or water dispersible oxidizable carbon source and about 50% by weight of a mixture of inorganic minerals. Preferably, the water soluble or water dispersible oxidizable carbon source is dextrose and the minerals include disodium hydrogen phosphate, dipotassium hydrogen phosphate, potassium dihydrogen phosphate, magnesium sulfate, calcium chloride, and iron(III) chloride. 
     Another preferred composition according to the invention includes at least 94% by weight of a water soluble or water dispersible oxidizable carbon source and the remainder by weight of a microbial mixture. The microbial mixture is a mixture of  Bacillus, Lactobacillus  or both. In some aspects the microbial composition comprises a mixture of  Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus licheniformis  and  Bacillus pumilus . In another aspect the microbial composition comprises  Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus licheniformis Bacillus pumilus, Pediococcus acidilactici, Pediococcus pentosaceus, Lactobacillus plantarum.    
     A first preferred  Bacillus  mixture includes 10% by weight  Bacillus licheniformis,  30% by weight  Bacillus pumilus,  30% by weight  Bacillus amyloliquefaciens  and 30% by weight  Bacillus subtilis . (referred to herein as  Bacillus  Mix #1). Preferably, the  Bacillus subtilis  in  Bacillus  Mix #1 is  Bacillus subtilis  subsp.  Mojavenis    
     A second preferred  Bacillus  mixture includes equal weights of  Bacillus licheniformis, Bacillus pumilus, Bacillus amyloliquefaciens  and  Bacillus subtilis . (referred to herein as  Bacillus  Mix #2). Preferably at least two strains of  Bacillus licheniformis  and  Bacillus subtilis  are present in  Bacillus  Mix #2) 
     A third preferred  Bacillus  mixture includes  Bacillus subtilis, Bacillus licheniformis, Bacillus amyloliquefaciens , and  Bacillus pumilus . In some embodiments, the  Bacillus subtilis  can include one or more subspecies such as  Mojavensis  and  Bacillus subtilis  34 KLB. 
     A forth preferred  Bacillus  mixture includes  Bacillus subtilis  34 KLB ( Bacillus  Mix #3) 
     A preferred  Lactobacillus  mixture includes equal weights of  Pediococcus acidilactici, Pediococcus pentosaceus, Lactobacillus plantarum . (referred to herein as  Lactobacillus  Mix #1). 
     A preferred composition according to the invention includes at least 94% by weight of a water soluble or water dispersible oxidizable carbon source and about at least 0.1 to 1%, 0.1 to 2%, 0.1 to 3%, 0.1 to 4%, 0.1 to 5% of  Bacillus  Mix#1 and/or of  Bacillus  Mix#2. Preferably the composition comprises about 0.1%, 0.2%, 0.3%, 0.4%, 0.5%, 0.6%, 0.7%, 0.8%, 0.9% or 1% of  Bacillus  Mix#1 and/or of  Bacillus  Mix#2. In some embodiments the composition also includes about at least 0.1 to 1%, 0.1 to 2%, 0.1 to 3%, 0.1 to 4%, 0.1 to 5% of  Bacillus  34KLB. Preferably the composition comprises about 0.1%, 0.2%, 0.3%, 0.4%, 0.5%, 0.6%, 0.7%, 0.8%, 0.9% 1%, 2%, 3%, 4% or 5% of  Bacillus  34KLB. 
     In yet another preferred composition according to the invention includes at least 94% by weight of a water soluble or water dispersible oxidizable carbon source and about at least 0.1 to 1%, 0.1 to 2%, 0.1 to 3%, 0.1 to 4%, 0.1 to 5% of  Bacillus  Mix#1 and  Bacillus  Mix#2 and about at least 1 to 5%  Lactobacillus  Mix #1. Preferably the composition comprises about 0.1%, 0.2%, 0.3%, 0.4%, 0.5%, 0.6%, 0.7%, 0.8%, 0.9% or 1% of  Bacillus  Mix#1 and  Bacillus  Mix#2 and about 1%, 2%, 3% 4% or 5% of  Lactobacillus  Mix #1. 
     In another preferred composition according to the invention includes at least 94% by weight of a water soluble or water dispersible oxidizable carbon source and about at least 0.1%, 0.2%, 0.3%, 0.4%, or 0.5%, of  Bacillus  Mix#1; at least 0.1%, 0.2%, 0.3%, 0.4%, or 0.5%  Bacillus  Mix#2; about at least 1 to 5%  Lactobacillus  Mix #1 and 0.1%, 0.2%, 0.3%, 0.4%, 0.5%,  Bacillus  Mix#3. 
     In a more preferred composition according to the invention includes equal weights of  Bacillus  Mix#1,  Bacillus  Mix#2,  Bacillus  Mix#3 and at least 4%  Lactobacillus  Mix #1. The remainder of the composition being a non oxidizable carbon source such as anhydrous dextrose or dextrose monohydrate. 
     In another preferred composition according to the invention includes at least 0.4%  Bacillus  Mix#1, at least 0.4%  Bacillus  Mix#2, at least 0.4%  Bacillus  Mix#3 and at least 4%  Lactobacillus  Mix #1. The remainder of the composition being a non oxidizable carbon source such as anhydrous dextrose or dextrose monohydrate. 
     In some embodiments, the composition comprises (a) between 75-99% w/w of anhydrous dextrose or dextrose monohydrate; (b) a mixture of  Bacillus  bacterial species comprising  Bacillus subtilis, Bacillus licheniformis, Bacillus amyloliquefaciens , and  Bacillus pumilus  having a bacterial concentration of at least 1×10 6  colony forming units (CFU) per gram of the mixture, wherein each of the  Bacillus  species are individually fermented aerobically, dried and ground to an average particle size of about 200 microns, and wherein the  Bacillus subtilis  comprises  Mojavensis  and  Bacillus subtilis  34 KLB; and (c) a mixture of  Lactobacillus  bacterial species comprising  Pediococcus acidilactici, Pediococcus pentosaceus , and  Lactobacillus plantarum  having a bacterial concentration of at least 1×10 6  colony forming units (CFU) per gram of the mixture, wherein each of the  Lactobacillus  species are fermented anaerobically, dried, and ground to an average particle size of about 200 microns. 
     In some embodiments, the composition comprises (a) between 75-95% w/w of anhydrous dextrose or dextrose monohydrate; (b) at least 1% w/w of a mixture containing  Bacillus  bacterial species comprising  Bacillus subtilis, Bacillus licheniformis, Bacillus amyloliquefaciens , and  Bacillus pumilus , wherein each of the  Bacillus  species are individually fermented aerobically, dried and ground to an average particle size of about 200 microns, and wherein the  Bacillus subtilis  comprises  Mojavensis  and  Bacillus subtilis  34 KLB; and (c) at least 4% w/w of a mixture containing  Lactobacillus  bacterial species comprising  Pediococcus acidilactici, Pediococcus pentosaceus , and  Lactobacillus plantarum , wherein each of the  Lactobacillus  species are fermented anaerobically, dried, and ground to an average particle size of about 200 microns. 
     The levels of the bacteria to be used according to the present invention will depend upon the types thereof. It is preferred that the present product contains bacteria in an amount between about 10 5  and 10 11  colony forming units per gram. 
