TECHNOLOGY FOCUS - INORGANIC CHEMISTRY - Preferred Components: The first acid comprises greater than or equal to 50 wt.% of phosphoric acid. The second acid comprises phosphoric acid and/or sulfuric acid. The base comprises anhydrous or aqueous ammonia. The ferrate is selected from calcium ferrate, sodium ferrate, potassium ferrate, and/or ferrous sulfate heptahydrate. The oxidizing agent is selected from hydrogen peroxide, calcium hypochlorite, sodium hypochlorite, potassium hypochlorite, chlorine dioxide, ozone, and/or oxygen. The plant nutrient is selected from urea, ammonium nitrate, ammonium sulfate, monoammonium phosphate, diammonium phosphate, urea ammonium nitrate, liquid urea, potash, iron oxide, soluble iron, and/or chelated iron. The hardening agent is selected from ferric oxides, alum attapulgite clay, industrial molasses, lignon, lignosulfonate, and/or urea formaldehyde polymerizer.    TECHNOLOGY FOCUS - ORGANIC CHEMISTRY - Preferred Method: The dewatered biosolids are created by subjecting biosolids to filtration, centrifugation, and/or pressure. The second acid and the base together create an exothermic reaction within the mixture, where the exothermic reaction takes place without external heating. The mixture is maintained at greater than or equal to 230 degrees F. The method further involves adding ferrate or oxidizing agent to the mixture, where the ferrate is formed from reaction of a solid-state sodium hydroxide with sodium hypochlorite and ferric chloride. The retention time is less than or equal to 15 minutes. The acidity, pressure, flow speed, pH, and base infusion speed are controlled by closed-loop computer controls to maintain a predetermined reaction temperature. The biosolids are continuously processed through the pressure vessel continuously forming the treated and dried biosolids. The organic material in the treated and dried biosolids is partially or completely hydrolyzed, denatured, or sterilized. The phosphate content of the dried mixture is 0.5-4 wt.%. The nitrogen content of the dried mixture is enhanced by aqueous ammonia that is added to the reaction vessel. The method further involves adding a granulating agent to the mixture before drying to form a dried and granulated mixture; crushing the dried and granulated mixture; passing the dried and granulated mixture through screens to isolate granules of a predetermined size; coating the dried granules with a coating agent, where the coating agent is applied to the granules within a cooling apparatus; cooling the dried and granulated mixture in a cooling apparatus to less than or equal to 140 degrees F, where the cooling apparatus is a fluidized bed, ammonia chiller, or rotating drum; passing the reaction mixture through a second pressure vessel; adding at least one plant nutrient to the mixture in the pressure vessel; and adding hardening agent to the mixture. Preferred System: The system further comprises a steam generator, where steam produced by the steam generator is injected into the first mixer; ammonia vaporizer; and baghouse dryer. The pressure vessel further comprises several valves to control at least one of steam levels, mixture levels, and temperature, presser, pH, and nitrogen levels. The air discharge from the facility is less than 30 cubic feet per minute (CFM). Preferred Components: The organic material is selected from pharmaceutical compounds, antibiotics, hormones, hormone-like molecules, biologically active compounds, macromolecules, carbohydrates, nucleic acids, fats, lipids, and/or proteins.