the present invention relates to a water - dispersible particle for delivery of bioavailable nitrogen to a plant . the invention further relates to a method for making and using the water - dispersible particle . the inventive particle retains its size and shape during handling and application to a desired area and dissolves or crumbles into small particles upon contact with a water overspray within twelve hours . thus the durability of the particle allows delivery of the particle to the vicinity of the desired site of action whereupon contact with water sufficient to wet the particle surface causes dispersion of particle components , facilitating distribution of the active agents to the target . the term dispersion in the context of the present invention is intended to mean that an inventive particle disperses by breaking into numerous smaller pieces upon contact with water . in a preferred embodiment , an inventive particle disperses by breaking up into greater than 100 smaller pieces upon contact with water over a period of time ranging from 1 second to 24 hours . preferably , an inventive particle disperses into 1 , 000 to 10 , 000 smaller pieces over a period of time ranging from 1 second to 12 hours . even more preferably , a particle disperses into 100 to 10 , 000 smaller pieces over a period of 30 seconds to 6 hours . most preferably , a particle disperses as described over a period of 1 minute to 1 hour . the ability of the inventive material to degrade with water is generally measured in a water dispersibility test . the test involves placing about 10 grams of the inventive material into 100 ml of water at room temperature in a closed glass container . the container is then inverted and the time is observed until the material disperses . after every minute , the container is inverted . the inventive material of the present invention has a dispersibility time of generally less than 15 minutes with a period of less than 5 minutes being preferred and a period of less than 2 minutes being most preferred . the inventive particle provides a delivery system for controlled release nitrogen , and optional additional agents such as plant nutrients , pesticides , hormones , herbicides , micronutrients and other active ingredients . a particle of the present invention has a bioavailable nitrogen - containing ingredient and a binder component . the particle optionally contains an active ingredient . in a preferred embodiment the bioavailable nitrogen - containing ingredient is a source of nitrogen bioavailable to targeted desirable organisms illustratively including cultivated plants such as lawn grass , crops , flowers , shrubs , trees and bushes . the bioavailable nitrogen - containing ingredient is present in amounts ranging from 5 % to 99 . 9 % by weight of the total dry weight of the particle . more preferably , the bioavailable nitrogen - containing ingredient is present in amounts ranging from 30 % to 99 . 5 % by weight of the total dry weight of the particle . still more preferably , the bioavailable nitrogen - containing ingredient is present in amounts ranging from 50 % to 99 % by weight of the total dry weight of the particle . bioavailable nitrogen is nitrogen in a form that fills a nutritional requirement of a plant either directly , where the plant is capable of physiological processing of a nitrogen - containing ingredient , or indirectly , where another organism such as a bacterium must first act on the nitrogen - containing ingredient to produce a nitrogen form usable by the plant . illustrative examples of bioavailable nitrogen - containing ingredients include methylene urea oligomers , oxamide , urea formaldehyde - based compounds , dicyandiamide , crotilidiene diurea , nitrocellulose , metal ammonium phosphates , ammonium nitrate , ammonium sulfate , urea , coated urea , monoammonium phosphate , diammonium phosphate , calcium nitrate , isobutylidene diurea and other fertilizers as detailed herein . in a preferred embodiment , the bioavailable nitrogen - containing ingredient is a methylene urea oligomer or a mix of methylene urea oligomers as represented by the formula nh 2 conh ( ch 2 nhconh 2 ) n h , where n is an integer from 1 to 10 . illustrative examples of methylene urea oligomers include methylene diurea ( nh 2 conhch 2 nhconh 2 ), dimethylene triurea ( nh 2 conhch 2 nhconhch 2 nhconh 2 ), trimethylene tetraurea and tetramethylene pentaurea . particularly preferred is the mix of methylene urea oligomers such as the material commercially sold as nutralene ® by nu - gro technologies , canada , the material sold commercially as methex - 40 by homestead corporation and the material sold commercially as nitroform ®. a mix of methylene urea oligomers suitable for incorporation in the pellets of the present invention are methylene urea oligomer aggregates having a mean aggregate domain size less than 420 micrometers . in a preferred embodiment the particle contains a binder that produces or promotes cohesion of the methylene urea oligomer fines . the binder component is present in amounts ranging from 1 % to 95 % by weight of the total dry weight of the particle . more preferably , the binder component is