     The microbial compositions according to the invention may be produced using any standard fermentation process known in the art. For example, solid substrate or submerged liquid fermentation under conditions which are optimized for growth of each organism. The fermented cultures can be mixed cultures or single isolates. 
     Preferably, mixtures of bacteria are manufactured by individually aerobically or anaerobically fermenting each organism; harvesting each organism; drying the harvested organisms, grinding the dried organisms to produce a powder combining each of the organisms into the final mixture. 
     In some embodiments, the bacteria are anaerobically fermented in the presence of carbohydrates. Suitable carbohydrates include inulin, fructo-oligosaccharide, and gluco-oligosaccharides. 
     When the cell density of the fermentation reaches about 10 11 -10 12  cfu/g, the individual bacteria are harvested. The bacteria may be harvested by any known methods in the art. For example the bacteria are harvested by filtration or centrifugation. 
     The bacteria are dried by any method known in the art. For example the bacteria are air dried, or dried by freezing in liquid nitrogen followed by lyophilization. 
     The compositions according to the invention have been dried to moisture content less than 20%, 15%, 10% 9%, 8%, 7%, 6%, 5%, 4%, 3%, 2%, or 1%. Preferably, the composition according to the invention has been dried to moisture content less than 5%. 
     In some embodiments the dried powder is ground to decrease the particle size. The bacteria are ground by conical grinding at a temperature less than 10° C., 9° C., 8° C., 7° C., 6° C., 5° C., 4° C., 3° C., 1° C., 0° C., or less. Preferably the temperature is less than 4° C. 
     For example the particle size is less than 1500, 1400, 1300, 1200, 1100, 1000, 900, 800, 700, 600, 500, 400, 300, 200, or 100 microns. Preferably, the freeze dried powder is ground to decrease the particle size such that the particle size is less than 800 microns. Most preferred are particle sizes less than about 400 microns. In most preferred embodiments, the dried powder has a mean particle size of 200 microns, with 60% of the mixture in the size range between 100-800 microns. In various embodiments the freeze dried powder is homogenized. 
     In various embodiments the microbial compositions are mixed with an inert carrier such anhydrous dextrose, dextrose monohydrate, dendritic salt, rice bran, wheat bran, oat bran, soybean meal, rice hulls, or a mixture thereof. 
     The inert carrier is at a concentration of at least 60%, 70%, 75%, 80%, 85%, 90%, 95% or more. Preferably, the inert carrier is at a concentration of about between 75-95% (w/w). 
     In other aspects the bacterial compositions contain an organic emulsifier such as, for example, soy lecithin. The organic emulsifier is at a concentration of about 1%, 2%, 3%, 4%, 5%, 5, 7%, 8%, 9% or 10%. Preferably, the organic emulsifier is at a concentration of between 2 to 5% (w/w). 
     In other aspects the microbial compositions are mixed in equal proportion and added to an oxidizable carbon source. Typically, the final concentration of bacteria in the finished composition ranges from 10 5  to 10 11  cfu/g. In some embodiments, the final concentration of bacteria in the finished composition is at least 10 6  cfu/g. 
     Further, if desired, the microbial compositions may be encapsulated to further increase the probability of survival; for example in a sugar matrix, fat matrix or polysaccharide matrix. 
     Importantly, the compositions of the invention fully disperses upon the addition to water and unlike other water treatment microbial compositions the compositions do not require a pre-activation of the bacteria prior to use. 
     The compositions of the invention can be used to treat both fresh and salt water commercial, municipal, industrial, and residential swimming pools, spas, hot tubs, jetted tubs and the like. 
     An aqueous solution of the dry composition according to the invention can be employed to increase clarity of the water, decrease nitrate concentrations, cyanuric acid levels, biological oxygen demand (BOD), total suspended solids (TSS), total Kjeldahl nitrogen (TKN) and fats, oils and grease (FOG) in body of water. The compositions of the invention may also be used to treat swimming pools and the like to remove scum and reduce algae. 
     Preferably, the compositions of the invention can be used in methods to decrease the concentrations of cyanuric acid in recreational water systems such as swimming pools, spas, hot tubs, jetted tubs and the like. In some embodiments the compositions of the invention stimulates or augments the endogenous biofilm of the recreational water systems filter to break down the cyanuric acid. 
     Solutions of the composition can be pumped into the system to be treated or sprayed onto the surface, or into the airspace surrounding the material, or applied to a filter or other solid support through which the water to be cleaned is passed. The dry material can be mixed into a slurry or solution at the point of application and applied in a similar manner. 
     The invention includes methods for treating a recreational water system by contacting the water system with a composition having an oxidizable carbon source. The carbon source is water soluble or water dispersible. The method results in decreased cyanuric acid levels. 
     Solutions of the composition can be pumped into the system to be treated or sprayed onto the surface, or into the airspace surrounding the material, or applied to a filter or other solid support through which the water to be cleaned is passed. The dry material can be mixed into a slurry or solution at the point of application and applied in a similar manner. 
     The water system is dosed at a concentration range of about 0.01 to 100 ppm, preferably from 0.1 to 10 ppm. 
     In various aspects the invention provides compositions containing a mixture of micro-organisms for augmenting the treatment of swimming pool water. Importantly, the compositions of the invention fully disperse in water and do not require a pre-activation of the bacteria prior to use. 
     The compositions contain a mixture of  Bacillus  organisms or a mixture of  Bacillus  and  Lactobacillus . In some embodiments the compositions contain  Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus licheniformis, Bacillus pumilus, Bacillus megaterium, Bacillus coagulans , or  Paenibacillus polymyxa . In other embodiments the composition contains  Pediococcus acidilactici, Pediococcus pentosaceus, Lactobacillus plantarum , or  Bifidobacterium animalis    
