TECHNOLOGY FOCUS - INORGANIC CHEMISTRY - Preferred Method: The step of subjecting water to magnetic perturbation includes: subjecting water to a field from a monopolar magnet; subjecting water to a strong magnetic field gradient; or moving water through a centrifugal pump. The step (iii) includes the step of preparing the aqueous solution of Ca2+ ions by mixing a calcium compound in water contained in a non-magnetic mixing tank. The step of mixing the calcium compound in water contained in the non-magnetic mixing tank includes the step of subjecting the calcium compound in water to a monopolar magnetic field or magnetic field gradient. The step (iii) includes the step of chilling the solution of Ca2+ ions in water, where the solubility of the calcium compound is increased. The step (vi) includes the step of allowing the calcium precipitates to settle after which the precipitates are removed by decanting and filtering the solution from the precipitates. In step (vi), precipitation and settling of precipitates is aided. The ice collected from step (vi) is added to step (v) of a next cycle in the method for generating hydronium ion hydrate. The filter of step (viii) is a twenty mesh screen and step (viii) further includes: forcing the decanted precipitates with water through a filter press, in which a cake of calcium sulfate, usable as a soil pH modifier, is formed. Preferred Components: The calcium compound is calcium metal turnings, calcium hydrate, calcium oxide, calcium hydroxide, calcium phosphate dibasic, calcium sulfate or calcium carbonate. EXAMPLE - Pure water (600 gallons) was placed in a non-magnetic mixing tank equipped with a mechanical mixer and a recirculating pumping system. After water was recirculated for twenty minutes, reagent grade (93%) sulfuric acid was added to water to create a 3 molar solution. The acid-water mixture was recirculated for 10 minutes. The solution was next transferred to the nonmagnetic final mix tank. Then, pure water (200 gallons) was placed in a second non-magnetic mix tank. The recirculation system included an ISM (ion-state-modification) electro-oxidation unit in line that was designed to oxidize Ca2+ ions to Ca3+ ions. A calcium compound in the amount of 2/3 acid equivalent was added to water. The solution was recirculated until substantially all of the calcium was dissolved and oxidized. The oxidized calcium mixture was chilled and added to the sulfuric acid solution in the final mix tank. In the final mix tank, after all of the compound had been added, the reaction was permitted to go to completion. After the reaction was completed, a small amount of anionic surfactant was mixed thoroughly into the solution. The mechanical mixer was then turned off allowing calcium sulfate to crystallize and precipitate out from solution. The decant from the final mix tank was transferred to the product tank. The sludge was transferred to the product tank. The sludge was removed from the bottom of the final mix tank and dewatered in a belt or filter press. The filtrate was then transferred to the product tank. The solution from the product tank was placed in a batch or continuous freezing unit to create a frozen slush. The slush was placed in 20 mesh screen to separate liquid from ice. Then ice was permitted to melt and the liquid was transferred to the acid mix tank for reuse. The freezer concentrate was placed in a continuous low pressure low temperature distillation unit, in which the remaining water molecules were removed. The condensate was collected and returned to the acid water mix tank for reuse. The remaining liquid was the concentrated hydronium ion hydrate liquid.