present in amounts ranging from 1 % to 75 % by weight of the total dry weight of the particle . still more preferably , the binder component is present in amounts ranging from 1 % to 50 % by weight of the total dry weight of the particle . most preferably , the binder is present in amounts ranging from 1 % to 25 % by weight of the total dry weight of the particle . illustrative examples of binders operative herein are bentonite ; carbohydrates such as monosaccharides , disaccharides , oligosaccharides and polysaccharides ; proteins ; lipids ; glycolipid ; glycoprotein ; lipoprotein ; and combinations and derivatives of these . bentonite is an alkali metal ion containing montmorillonite clay that swells upon exposure to water . specific carbohydrate binders illustratively include glucose , mannose , fructose , galactose , sucrose , lactose , maltose , xylose , arabinose , trehalose and mixtures thereof such as corn syrup ; celluloses such as carboxymethylcellulose , ethylcellulose , hydroxyethylcellulose , hydroxy - methylethylcellulose , hydroxyethylpropylcellulose , methylhydroxyethyl - cellulose , methylcellulose ; starches such as amylose , seagel , starch acetates , starch hydroxyethyl ethers , ionic starches , long - chain alkyl starches , dextrins , amine starches , phosphates starches , and dialdehyde starches ; plant starches such as corn starch and potato starch ; other carbohydrates such as pectin , amylopectin , xylan , glycogen , agar , alginic acid , phycocolloids , chitin , gum arabic , guar gum , gum karaya , gum tragacanth and locust bean gum ; complex organic substances such as lignin and nitrolignin ; derivatives of lignin such as lignosulfonate salts illustratively including calcium lignosulfonate and sodium lignosulfonate and complex carbohydrate - based compositions containing organic and inorganic ingredients such as molasses . suitable protein binders illustratively include soy extract , zein , protamine , collagen , and casein . binders operative herein also include synthetic organic polymers capable of promoting or producing cohesion of methylene urea oligomer fines and these illustratively include ethylene oxide polymers , polyacrylamides , polyacrylates , polyvinyl pyrrolidone , polyethylene glycol , polyvinyl alcohol , polyvinylmethyl ether , polyvinyl acrylates , polylactic acid , and latex . in a preferred embodiment , the binder is bentonite . the particles of the present invention are optionally associated with an active ingredient . illustrative examples of active ingredients include fertilizers , soil nutrients , amendment materials , biological factors and biostimulants . a solid , liquid or powder active ingredient is recognized to be operative herein . it will be recognized by those skilled in the art that more than one active ingredient may be incorporated into the particle and that the choice of active ingredient or combination of active ingredients will depend on the intended purpose of the particle and the chemical compatibility of the ingredients and other particle components . in a preferred embodiment , where the active ingredient is a fertilizer , soil nutrient or amendment material , the fertilizer , soil nutrient or amendment material active ingredient is present in an amount ranging from 0 . 05 % to 50 % by weight of the total dry weight of the particle . in a more preferred embodiment , the fertilizer , soil nutrient or amendment material active ingredient is present in an amount ranging from 0 . 1 % to 30 % by weight of the total dry weight of the particle . in a still more preferred embodiment , the fertilizer , soil nutrient or amendment material active ingredient is present in an amount ranging from 0 . 5 % to 10 % by weight of the total dry weight of the particle . where the active ingredient is a biological factor or biostimulant , the active ingredient is present in an amount ranging from 0 . 05 % to 10 % by weight of the total dry weight of the particle . in a more preferred embodiment , the biological factor or biostimulant active ingredient is present in an amount ranging from 0 . 1 % to 5 % by weight of the total dry weight of the particle . in a still more preferred embodiment , the biological factor or biostimulant active ingredient is present in an amount ranging from 0 . 25 % to 1 % by weight of the total dry weight of the particle . fertilizers are substances containing one of the plant nutrients nitrogen , phosphate or potassium and illustratively include urea , sulfur - coated urea , isobutylidene diurea , ammonium nitrate , ammonium sulfate , ammonium phosphate , triple super phosphate , phosphoric acid , potassium sulphate , potassium nitrate , potassium metaphosphate , potassium chloride , dipotassium carbonate , potassium oxide and a combination of these . soil nutrients illustratively include calcium , magnesium , sulfur , iron , manganese , copper , zinc ; oxides thereof , salts thereof and combinations thereof . amendment materials are natural organic products such as humic acid , blood meal , bone meal , seed meal , feather meal and soy meal ; meat meal ; animal waste from various animal sources ; activated sludge , hydrolyzed animal hair ; fish byproducts ; chitin ; composts ; and a combination thereof . biological factors are those factors that have a deleterious effect on a biological organism and illustratively include algicides , bacteriocides , defoliants , desiccants , fungicides , herbicides , insecticides , insect growth regulators , miticides , nematicides , ovicides , pesticides , pheromones , repellents , rodenticides and a combination thereof . biostimulants are substances that promote plant survival and health and illustratively include plant growth hormones and plant growth regulators such as cytokinins , auxins , gibberellins , ethylene , absisic acid and a combination of these . in a preferred embodiment , methylene urea oligomer fines are mechanically aggregated into pellets in a pan granulator in the presence of a binder . methylene urea oligomer fines are very small methylene urea oligomer aggregates that have a mean aggregate domain size that is less than 500 micrometers . more preferably , the mean aggregate domain size of the fines is less than 250 micrometers . still more preferably , the mean aggregate domain size of the fines is less than 180 micrometers . the binder solution or slurry is sprayed into the pan granulator with the methylene urea oligomer fines . the pellets are dried and the resulting particles are size screened and particles of desired size are stored . optionally , the particles are transferred to a coating drum for addition of an active ingredient or a conditioner material . in another embodiment , methylene urea oligomer fines are mechanically aggregated into pellets in a drum granulator in the presence of a binder . methylene urea oligomer fines are very small methylene urea oligomer aggregates that have a mean aggregate domain size that is less than 500 micrometers . more preferably , the mean aggregate domain size of the fines is less than 250 micrometers . still more preferably , the mean aggregate domain size of the fines is less than 180 micrometers . the binder is sprayed into the drum granulator with the methylene urea oligomer fines . the pellets are dried and the resulting particles are size screened and particles of desired size are stored . optionally , the particles are transferred to a coating drum for addition of an active ingredient or a conditioner material . in another embodiment , methylene urea oligomer fines are mechanically aggregated into pellets in an eirich unit in the presence of a binder . methylene urea oligomer fines are very small methylene urea oligomer aggregates that have a mean aggregate domain size that is less than 500 micrometers . more preferably , the mean aggregate domain size of the fines is less than 250 micrometers . still more preferably , the mean aggregate domain size of the fines is less than 180 micrometers . the binder solution or slurry is sprayed into the eirich unit granulator with the methylene urea oligomer fines . the pellets are dried and the resulting particles are size screened and particles of desired size are stored . optionally , the particles are transferred to a coating drum for addition of an active ingredient or a conditioner material . various means of drying the material are available . a preferred method is fluid bed drying . the material is placed in a fluid bed drier and the drier inlet air temperature ranges from about 120 ° f . to about 220 ° f . more preferably , the temperature ranges from 140 ° f . to 190 ° f . further methods of drying particles will be apparent to one of skill in the art and illustratively include use of a rotary drum dryer and drying under vacuum conditions . an active ingredient is associated with a particle during the process of particle formation or after particles are formed . for example , an active ingredient is mixed with the binder . the binder / active ingredient mixture is added to methylene urea oligomer fines and mechanically aggregated in a pan granulator resulting in particles wherein the active ingredient and methylene urea oligomers are in suspension in the binder . where it is desirable to add the active ingredient after particle formation , for example where the active ingredient is incompatible with suspension in the binder , the active ingredient is added to the particle following particle formation in the presence or absence of an adhesive . methods of active ingredient addition illustratively include spraying onto the particle or adsorption of the active ingredient by coating the particle in a non - aqueous solution of the active ingredient . in another embodiment , the active ingredient is mixed with an adhesive before application to a particle . an adhesive is a substance that binds to a particle , such that the active ingredient adheres to the particle in suspension in the adhesive . the adhesive may be the same as the binder or different . the choice of adhesive depends on the particle components and will be evident to one skilled in the art . examples of adhesives include , but are not limited to , substances listed herein as binder components . preferably , the adhesive is bentonite . for example , the active ingredient in powdered form is adhered to the outside surface of the particle with the use of an adhesive . an adhesive liquid may be used and is applied before or after the addition of the powdered active ingredient or it may be applied at the same time as the active ingredient . the choice of adhesive depends on the particle components and will be evident to one skilled in the art . examples of a liquid adhesive include but are not limited to binders listed herein , including mineral oils or polymer liquids such as polybutene . the particles of the present invention have a minimum resistance to attrition ( rta ) rating ranging from 60 % to 100 % as determined by the method detailed in example r or an art - recognized equivalent procedure . the particles of the present invention have a mean particle domain size that ranges from 0 . 