     In preferred embodiments the mixture contains  Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus licheniformis Bacillus pumilus  and  Pediococcus acidilactici, Pediococcus pentosaceus , and  Lactobacillus plantarum . In another preferred embodiment the mixture contains  Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus licheniformis, Bacillus pumilus, Bacillus megaterium, Bacillus coagulans , and  Paenibacillus polymyxa.    
     Each of the organisms in the mixture is individually aerobically ( Bacillus ) or anaerobically ( Lactobacillus ) fermented, harvested, dried, and ground to produce a powder having a mean particle size of about 200 microns, with greater than about 60% of the mixture in the size range between 100-800 microns. 
     In some aspects the composition has a moisture content of less than about 5%; and a final bacterial concentration of about between 10 5 -10 11  colony forming units (CFU) per gram of the composition. 
     In various aspects the composition further contains an inert carrier such as anhydrous dextrose, dextrose monohydrate, dendritic salt, rice bran, wheat bran, oat bran, soybean meal, rice hulls, or a mixture thereof. Preferably, the inert carrier is at a concentration of about between 75-95% (w/w). 
     In other aspects the composition further includes an organic emulsifier. The organic emulsifier is for example, soy lecithin. Preferably, the organic emulsifier is at a concentration of about between 2 to 5% (w/w). 
     Also included in the invention are methods for treating the water in a swimming pool by contacting the water with a composition according to the invention. The method results in increased clarity of the water, decreased nitrate concentrations, decreased cyanuric acid levels, decreased biological oxygen demand (BOD), decreased total suspended solids (TSS), decreased total Kjeldahl nitrogen (TKN) and decreased fats, oils and grease (FOG) in the water. 
     In some aspects the water is contacted by contacting a swimming pool filtration unit with the composition. In other aspects the composition is imbedded in a solid support. 
     The terms “microbial”, “bacteria” or microbes” as used herein, refer to micro-organisms that confer a benefit. The microbes according to the invention may be viable or non-viable. The non-viable microbes are metabolically-active. By “metabolically-active” as used herein is meant that they exhibit at least some respiration or residual enzyme, or secondary metabolite activity characteristic to that type of microbe. 
     By the term “non-viable” as used herein is meant a population of bacteria that is not capable of replicating under any known conditions. However, it is to be understood that due to normal biological variations in a population, a small percentage of the population (i.e. 5% or less) may still be viable and thus capable of respiration and/or replication under suitable growing conditions in a population which is otherwise defined as non-viable. 
     By the term “viable bacteria” as used herein is meant a population of bacteria that is capable of respirating and/or replicating under suitable conditions in which respiration and/or replication is possible. A population of bacteria that does not fulfill the definition of “non-viable” (as given above) is considered to be “viable”. 
     The term “recreational water system” as used herein is meant to include swimming pools, spas, hot tubs, jetted tubs or the like, and includes both salt water and fresh water systems. 
     “Treating” as used herein means inoculating water with an oxidizable carbon source and/or microbes designed to enhance efficient degradation of organic matter, cyanuric acid or both. 
     The term “swimming pools” as used herein are meant to include swimming pools, spas, hot tubs or the like, and includes both salt water and fresh water systems. 
     Unless stated otherwise, all percentages mentioned in this document are by weight based on the total weight of the composition. 
     A better understanding of the present invention may be given with the following examples which are set forth to illustrate, but are not to be construed to limit the present invention. 
     EXAMPLES 
     Example 1: Preparation of the Microbial Species 
     The microbial species of the present invention may be made by any of the standard fermentation processes known in the art. In the following examples, both solid state and submerged liquid fermentation processes are described. 
     Solid State Fermentation— Bacillus  Species 
     Individual purified isolates of  Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus licheniformis, Bacillus pumilus, Bacillus megaterium, Bacillus coagulans , and  Paenibacillus polymyxa  were grown-up in separate fermenters using standard aerobic submerged liquid fermentation protocols. The individual organisms were recovered from the fermenters via centrifugation, mixed together in equal proportions on a weight basis, then added to the following mixture: 1 part inulin, 2.2 parts isolated soy protein, 8 parts rice flour with 0.25% w/w sodium chloride, 0.045% w/w Calcium carbonate, 0.025% w/w Magnesium sulphate, 0.025% w/w Sodium phosphate, 0.012% w/w Ferrous sulphate and 29.6% water. This mixture was allowed to ferment for up to 5 days at 30° C. Upon completion of the fermentation, the entire mixture was freeze dried to a moisture content less than 5%, ground to an average particle size of 295 microns, with 60% of the product in the size range between 175-840 microns, and homogenized. The final microbial concentration of the powdered product is between 10 9  and 10 11  CFU/g. 
     Submerged Liquid Fermentation— Bacillus  Species 
     Individual starter cultures of  Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus licheniformis, Bacillus pumilus, Bacillus megaterium, Bacillus coagulans , and  Paenibacillus polymyxa  are grown according to the following general protocol: 2 grams nutrient broth, 2 grams AmberFerm (yeast extract), and 4 grams Maltodextrin are added to a 250 ml Erlenmeyer flask. 100 milliliters distilled, deionized water was added and the flask stirred until all dry ingredients were dissolved. The flask was covered and placed for 30 min. in an Autoclave operating at 121° C. and 15 psi. After cooling, the flask was inoculated with 1 ml of one of the pure microbial strains. The flask was sealed and placed on an orbital shaker at 30° C. Cultures were allowed to grow for 3-5 days. This process was repeated for each of the micro-organisms in the mixture. This process provided starter cultures of each organism which were then used to prepare larger scale fermentations. 
     Individual fermenters were run under aerobic conditions at pH 7 at the temperature optimum for each species: 
     
