an adsorption medium having increased metal loading and increased capacity is produced . the adsorption medium 2 includes a matrix 4 and at least one active component 6 , as shown in fig1 . the at least one active component 6 may permeate into pores of the matrix 4 and absorb to the matrix 4 . the at least one active component 6 is synthesized during formation of the adsorption medium 2 , allowing for increased loading of the at least one active component 6 . the adsorption medium 2 may be used to remove at least one constituent from a feed stream . the feed stream may be , for example , a drinking water source or an industrial water stream having at least one constituent that is to be removed . the drinking water source may include groundwater , surface water , well water , or other drinking water sources . the industrial water stream may be a process solution or a waste stream generated by an industrial process , such as a stream generated by the mining , agriculture , semiconductor , or petroleum industry . the at least one constituent to be removed may be an undesirable component of the feed stream , such as a component that produces health risks when ingested by humans or other mammals . for sake of example only , the at least one constituent may include , but is not limited to , arsenic , selenium , or antimony compounds . the matrix 4 may be an inert substrate , such as pan . as used herein , the term “ pan ” refers to an acrylonitrile homopolymer or a copolymer containing at least about 40 % acrylonitrile units . for instance , the pan may be an acrylonitrile polymer or a copolymer having a ratio of at least about 40 % acrylonitrile molecules to total molecules . pan may be provided in a solid form . the acrylonitrile homopolymer may include crystalline , quasicrystalline , and / or amorphous phases . the matrix 4 may be constituted to enable formation thereof into a plurality of small , slightly porous , particles , which are also referred to herein as beads . pan is an organic polymer that is easily formed into spherical beads having a high surface area . however , additional organic and inorganic polymers having these properties , such as polystyrene , may also be used as the matrix 4 , provided that the polymer is soluble in a solvent used to produce the adsorption medium 2 and is compatible with the at least one active component 6 . an active component 6 may be selected for its ability to remove the constituent from the feed stream . for sake of example only , the active component 6 may be a metal hydroxide or a metal oxide that is incorporated , or physically trapped , in the matrix 4 . the active component 6 may be a hydroxide or an oxide of a divalent , trivalent , or tetravalent metal , such as a hydroxide or an oxide of a transition metal , a lanthanide or rare earth metal , a group iii metal , a group iv metal , or a group v metal . for instance , the active component 6 may be a hydroxide or an oxide of iron , zirconium , lanthanum , cerium , titanium , aluminum , tin , silver , zinc , mercury , bismuth , copper , antimony , tungsten , molybdenum . the active component 6 may also include mixtures of metal hydroxides or mixtures of metal oxides that are incorporated in the matrix 4 . for sake of example only , a mixture of ferric hydroxide , lanthanum hydroxide , and titanium hydroxide may be present in the matrix 4 . by utilizing the mixture of metal hydroxides or mixtures of metal oxides , the adsorption medium 2 may be tailored to remove specific oxidation states of arsenic , selenium , or antimony , depending on which constituents are present in the feed stream . for sake of example only , one metal mixture may be more specific to remove as ( iii ) compounds , while a second metal mixture may have increased specificity for as ( v ) compounds . the metal mixture may also be tailored to selectively remove constituents in the presence of other potentially competing anions , such as phosphates or nitrates . to produce the adsorption medium 2 having a metal hydroxide as the active component 6 , at least one metal compound may be dissolved in a solvent to form a metal solution . the metal compound may be a metal salt , a metal oxide , or mixtures thereof . for instance , the metal compound may be a salt or an oxide of a divalent , trivalent , or tetravalent metal , such as a salt or an oxide of a transition metal , a lanthanide or rare earth metal , a group iii metal , a group iv metal , or a group v metal . the metal in the metal compound may include , but is not limited to , a cation of iron , zirconium , lanthanum , cerium , titanium , aluminum , tin , silver , zinc , mercury , bismuth , copper , antimony , tungsten , or molybdenum . the metal salt may include , but is not limited