1 millimeter to 30 millimeters . more preferably , the mean particle domain size ranges from 0 . 25 millimeter to 20 millimeters . still more preferably , the mean particle domain size ranges from 0 . 50 millimeter to 15 millimeters . the particles formed by the process of the present invention have a uniformity index rating in the range of 30 to 60 where the uniformity index rating is calculated as the 10 th percentile particle size expressed as a percentage of the 95 th percentile particle size . particles of the present invention take any shape illustratively including spheres , cylinders , ellipses , rods , cones , discs , needles and irregular . in a preferred embodiment the particles are approximately spherical . the particles of the present invention are administered to a target to produce a desired effect on a desirable or an undesirable organism . particles are administered by a method which delivers the nitrogen - containing ingredient to the vicinity of a desirable organism whose health is to be encouraged . further , the particles are administered by a method which delivers the active ingredient to an area where it will be available to a targeted desirable or undesirable organism . for example , where a particle contains a controlled release nitrogen source such as methylene urea oligomers and an active ingredient such as a plant hormone , the particles are delivered to a desirable plant target , such as a golf course lawn , by broadcast scattering via rotary spreader . the particles are then dispersed by water which is user applied or natural such as rain , dew or atmospheric humidity . alternatively , the particles are placed in a limited target area such as near a particular desired plant in a garden or in a crop row . in another embodiment , the particles are placed under the soil surface . a target desirable organism illustratively includes cultivated plants such as lawn grass , crops , flowers , shrubs , trees and bushes . target undesirable organisms illustratively include pest insects at any stage of development , bacteria , molds , algaes , weeds , worms and rodents . dispersible methylene urea : using a pan agglomeration disk , a binder such as calcium lignosulfanate , corn starch , and corn syrup is applied to a mixture of methylene urea fines ( material less than 250 microns ). the agglomeration disk is operated and adjusted to generate the desired size distribution of particles before the particles are conveyed to a fluid bed drier where the material is dried at a temperature of 140 ° f . to a moisture content of less than 0 . 5 %. the material is then separated into various size categories using conventional gyroscopic screeners . general size of these product streams are as follows : 3 , 360 microns and larger , from 3 , 360 microns to 1 , 191 microns , from 1 , 191 microns to 594 microns , and material smaller than 594 microns . the range of sizing for each product stream can be varied to separate the desired material from the mixture of sizing . dispersible methylene urea containing pesticides ( powdered pesticides ): a mixture of methylene urea fines and a powdered pesticide ( such as pcnb , prodiamine , or thiphanate - methyl ) is added to a pan agglomeration disk . a binder such as calcium lignosulfanate , corn starch , or corn syrup is sprayed onto the mixture . the pan agglomeration disk is operated and adjusted to provide the desired size distribution of particles . the material is then conveyed to a fluid bed drier where the material is dried at a temperature of 140 ° f . to a moisture content of less than 0 . 5 %. the material is then separated into various size categories using conventional gyroscopic screeners . general size of these product streams are as follows : 3 , 360 microns and larger , from 3 , 360 microns to 1 , 191 microns , from 1 , 191 microns to 594 microns , and material smaller than 594 microns . the range of sizing for each product stream can be varied to separate the desired material from the mixture of sizing . dispersible methylene urea containing pesticides such as liquid pesticides : using a pan agglomeration disk , a liquid pesticide and a binder such as calcium lignosulfanate , corn starch , and corn syrup were applied to a mixture of methylene urea fines ( material less than 250 microns ). the agglomeration disk is operated and adjusted to generate the desired size distribution of particles before the particles are conveyed to a fluid bed drier where the material was dried at a temperature of 140 ° f . to a moisture content of less that 0 . 