       
         
           
               
               
               
             
               
                   
                 TABLE 1 
               
               
                   
                   
               
               
                   
                 Microbe 
                 Temperature Optimum 
               
               
                   
                   
               
             
            
               
                   
                 
                   Bacillus subtilis 
                 
                 35° C. 
               
               
                   
                 
                   Bacillus amyloliquefaciens 
                 
                 30° C. 
               
               
                   
                 
                   Bacillus licheniformis 
                 
                 37° C. 
               
               
                   
                 
                   Bacillus coagulans 
                 
                 37° C. 
               
               
                   
                 
                   Bacillus megaterium 
                 
                 30° C. 
               
               
                   
                 
                   Bacillus pumilus 
                 
                 32° C. 
               
               
                   
                 
                   Paenibacillus polymyxa 
                 
                 30° C. 
               
               
                   
                   
               
            
           
         
       
     
     Solid State Fermentation— Lactobacillus    
     Individual purified isolates of  Pediococcus acidilactici, Pediococcus pentosaceus, Lactobacillus plantarum , and  Bifidobacterium animalis  were grown-up in separate fermenters using standard anaerobic submerged liquid fermentation protocols. The individual organisms were recovered from the fermenters via centrifugation, mixed together in equal proportions on a weight basis, then added to the following mixture: 1 part inulin, 2.2 parts isolated soy protein, 8 parts rice flour with 0.25% w/w sodium chloride, 0.045% w/w Calcium carbonate, 0.025% w/w Magnesium sulphate, 0.025% w/w Sodium phosphate, 0.012% w/w Ferrous sulphate and 29.6% water. This mixture was allowed to ferment for up to 5 days at 30° C. Upon completion of the fermentation, the entire mixture was freeze dried to a moisture content less than 5%, ground to an average particle size of 295 microns, with 60% of the product in the size range between 175-840 microns, and homogenized. The final microbial concentration of the powdered product is between 109 and 1011 CFU/g. 
     Submerged Liquid Fermentation— Lactobacillus    
     Individual, purified isolates of  Pediococcus acidilactici, Pediococcus pentosaceus, Lactobacillus plantarum , and  Bifidobacterium animalis  were grown-up in separate fermenters using standard anaerobic submerged liquid fermentation protocols. After fermentation the individual cultures were filtered, centrifuged, freeze dried to a moisture level less than about 5%, then ground to a mean particle size of 295 microns, with 60% of the product in a size range between 175-840 microns. The individual dried microbial cultures were then mixed in equal proportion by weight to obtain the microbial composition of the present invention. The final microbial concentration of the mixed powdered product is between 10 9  and 10 11  CFU/g. 
     Example 2: Formulation of Swimming Pool Treatment Products 
     The following formulations were prepared by dry blending the ingredients in a ribbon blender (all percentages are by weight): 
     