to , a chloride , an oxychloride , a sulfate , a nitrate , or an acetate of the metal cation . the metal oxide may be an oxide or a hydroxide of the metal . in one embodiment , the metal cation is iron ( iii ), which is provided as an iron salt or as iron oxide ( fe 3 o 4 or fe 2 o 3 ). the solvent used to dissolve the metal compound may be a mineral or inorganic acid or an organic solvent in which both the metal compound and the pan are soluble . in one embodiment , the solvent is concentrated nitric acid ( hno 3 ). other solvents include , but are not limited to , aprotic polar organic solvents , such as dimethylformamide , dimethylacetamide , dimethylsulfoxide ( dmso ), sulfolane , ethylene carbonate , and n - methylpyrrolidone ; acids , such as concentrated sulfuric acid ; and concentrated aqueous solutions of certain inorganic salts , such as lithium bromide , sodium thiocyanate , and zinc chloride . to achieve a maximum concentration of the metal hydroxide in the adsorption medium 2 , the metal compound may be dissolved in the metal solution in an amount sufficient to provide maximum solubility . in other words , a saturated solution of the metal compound in the solvent may be produced . for sake of example only , if the metal hydroxide on the adsorption medium 2 is ferric hydroxide ( feo ( oh )), approximately 70 g / l of iron ( as a salt or oxide of iron , such as iron oxide ( fe 3 o 4 )), may be dissolved in the solvent . if a maximum concentration of the metal hydroxide is not desired in the adsorption medium 2 , the amount of the metal compound in the metal solution may be decreased from the maximum solubility to provide a desired concentration . the pan may be dissolved in the metal solution to form a pan - metal solution . the pan may be dissolved in the metal solution from approximately 3 % by weight (“ wt %”) to approximately 5 wt %. as previously described , pan is an inert substrate that is readily formed into spherical beads and provides a high surface area adsorption medium 2 in combination with the metal hydroxide . however , additional polymers having these properties may be used as the matrix 4 , as long as the polymer is soluble in the solvent used in the metal solution . the polymer may also be compatible with the metal compound used in the metal solution . the pan may be added to the metal solution with slight agitation and heating to dissolve the pan . various techniques may be used to produce the adsorption medium 2 from the pan - metal solution . solid beads of the adsorption medium 2 may be formed by spraying the pan - metal solution through an air / nozzle device into a quenching bath . the air / nozzle device may be a conventional spray nozzle that is adjusted to form droplets of a desired size . the droplets solidify into beads when they contact the quenching bath . the air / nozzle device may also utilize air to accelerate formation or release of the droplets . the quenching bath also causes metal hydroxide to precipitate from the pan - metal solution and become incorporated into the pan . the quenching bath may be an aqueous , alkaline solution that includes an alkaline agent , such as sodium hydroxide or potassium hydroxide . the concentration of the alkaline agent in the alkaline solution may range from approximately 0 . 1 m to approximately 8 m . desirably , the concentration of the alkaline agent ranges from approximately 0 . 5 m to approximately 6 m . more desirably , the concentration of the alkaline agent is approximately 1 m . the quenching bath may be constantly stirred while the pan - metal solution is sprayed into it . the alkaline agent in the quenching bath may cause the metal compound in the droplets of the pan - metal solution to dissociate into a metal cation and an anion . upon contact with the quenching bath , the metal cation reacts with the alkaline solution to form the metal hydroxide , which is water - insoluble . simultaneously , the pan in the droplets becomes insoluble in the alkaline solution , forming solid beads that have the metal hydroxide incorporated into the pan . the metal hydroxide may be homogenously dispersed within the pan . the quenching bath is used to dilute , remove , or neutralize the solvent in the droplets , causing the pan to become insoluble and solidify . since the metal hydroxide is produced from the metal oxide or metal salt during the formation of the adsorption medium 2 , the adsorption medium 2 may have an increased metal loading compared to the metal loading in conventional ion exchange resins . the metal loading of the adsorption medium 2 may be up to approximately seventy times the metal loading achieved with conventional ion exchange resins . in one embodiment where ferric hydroxide is the active component 6 , the metal loading of the adsorption medium 2 ranges from approximately 250 mg of iron per gram of the adsorption medium 2 to approximately 300 mg of iron per gram of the adsorption medium 2 . with the increased loading , the solid beads may have an increased capacity for the constituents compared to the capacity of conventional ion exchange resins . the solid beads may include from approximately 10 wt % to approximately 85 wt % of the metal in the form of an elemental metal and / or the metal hydroxide . the solid beads having the metal hydroxide incorporated into the pan are removed from the quenching bath , rinsed , dried , and screened to obtain a desired size fraction of the solid beads . the solid beads may have the metal hydroxide incorporated into , or physically trapped in , the matrix 4 . in one embodiment , the solid beads may include at least approximately 50 wt % of the metal in the form of the elemental metal and / or the metal hydroxide , such as approximately 85 wt %. for sake of example only , if iron oxide is used as the metal compound , the resulting solid beads may include at least 50 wt % iron in the form of fe ( iii ) and / or feo ( oh ). the remainder of the solid beads may include pan . for instance , the solid beads may include from approximately 15 wt % to approximately 90 wt % of the pan . if the solid beads include a mixture of metals , the pan may be present from approximately 15 wt % to approximately 20 wt %. the remainder of the solid beads may include from approximately 80 wt % to approximately 85 wt % of the metal in the form of an elemental metal and / or the metal hydroxide . in one embodiment , the solid beads include approximately 25 wt % to approximately 30 wt % of fe ( iii ), which equates to approximately 40 wt % to approximately 50 wt % as feo ( oh ), and approximately 40 wt % to approximately 50 wt % pan . a rate at which the metal hydroxide precipitates from the pan - metal solution may affect the shape and metal loading of the solid beads that are formed . the precipitation rate of the metal hydroxide may be adjusted by adjusting the concentration of the alkaline agent in the alkaline solution . if the concentration of the alkaline agent is high , the metal hydroxide may precipitate quickly and the solid beads may not be sufficiently spherical . however , loading of the metal hydroxide on the solid beads may be increased . in contrast , if the concentration of the alkaline agent is low , the metal hydroxide precipitates slowly and forms spherical , solid beads . however , these solid beads may have a decreased loading of the metal hydroxide . alternatively , the adsorption medium 2 may be impregnated onto a support , such as a filter , disc , or membrane . the support may be a fibrous material , such as a glass wool fiber . a pressure differential , such as a vacuum , may be applied on one side of the filter . the pan - metal solution may be applied to the high pressure side of the pressure differential . the pressure differential causes the pan - metal solution to flow into , and impregnate , the filter . the impregnated filter may be immersed in a water bath to dilute , remove , or otherwise neutralize the solvent . diluting the solvent may cause the pan to solidify in the support . for instance , the pan may solidify , forming a filter disk or a filter medium that includes the pan and the metal hydroxide . in other words , the impregnated support may include the metal hydroxide incorporated into , or physically trapped in the pan . the adsorption medium 2 may also be used in a cartridge . the loading of the metal in the adsorption medium 2 and , therefore , the concentration of the metal hydroxide in the adsorption medium 2 may be limited by the solubility of the metal in the metal solution . during formation of the adsorption medium 2 , the pan and the metal cation are each present at the same time in a liquid state . since the pan and the metal hydroxide are formed into the adsorption medium 2 at the same time and do not require active sites , the concentration of the metal hydroxide in the adsorption medium 2 is not limited by the number of active sites on the adsorption medium 2 . in contrast , the metal loading in conventional ion exchange resins , where the metal is added to a preformed ion exchange resin , is limited by the number of active sites on the ion exchange resin . therefore , the adsorption medium 2 of the present invention may have a capacity approximately 70 times higher than that of conventional ion exchange resins . the adsorption medium 2 may also have a high surface area and porosity , which provides the adsorption medium 2 with an increased removal capacity for the constituents compared to conventional ion exchange resins . in