5 %. the material is then separated into various size categories using conventional gyroscopic screeners . general size of these product streams are as follows : 3 , 360 microns and larger , from 3 , 360 microns to 1 , 191 microns , from 1 , 191 microns to 594 microns , and material smaller than 594 microns . the range of sizing for each product stream can be varied to separate the desired material from the mixture of sizing . dispersible methylene urea with other nutrient sources , micronutrients , soil amendments , or biostimulants : using a pan agglomeration disk , a binder such as calcium lignosulfanate , corn starch , and corn syrup is applied to a mixture of methylene urea fines , other nutrient sources ( diammonium phosphate or sulfate of potash for example ), micronutrients ( such as iron sulfate or manganese oxide ), soil amendments ( such as humic acid materials ), or biostimulants with all materials less than 250 microns in size . the agglomeration disk is operated and adjusted to generate the desired size distribution of particles before the larger particles were conveyed to a fluid bed drier where the material was dried at a temperature of 140 ° f . to a moisture content of less that 0 . 5 %. the material is then separated into various size categories using conventional gyroscopic screeners . general size of these product streams are as follows : 3 , 360 microns and larger , from 3 , 360 microns to 1 , 191 microns , from 1 , 191 microns to 594 microns , and material smaller than 594 microns . the range of sizing for each product stream can be varied to separate the desired material from the mixture of sizing . dispersible methylene urea with other nutrient sources , micronutrients , soil amendments , or biostimulants containing pesticides such as powdered pesticides : a mixture of methylene urea fines , other nutrient sources ( diammonium phosphate and sulfate of potash for example ), micronutrients ( such as iron sulfate or manganese oxide ), soil amendments ( such as humic acid materials ), or biostimulants and a powdered pesticide ( such as pcnb , prodiamine , or thiphanate - methyl ) is added to a pan agglomeration disk . a binder such as calcium lignosulfanate , corn starch , and corn syrup , is sprayed onto the mixture . the pan agglomeration disk is operated and adjusted to provide the desired size distribution of particles . the material is then conveyed to a fluid bed drier where the material is dried at a temperature of 140 ° f . to a moisture content of less than 0 . 5 %. the material is then separated into various size categories using conventional gyroscopic screeners . general size of these product streams were as follows : 3 , 360 microns and larger , from 3 , 360 microns to 1 , 191 microns , from 1 , 191 microns to 594 microns , and material smaller than 594 microns . the range of sizing for each product stream can be varied to separate the desired material from the mixture of sizing . dispersible methylene urea with other nutrient sources , micronutrients , soil amendments , or biostimulants containing pesticides such as liquid pesticides : using a pan agglomeration disk , a liquid pesticide and a binder such as calcium lignosulfanate , corn starch , and corn syrup are applied to a mixture of methylene urea fines , other nutrient sources ( diammonium phosphate and sulfate of potash for example ), micronutrients ( such as iron sulfate or manganese oxide ), soil amendments ( such as humic acid materials ), or biostimulants , with all material less than 250 microns in diameter . the agglomeration disk is operated and adjusted to generate the desired size distribution of particles before the particles are conveyed to a fluid bed drier where the material was dried at a temperature of 140 ° f . to a moisture content of less that 0 . 5 %. the material is then separated into various size categories using conventional gyroscopic screeners . general size of these product streams were as follows : 3 , 360 microns and larger , from 3 , 360 microns to 1 , 191 microns , from 1 , 191 microns to 594 microns , and material smaller than 594 microns . the range of sizing for each product stream can be varied to separate the desired material from the mixture of sizing . post production surface coating of dispersible methylene urea ( example a ) or dispersible methylene urea containing other nutrient sources , micronutrients , soil amendments , or biostimulants ( example d ) with a powdered pesticide : materials generated by the methods described in example a or example d above are fed to a blender ( such as a forberg fluidized zone blender ) or other coating equipment ( such as a coating drum ). the material is sprayed with a liquid , such as a lightweight mineral oil , to make the surface slightly tacky before adding a powdered pesticide ( such as prodiamine , thiophanate - methyl , or pcnb ). a second spray of liquid may be necessary to adhere the powder to the surface of the material . post production surface impregnation of dispersible methylene urea ( example a ) or dispersible methylene urea containing other nutrient sources , micronutrients , soil amendments , or biostimulants ( example d ) with a liquid pesticide : materials generated by the methods described in example a or example d above are fed to a blender ( such as a forberg fluidized zone blender ) or other coating equipment ( such as a coating drum ). the material is then sprayed with a liquid pesticide that slightly penetrates the surface of the material . the material is mixed to assure even distribution of the pesticide to all particles . methylene urea dispersible ( mud ) particles are generated in an exemplary method , using an 18 ″ agglomeration pan and a fluid bed drier . an illustrative procedure for producing a small batch of mud particles : 1 . 