       
         
           
               
               
             
               
                   
                 TABLE 2 
               
             
            
               
                   
                   
               
               
                   
                 COMPOSITIONS 
               
            
           
           
               
               
               
               
               
               
               
               
               
            
               
                 Ingredients 
                 A 
                 B 
                 C 
                 D 
                 E 
                 F 
                 G 
                 H 
               
               
                   
               
            
           
           
               
               
               
               
               
               
               
               
               
            
               
                 Microbial 
                 5 
                 5 
                 10 
                 10 
                 25 
                 25 
                   
                   
               
               
                 Composition from 
               
               
                 Example 1 
               
               
                 
                   Bacillus subtilis 
                 
                   
                   
                   
                   
                   
                   
                 1 
                 10 
               
               
                 34KLB produced 
               
               
                 via submerged 
               
               
                 liquid fermentation 
               
               
                 according to 
               
               
                 Example 1 B 
               
               
                 Monohydrate 
                 95 
                   
                 90 
                   
                 75 
                   
                 99 
                 90 
               
               
                 Dextrose 
               
               
                 Nutri-Sure ™ 
                   
                 95 
                   
                 90 
                   
                 75 
               
               
                   
               
            
           
         
       
     
     Example 3: Denitrification of Swimming Pool Water 
     The composition of Example 2H was used to reduce the nitrate level in a swimming pool. 100 grams of the composition of Example 2H were added to the skimmer of a 15,000 gallon swimming pool with initial nitrate level of about 25 ppm. Significant denitrification was observed within the first 24 hours of dosing. See  FIG. 1 . 
     Example 4: Water Clarification 
     The conditions of a typical swimming pool (chlorine level, temperature) were mimicked in the laboratory using 10 gallon aquaria fitted with a filter and circulation pump. The composition of Example 2F was evaluated for its ability to clarify the water after addition of 250 ppm Sunscreen. Results are in  FIG. 2 . 
     Significant clarification is noted in as little as 24 hours. Separate respirometer analysis with sunscreen as a substrate showed significant CO2 generation and O2 consumption when the composition of Example 2F is added. 
     Example 5: Biodegradation of Cyanuric Acid 
     The composition of Example 2E was evaluated for its ability to degrade cyanuric acid. A solution of 1 gram of the composition of Example 2E in 1 L of Deionized Water was prepared and allowed to stand for 40 hours at room temperature. 5 ml of this solution were then added to 500 ml of water containing minimal media and 50 ppm cyanuric acid. The degradation of cyanuric acid was followed by HPLC. Results are shown in  FIG. 3 . 
     Example 6: Cyanuric Acid Control in Swimming Pools 
     The composition of Example 2E was evaluated in swimming pool applications. Testing was conducted in 6 fresh water swimming pools and 3 salt water pools in Southern California. 100 grams of the composition of Example 2E were added to each pool and the cyanuric acid level determined as a function of time using a commercially available cyanuric acid test kit. Results are summarized in Table 3: 
     
       
         
           
               
             
               
                 TABLE 3 
               
             
            
               
                   
               
               
                 Cyanuric Acid Control in Swimming Pools 
               
            
           
           
               
               
               
               
            
               
                   
                 Cyanuric Acid at 
                 Cyanuric Acid 
                   
               
               
                   
                 T = 0 
                 at 1 week 
                 % Reduction 
               
               
                   
                   
               
            
           
           
               
               
               
               
            
               
                 Fresh Water Pool 
                   
                   
                   
               
               
                 Pool #1 
                  100 ppm 
                 57.5 ppm   
                 42.5 
               
               
                 Pool #2 
                  100 ppm 
                 65 ppm 
                 35 
               
               
                 Pool #3 
                  50 ppm 
                 20 ppm 
                 60 
               
               
                 Pool #4 
                  100 ppm 
                 67.5 ppm   
                 32.5 
               
               
                 Pool #5 
                 &gt;125 ppm 
                 100 ppm  
                 &gt;20 
               
               
                 Pool #6 
                  100 ppm 
                 65 ppm 
                 35 
               
               
                 Salt Water Pool 
               
               
                 Pool #1 
                 &gt;100 ppm 
                 40 ppm 
                 &gt;60 
               
               
                 Pool #2 
                 &gt;200 ppm 
                 60 ppm 
                 &gt;70 
               
               
                 Pool #3 
                 &gt;500 ppm 
                 120 ppm  
                 &gt;75 
               
               
                   
               
            
           
         
       
     
     Example 7. Preparation of Cyanuric Acid Reducing Compositions 
     The following compositions were prepared (all percentages are by weight): 
     
       
         
           
               
               
               
               
               
               
               
             
               
                   
                 TABLE 4 
               
               
                   
                   
               
               
                   
                 Compo- 
                 Compo- 
                 Compo- 
                 Compo- 
                 Compo- 
                 Compo- 
               
