A method for recovering sulfur values from waste by-product gypsum produced by the wet process production of phosphoric acid and recycling such sulfur values as sulfuric acid for utilization as a reagent in the wet process, comprising the steps of:
- dehydrating said gypsum to convert gypsum to calcium sulfate;
- supplying said calcium sulfate to a first reaction zone maintained at a temperature of from about 1600.degree. F. to about 2300.degree. F.;
- heating elemental sulfur to the boiling point of sulfur in an enclosed vessel which communicates with a delivery conduit to continuously supply sulfur vapor to said conduit;
- super heating said sulfur vapor during transit through said delivery conduit to a temperature of from about 1300.degree. F. to about 1800.degree. F.;
- debouching said super heated sulfur vapor from said conduit into said first reaction zone as a coherent gas which resists diffusion within said first zone and thus flows into concentrated contact with said calcium sulfate whereby a portion of said calcium sulfate is converted into calcium sulfide and sulfur dioxide;
- supplying said calcium sulfide and said unreacted portion of calcium sulfate to a second reaction zone which is held at a temperature of from about 1950.degree. F. to about 2400.degree. F. and maintaining said solids in said second zone for a time sufficient to permit essentially complete reaction between calcium sulfide and calcium sulfate to produce lime and sulfur dioxide;
- passing a non-reacting gas in counter-current flow through said second and first zone to collect and remove the sulfur dioxide generated therein from said zones;
- and
- converting said collected sulfur dioxide to sulfuric acid.