500 to 1000 grams of methylene urea fines passing 50 mesh are weighed out . 2 . the ratio of methylene urea fines to binder material depends on the binder and varies from about 19 : 1 to about 1 : 3 . preferably the ratio of methylene urea fines to binder is in the range from 10 : 1 to 1 : 1 . more preferably the ratio of methylene urea fines to binder is in the range from 7 : 1 to 2 : 1 . 3 . approximately ⅔ of this material is placed into the 18 ″ agglomeration pan and the speed of rotation and the slope of incline of the pan are adjusted to ensure an acceptable falling curtain of material in the pan bed . 4 . a binder is applied via a spray bottle , peristaltic pump with air atomizing nozzle , or sparge tube depending on the material used . binder is added by the operator until particle growth begins to occur . 5 . as necessary , the size of the particles is adjusted by the operator by crushing the material back down by hand as the material is rotating within the pan . 6 . the additional ⅓ of the methylene urea fines is added in small amounts to the pan along with additional binder as needed 7 . after all of the methylene urea is added to the pan and any binder required to grow the particles is applied , the material is discharged into a collection container and transported to a fluid bed drier . 8 . the material is placed in a fluid bed drier to drive off moisture added by the binder material . the temperature of the air entering the drier varies depending on the materials included in the mud particles . 9 . the material is dried until the temperature of the air exiting the dryer stabilizes for a period of five minutes . 10 . once the material is taken from the drier , it is split into size fractions using round sieve screens by hand . for example , four fractions are used including : 11 . the size fractions are placed into an oven and dried for additional period . for example , the particles are placed at a temperature ranging from 70 ° f . to 150 ° f . for 1 hour to 48 hours . more preferably the temperature ranges from 90 ° f . to 120 ° f . for 1 hour to 48 hours . in a specific example , the particles are dried at 110 ° f . for an additional 16 + hours . 12 . when pulled from the oven , the size fractions are checked for dispersibility and resistance to attrition . an example procedure for making mud particles using norlig a - lignin as a binder is as follows : 500 g methylene urea fines , − 50 mesh , are combined with 118 . 8 g of norlig a / water mixture ( 10 : 1 ) using a peristaltic pump / air atomizing nozzle . drier inlet air is used at 190 ° f . final drier exiting air has a temperature of 164 ° f . assay of dispersibility of particles is acceptable and resistance to attrition is 95 . 6 %. an example procedure for making mud particles using cerestar corn starch as a binder is as follows : 500 g methylene urea fines , − 50 mesh are combined with 158 . 3 g of cerestar corn starch using a peristaltic pump / air atomizing nozzle . drier inlet air is used at 140 ° f . final drier exiting air has a temperature of 117 ° f . assay of dispersibility of particles is acceptable and resistance to attrition is 94 . 8 %. an example procedure for making mud particles using corn syrup as a binder is as follows : 500 g methylene urea fines , − 50 mesh , are combined with 157 . 4 g of corn syrup / water ( 5 : 1 ) using a peristaltic pump / air atomizing nozzle . drier inlet air is used at 140 ° f . final drier exiting air has a temperature of 117 ° f . assay of dispersibility of particles is acceptable and resistance to attrition is 96 . 1 %. an example procedure for making mud particles using norlig a - lignin as a binder is as follows : 1000 g methylene urea fines , − 50 mesh , are combined with 240 g of norlig a / water mixture ( 10 : 1 ) using a peristaltic pump / air atomizing nozzle . drier inlet air is used at 190 ° f . final drier exiting air has a temperature of 164 ° f . assay of dispersibility of particles is acceptable and resistance to attrition is 94 . 5 %. an example procedure for making mud particles using cerestar corn starch as a binder is as follows : 1000 g methylene urea fines , − 50 mesh are combined with 316 . 4 g of cerestar corn starch using a peristaltic pump / air atomizing nozzle . drier inlet air is used at 140 ° f . final drier exiting air has a temperature of 117 ° f . assay of dispersibility of particles is acceptable and resistance to attrition is 95 . 