               
                   
                 sition 
                 sition 
                 sition 
                 sition 
                 sition 
                 sition 
               
               
                   
                 A 
                 B 
                 C 
                 D 
                 E 
                 F 
               
               
                   
                   
               
             
            
               
                   
               
            
           
           
               
               
               
               
               
               
               
            
               
                 Dextrose 
                 100% 
                 94.30% 
                 95.0% 
                 97.0% 
                   
                 50% 
               
               
                 Maltodextrin 
                   
                   
                   
                   
                 94.0% 
               
               
                   Bacillus  Mix 
                   
                 0.43% 
                   
                 1.0% 
                 0.44% 
               
               
                 #1 
               
               
                   Bacillus  Mix 
                   
                 0.43% 
                   
                 1.0% 
                 0.44% 
               
               
                 #2 
               
               
                 
                   Lactobacillus 
                 
                   
                 4.40% 
                   
                   
                 4.40% 
               
               
                 Mix #1 
               
               
                 
                   B. Subtilis 
                 
                   
                 0.44% 
                 5.0% 
                 1.0% 
                 0.72% 
               
               
                 34KLB 
               
               
                 Mineral Mix 
                   
                   
                   
                   
                   
                 50% 
               
               
                   
               
            
           
         
       
     
     Where  Bacillus  Mix #1 comprises 10% by weight  Bacillus licheniformis,  30% by weight  Bacillus pumilus,  30% by weight  Bacillus amyloliquefaciens , and 30% by weight  Bacillus subtilis  subspecies  Mojavensis  and has an activity&gt;10 1  cfu/g;  Bacillus  Mix #2 comprises equal weights of  Bacillus licheniformis, Bacillus pumilus, Bacillus amyloliquefaciens , and  Bacillus subtilis  with an activity&gt;10 9  cfu/g; and,  Lactobacillus  Mix #1 comprises equal weights of  Pediococcus  acidilactici,  Pediococcus pentosaceus , and  Lactobacillus plantarum  at a concentration&gt;10 10  cfu/g. The  Bacillus subtilis  34KLB had an activity&gt;10 10  cfu/g. 
     The mineral mix comprises the following: 
     
       
         
           
               
               
               
             
               
                   
                 TABLE 5 
               
               
                   
                   
               
               
                   
                 Mineral 
                 Wt. % 
               
               
                   
                   
               
             
            
               
                   
               
            
           
           
               
               
               
            
               
                   
                 KH2PO4 
                 12% 
               
               
                   
                 K2HPO4 
                 31% 
               
               
                   
                 Na2HPO4*2H2O 
                 48% 
               
               
                   
                 CaCl2*2H2O 
                 5% 
               
               
                   
                 MgSO4*7H2O 
                 3% 
               
               
                   
                 FeCl3*6H2O 
                 1% 
               
               
                   
                   
               
            
           
         
       
     
     Example 8. In Vitro Cyanuric Acid Reduction 
     Compositions A and B from Example 7 were tested for their ability to degrade cyanuric acid in vitro. Stock solutions of Cyanuric acid were prepared by dissolving 100 mg cyanuric acid in 1 liter of hot autoclaved DI water. Compositions A and B were dosed at 1 gram/L into separate 100 mls aliquots of the stock cyanuric acid solutions then incubated in an incubating shaker at 30° C./150 rpm. 10 ml aliquots were pulled from each sample at times 0, 3, 6, 8, and 24 hours then frozen to shut down microbial activity. The frozen samples were analyzed by MS-MS. Results are shown in  FIG. 4 . 
     As expected, in sterile systems, addition of an oxidizable carbon source alone (Composition A) is not sufficient to cause reduction of cyanuric acid. However, in combination with select microbial species (Composition B), 65% of the initial cyanuric acid is removed after 24 hours incubation. 
     Example 9. In-Vivo Cyanuric Acid Reduction 
     Compositions A, B, and C from Example 7 were tested for their ability to reduce cyanuric acid in recreational swimming pools. For this analysis cyanuric acid levels were measured using a test kit common to the pool industry. The kit comprises a plastic tube into which a sample of pool water is added. A reagent solution comprising a low level of melamine is added to the pool water and the sample agitated for 1-2 minutes. Cyanuric acid levels are recorded visually using a dipstick calibrated between 20-100 ppm. 8 Ounces of the compositions from Example 7 were added into the skimmers of three separate pools. Results are shown below: 
     
       
         
           
               
               
               
             
               
                 TABLE 6 
               
               
                   
               
               
                 Pool #1 
                 Pool #2 
                 Pool #3 
               
               
                   
               
             
            
               
                 4.3 ppm Composition A 
                 3.7 ppm Composition B 
                 3.7 ppm Composition C 
               
               
                 Pool Capacity = 14,000 gal. 
                 Pool Capacity = 16,000 gal. 
                 Pool Capacity = 16,000 gal. 
               
               
                 82° F. 
                 80° F. 
                 85° F. 
               