addition , the adsorption medium 2 may be selective for certain constituents , such as arsenic , in the presence of other potentially competing anions , such as phosphate or nitrate . to produce the adsorption medium 2 having a metal oxide as the active component 6 , the matrix 4 may be dissolved in an organic solvent to form a pan solution . any organic solvent may be used provided that the organic solvent does not dissolve the metal oxide groups . for sake of example only , the organic solvent may be dmso . in one embodiment , the matrix 4 is pan and is dissolved in dmso . the metal oxide may be ground into a fine powder and added to the pan solution . the metal oxide may be an oxide of a divalent , a trivalent , or a tetravalent metal , such as an oxide of a transition metal , a lanthanide or rare earth metal , a group iii metal , a group iv metal , or a group v metal . for instance , the metal oxide may be an oxide of iron , zirconium , lanthanum , cerium , titanium , aluminum , tin , silver , zinc , mercury , bismuth , copper , antimony , tungsten , molybdenum . the metal oxide may be homogenously dispersed into the pan solution to form a metal oxide - pan solution . solid beads that include pan and the metal oxide may be formed by spraying the metal oxide - pan solution through an air / nozzle device into a quenching bath , as previously described , except that the quenching bath is a water bath . the solid beads are removed from the quenching bath , rinsed , dried , and screened to obtain a desired size fraction of the solid beads . the resulting solid beads may have the metal oxide incorporated into , or physically trapped in the matrix 4 . the adsorption medium 2 of the present invention may be used to remove oxyanion or oxyacid constituents of arsenic , selenium , or antimony from the feed stream 8 , as shown in fig2 . as previously described , the feed stream 8 includes at least one of these constituents . the feed stream 8 may be a drinking water source or an industrial water stream that is contaminated with at least one of the constituents . for sake of example only , the adsorption medium 2 may be used to remove as ( iii ) oxyacids , such as h 3 aso 3 or haso 2 , or as ( v ) oxyanions or oxyacids , such as h 3 aso 4 , h 2 aso 4 − , or haso 4 2 − . the feed stream 8 may be passed through the adsorption medium 2 to remove the arsenic before the feed stream 8 is distributed to users as potable water . the adsorption medium 2 has the capability of removing a substantial portion of the arsenic , even when the arsenic is present in the feed stream 8 at a low concentration . since the adsorption medium 2 has a high capacity for the constituents , the feed stream 8 ′ that exits the adsorption medium 2 may be substantially free of the constituents . in other words , the feed stream 8 ′ is substantially free of arsenic , selenium , or antimony and , therefore , may be a potable water supply . to remove the oxyanion or oxyacid constituents of arsenic , selenium , or antimony , the feed stream 8 may be passed through the adsorption medium 2 in a single pass operation . when these constituents contact the metal hydroxide in the adsorption medium 2 , a metal complex of the constituent may be formed . for sake of example only , if the feed stream includes arsenic oxyanions or oxyacids and is passed over an adsorption medium 2 that includes ferric hydroxide , the metal complex may be an iron arsenate salt complex or an iron arsenite salt complex . the metal complex is immobilized on the adsorption medium 2 and , therefore , the constituent is removed from the wastewater or drinking water . when the adsorption medium 2 is loaded with the metal complexes of the constituents to a maximal capacity , the adsorption medium 2 may be removed and disposed of , such as in a landfill . it is believed that the adsorption medium 2 loaded with the metal complexes of the constituents may meet criteria of the toxicity characterization leaching procedure and , therefore , may be disposed of . however , the adsorption medium 2 may also be regenerated and reused by treating the adsorption medium 2 loaded with the metal complexes with an alkaline solution . in one embodiment , the adsorption medium 2 may be used to remove or reduce indigenous arsenic contamination in the feed stream 8 to make the water supply potable . for instance , the adsorption medium 2 may be used to remove arsenic from the feed stream 8 having an arsenic concentration of less than approximately 50 ppb . the adsorption medium 2 may be used to reduce the concentration of arsenic to a concentration of less than approximately 10 ppm . since the adsorption medium 2 provides a large surface area and a consequent increased capacity for arsenic , large