6 %. an example procedure for making mud particles using corn syrup as a binder is as follows : 1000 g methylene urea fines , − 50 mesh , are combined with 315 . 5 g of corn syrup / water ( 5 : 1 ) using a peristaltic pump / air atomizing nozzle . drier inlet air is used at 140 ° f . final drier exiting air has a temperature of 117 ° f . assay of dispersibility of particles is acceptable and resistance to attrition is 96 . 2 %. an example procedure for making mud particles using corn syrup with dye as a binder is as follows : 1000 g methylene urea fines , − 50 mesh , are combined with 314 . 0 g of corn syrup / water ( 5 : 1 ) using a peristaltic pump / air atomizing nozzle . drier inlet air is used at 140 ° f . final drier exiting air has a temperature of 117 ° f . assay of dispersibility of particles is acceptable and resistance to attrition is 94 . 9 %. an example procedure for making mud particles coated with a powdered active ingredient is as follows : mud particles are generated as outlined in example i . when dry , 1000 grams of the selected size fraction of finished particles are placed in a blender . 40 grams of the powdered active ingredient is added to the blender , which is then turned on . after 30 seconds of blending , the adhesive liquid is added to the blender . a total of 20 grams of adhesive liquid is added over 1 minute , which is followed by an additional 1 minute of blending . the material is then discharged from the blender . an example procedure for making mud particles using bentonite as a binder is as follows : 500 g methylene urea fines , − 50 mesh , are combined with 200 g of bentonite / water mixture ( 10 : 1 ) using a peristaltic pump / air atomizing nozzle . drier inlet air is used at 190 ° f . final drier exiting air has a temperature of 164 ° f . assay of dispersibility of particles is acceptable and resistance to attrition is 93 %. example b is repeated with the substitution of bentonite slurry as the binder that is sprayed onto the mixture , with comparable results being obtained . apparatus : ro - tap sieve shaker with 8 - inch sieves , balance with 0 . 1 g sensitivity , 10 - min timer , and 10 steel balls with smooth surfaces and 16 mm ( ⅝ in .) in diameter . 1 . using information from the screen analysis , choose your limiting screen size . the following table indicates the limiting screen for several fertilizer blends . fertilizer sizing u . s . ( tyler ) coarse 16 ( 14 ) premium standard 20 ( 20 ) fairways 20 ( 20 ) greens 30 ( 28 ) 2 . place about 75 g of a representative sample onto the limiting screen . 4 . place the screen apparatus onto the shaker and run it for 10 min ( use the hammer ). 6 . put ten ( 10 ) 16 - mm steel balls in the pan with the sample . 7 . reassemble the screen apparatus and place it onto the shaker and run it for 10 min ( do not use the hammer ). 8 . remove the steel balls from the pan and transfer the sample back into the limiting screen . 9 . place the screen apparatus back onto the shaker and run it for 10 min ( use the hammer ). 10 . weigh out the amount that remained on the limiting screen to the nearest 0 . 1 g and compare it to the original amount . percent resistance to attrition ={( 100 · a )/ b }, where a is the weight of the fraction that remained on the limiting screen in step 10 and b is total weight of the sample in step 5 . any patents or publications mentioned in this specification are indicative of the level of those skilled in the art to which the invention pertains . these patents and publications are herein incorporated by reference to the same extent as if each individual publication was specifically and individually indicated to be incorporated by reference . one skilled in the art will readily appreciate that the present invention is well adapted to carry out the objects and obtain the ends and advantages mentioned , as well as those inherent therein . the present methods , procedures , treatments , molecules , and specific compounds described herein are presently representative of preferred embodiments , are exemplary , and are not intended as limitations on the scope of the invention . changes therein and other uses will occur to those skilled in the art which are encompassed within the spirit of the invention as defined by the scope of the claims .
water - dispersible particles are provided that disperse into more than 100 pieces upon contact with water . particles include from 5 % to 99 . 9 % of a nitrogen - containing ingredient bioavailable to a targeted desirable organism and 1 % to 95 % of a bentonite binder component . additionally provided is a process for making a water - dispersible particle , the process including the steps of mechanically aggregating particle components into a pellet . particle components include a bioavailable nitrogen - containing ingredient and a binder , the components being such that a product particle is dispersed into more than 100 pieces upon contact with water . in a further step of a process for making a water - dispersible particle , the pellet is dried to form a particle . following administration of a described particle , water is allowed to contact the particle , dispersing it into pieces and thereby delivering a nutrient .