               
                 pH: 7.8 
                 pH: 7.6 
                 pH: 7.6 
               
               
                 Initial CYA (cyanuric acid) 
                 Initial CYA level = 120 ppm 
                 Initial CYA level = 120 ppm 
               
               
                 level = +150 ppm 
               
               
                 CYA level at 25 hours = 55 ppm 
                 CYA level at 25 hours = 65 ppm 
                 CYA level at 25 hours = 75 ppm 
               
               
                 % CYA Reduction &gt; 63% 
                 % CYA Reduction &gt; 45% 
                 % CYA Reduction &gt; 37% 
               
               
                   
               
            
           
         
       
     
     The Compositions were further tested for their ability to reduce cyanuric acid in recreational swimming pools. Results are shown below: 
     
       
         
           
               
               
               
               
               
               
               
               
               
             
               
                 TABLE 7 
               
               
                   
               
               
                 POOL 
                 TYPE 
                 TEMPERATURE 
                 CHLORINE 
                 ALKALINITY 
                 PH 
                 CYA 
                 FILLER 
                 GALLONS 
               
               
                   
               
             
            
               
                   
               
            
           
           
               
               
               
               
               
               
               
               
               
            
               
                 1 
                 Salt water 
                 START: 55° 
                 START: 2.0 
                 START: 100 
                 START: 7.4 
                 START: 70 
                 DE 
                 20,000 
               
               
                   
                 Vinyl liner 
                 24 HR: 58° 
                 24 HR: 1.0 
                 24 HR: 90 
                 24 HR: 7.4 
                 3 HR: N/C 
               
               
                   
                   
                   
                   
                   
                   
                 24 HR: 50 
               
               
                 2 
                 Fresh water 
                 START: 55° 
                 START: 5 
                 START: 120 
                 START: 7.2 
                 START: 140-150 
                 SAND 
                 14,000 
               
               
                   
                 Vinyl liner 
                 24 HR: 59° 
                 24 HR: 3.0 
                 24 HR: 120 
                 24 HR: 7.4 
                 3 HR: 100-110 
               
               
                   
                   
                   
                   
                   
                   
                 24 HR: 80 
               
               
                 3 
                 Salt water 
                 START: 58° 
                 START: 3.0 
                 START: 90 
                 START: 7.2 
                 START: 75-80 
                   
                 20,000 
               
               
                   
                 Vinyl liner 
                 24 HR: 58° 
                 24 HR: 3.0 
                 24 HR: 90 
                 24 HR: 7.4 
                 24 HR: 45-50 
               
               
                   
                   
                 48 HR: 55° 
                 48 HR: 3.0 
                 48 HR: 90 
                 48 HR: 7.4 
                 DAY 5: 35-40 
               
               
                 6 
                 Fiber Glass 
                 START: 65° 
                 START: 3.0 
                 START: 100 
                 START: 7.6 
                 START: 200+ 
                 SAND 
                 6,500 
               
               
                   
                   
                 3 HR: 85° 
                 3 HR: 4.0 
                 3 HR: 120 
                 3 HR: 7.8 
                 3 HR: 100 
               
               
                   
                   
                 26 HR: 85° 
                 72 HR: 4 
                 72 HR: 100 
                 72 HR: 7.8 
                 22 HR: 80-90 
               
               
                   
                   
                 65 HR: 65° 
                   
                   
                   
                 26 HR: 70 
               
               
                   
                   
                   
                   
                   
                   
                 72 HR: 60-70 
               
               
                 7 
                 Fiber Glass 
                 START: 60° 
                 START: 2.0 
                 START: 80 
                 START: 7.4 
                 START: 200+ 
                 SAND 
                 5,000 
               
               
                   
                   
                 3 HR: 62° 
                 3 HR: 2.0 
                 2 HR: 80 
                 3 HR: 7.2 
                 3 HR: N/C 
               
               
                   
                   
                 24 HR: 58° 
                 24 HR: 2.0 
                 24 HR: 80 
                 24 HR: 7.4 
                 24 HR: 90 
               
               
                   
                   
                   
                   
                   
                   
                 48 HR: 70 
               
               
                 8 
                 Cement 
                 START: 58° 
                 START: 5 
                 START: 120 
                 START: 7.4 
                 START: 300+ 
                 SAND 
                 12,000 
               
               
                   
                   
                 24 HR: 58° 
                 24 HR: 4 
                 24 HR: 120 
                 24 HR: 7.4 
                 24 HR: 100-110 
               
               
                   
                   
                   
                 48 HR: 10 
                 48 HR: 100 
                 48 HR: 7.4 
                 48 HR: 80-90 
               
               
                 9 
                 Commercial 
                 START: 60° 
                 START: 1.0 
                 START: 120 
                 START: 7.8 
                 START: 180 
                 SAND 
                 108,000 
               
               
                   
                 Gunnite 
                 21 HR: 62° 
                 21 HR: 2.0 
                 21 HR: 120 
                 21 HR: 7.8 
                 21 HR: 100 
               
               
                   
                   
                 72 HR: 60° 
                 72 HR: 2 
                 72 HR: 120 
                 72 HR: 7 
                 72 HR: 60 
               
               
                   
               
            
           
         
       
     
     Example 10. In-Vivo Cyanuric Acid Reduction 
     Table 8 shows the results of cyanuric acid reduction using the compositions of the invention: 
     
       
         
           
               
               
               
               
               
               
             
               
                 TABLE 8 
               
               
                   
               
               
                   
                   
                   
                   
                   
                 Final 
               
               
                   
                   
                   
                   
                   