volumes of the feed stream 8 may be passed through the adsorption medium 2 before the adsorption medium 2 is loaded to a maximal capacity with the arsenic complexes . one liter of the adsorption medium 2 may be used to treat from approximately 30 , 000 bed volumes to approximately 100 , 000 bed volumes of the feed stream 8 . however , the adsorption medium 2 may also be used to remove arsenic from the feed stream 8 having an arsenic concentration of greater than 50 ppb . the adsorption medium 2 may be used to reduce the concentration of arsenic to a concentration of less than approximately 50 ppm . the adsorption medium 2 may also be used to treat or remediate contaminated surface waters or effluents produced by industrial activities . to effectively remove the constituents , a ph of the feed stream 8 may be at least approximately 6 . for instance , the ph of the feed stream 8 may range from approximately 6 to approximately 8 . the ph of the feed stream may be maintained at least approximately 6 so that the constituents to be removed are present as oxyanions or oxyacids . the adsorption medium 2 may be packed into a bed 10 that is used at the well head or point of origin of a water supply . packed beds 10 are known in the art and , therefore , the formation of the packed bed 10 is not described in detail herein . the packed bed 10 may include a housing within which the adsorption medium 2 is contained . in one embodiment , spherical beads of the adsorption medium 2 are packed so that sufficient spaces are present between the spherical beads to allow the feed stream 8 to pass through the packed bed 10 . once the feed stream 8 has passed through the packed bed 10 and the constituents are removed , the feed stream 8 ′ may be distributed as potable water . since the packed bed 10 is easily formed , the adsorption medium 2 may be an easy and economical way for small and mid - sized municipalities and other smaller - volume water users to remove the constituents from the feed stream 8 . more specifically , the adsorption medium 2 may be used to remove arsenic contaminants in the feed stream 8 to a concentration below the newly reduced mcl . the arsenic may be removed at a lower capital and operating cost than is required to establish a centralized water treatment facility . preparation of solid beads having ferric hydroxide incorporated in a pan matrix solid beads of the adsorption medium 2 were prepared by dissolving approximately 70 g / l of iron oxide into concentrated nitric acid to form the metal solution . pan was then dissolved in the metal solution to form the pan - metal solution having approximately 3 wt % to approximately 5 wt % pan . the pan - metal solution was then sprayed through an air / nozzle device into an alkaline quenching bath having 3 m naoh to form the solid beads . the solid beads were removed from the alkaline quenching bath , rinsed with ethanol , dried at a temperature of approximately 60 ° c ., and screened to obtain a desired size fraction of the solid beads . solid beads having pan and ferric hydroxide were produced . the solid beads had approximately 30 % fe ( iii ). the solid beads described in example 1 were tested to determine equilibrium arsenic capacity at various feed concentrations . a known weight of the solid beads was contacted with a water sample having a specific arsenic concentration . contacts between the solid beads and the water sample were repeated using different weights of the solid beads to obtain a plot of equilibrium arsenic concentration in the solid phase versus equilibrium arsenic concentration in the liquid phase . these plots are referred to as equilibrium isotherms . fig3 shows iron loadings ranging from 30 wt % to 70 wt %. these equilibrium isotherms provide data at or near the low arsenic concentrations that exist in potable water in the united states . as fig3 shows , at 70 % iron loading , the adsorption medium 2 provides an arsenic loading of approximately 3 mg / g with 20 ppb arsenic in the feed stream 8 . since the concentration of arsenic is very low in the feed stream 8 , there is a correspondingly low concentration gradient or driving force for mass diffusion into the solid phase . therefore , 3 mg / g arsenic in the solid phase is quite high . while the invention may be susceptible to various modifications and alternative forms , specific embodiments have been shown by way of example in the drawings and have been described in detail herein . however , it should be understood that the invention is not intended to be limited to the particular forms disclosed . rather , the invention is to cover all modifications , equivalents , and alternatives falling within the spirit and scope of the invention as defined by the following appended claims .