                 CYA 
               
               
                 Pool 
                 Location 
                 Pool size 
                   
                 Initial CYA 
                 Level 
               
               
                 Number 
                 (city) 
                 (gallons) 
                 dosage 
                 Level (PPM) 
                 (PPM) 
               
               
                   
               
             
            
               
                   
               
            
           
           
               
               
               
               
               
               
            
               
                 1 
                 Murrieta, CA 
                 10,000 
                 16 Oz. 
                 600 
                 300 
               
               
                 2 
                 San Diego, 
                 30,000 
                 16 Oz. 
                 110 
                 40 
               
               
                   
                 CA 
               
               
                 3 
                 Murrieta, CA 
                 25,000 
                 16 Oz. 
                 280 
                 100 
               
               
                 4 
                 Oceanside, 
                 20,000 
                  8 Oz. 
                 100 
                 30 
               
               
                   
                 CA 
               
               
                 5 
                 Fallbrook, 
                 35,000 
                 16 Oz. 
                 120 
                 60 
               
               
                   
                 CA 
               
               
                 6 
                 Carlsbad, 
                 30,000 
                 16 Oz. 
                 200 
                 110 
               
               
                   
                 CA 
               
               
                 7 
                 Temecula, 
                 18,000 
                 16 Oz. 
                 550 
                 200 
               
               
                   
                 CA 
               
               
                   
               
            
           
         
       
     
     Example 11. In-Vivo Cyanuric Acid Reduction 
     Tables 9-11 show the progression of cyanuric acid reduction. 
     
       
         
           
               
             
               
                 TABLE 9 
               
             
            
               
                   
               
               
                 Before treatment 
               
            
           
           
               
               
               
               
            
               
                   
                 Fluidra Test 
                 Fluidra Test 
                 Fluidra Test 
               
               
                   
                 Pool #1 
                 Pool #2 
                 Pool #3 
               
               
                   
                   
               
            
           
           
               
               
               
               
               
            
               
                   
                 Cl 
                 0.5 
                 4.5 
                 9 
               
               
                   
                 pH 
                 7.8 
                 6.8 
                 6.8 
               
               
                   
                 Alk 
                 80 
                 80 
                 90 
               
               
                   
                 Cyanuric Acid 
                 50 
                 120-140 
                 140 
               
               
                   
                 (CYA) 
               
               
                   
                 TDS 
                 1600 
                 500 
                 500 
               
               
                   
                 Temp 
                 75 
                 75 
                 70 
               
               
                   
                 Gallons 
                 5200 
                 51000 
                 16000 
               
               
                   
                 Copper 
                 0 
                 1 
                 0.6 
               
               
                   
                 BIO-CAR 
                 8 oz ES 
                 16 oz 
                 8 oz 
               
               
                   
                 ADDED 
               
               
                   
                   
               
            
           
         
       
     
     
       
         
           
               
             
               
                 TABLE 10 
               
             
            
               
                   
               
               
                 24 hours into treatment 
               
            
           
           
               
               
               
               
            
               
                   
                 Fluidra Test 
                 Fluidra Test 
                 Fluidra Test 
               
               
                   
                 Pool #1 
                 Pool #2 
                 Pool #3 
               
               
                   
                   
               
            
           
           
               
               
               
               
               
            
               
                   
                 Cl 
                 0 
                 5 
                 9 
               
               
                   
                 pH 
                 7.8 
                 6.6 
                 6.8 
               
               
                   
                 Alk 
                 80 
                 80 
                 90 
               
               
                   
                 Cyanuric Acid 
                 35-40 
                 90-100 
                 100 
               
               
                   
                 (CYA) 
               
               
                   
                 TDS 
                 1600 
                 500 
                 500 
               
               
                   
                 Temp 
                 75 
                 75 
                 72 
               
               
                   
                 Copper 
                 0 
                 1 
                 0.6 
               
               
                   
                 Gallons 
                 5200 
                 51000 
                 16000 
               
               
                   
                   
               
            
           
         
       
     
     
       
         
           
               
             
               
                 TABLE 11 
               
             
            
               
                   
               
               
                 48 hours into treatment 
               
            
           
           
               
               
               
               
            
               
                   
                 Fluidra Test 
                 Fluidra Test 
                 Fluidra Test 
               
               
                   
                 Pool #1 
                 Pool #2 
                 Pool #3 
               
               
                   
                   
               
            
           
           
               
               
               
               
               
            
               
                   
                 Cl 
                 0 
                 5 
                 9 
               
               
                   
                 pH 
                 7.6 
                 6.4 
                 6.4 
               
               
                   
                 Alk 
                 80 
                 80 
                 90 
               
               
                   
                 Cyanuric Acid 
                 30 
                 80-90 
                 90 
               
               
                   
                 (CYA) 
               
               
                   
                 TDS 
                 1600 
                 500 
                 500 
               
               
                   
                 Temp 
                 75 
                 75 
                 70 
               
               
                   
                 Copper 
                 0 
                 1 
                 0.6 
               
               
                   
                 Gallons 
                 5200 
                 51000 
                 16000 
               
               
                   
                   
               
            
           
         
       
     
     Other Embodiments 
     While the invention has been described in conjunction with the detailed description thereof, the foregoing description is intended to illustrate and not limit the scope of the invention, which is defined by the scope of the appended claims. Other aspects, advantages, and modifications are within the scope of the following claims.