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A process for treating acid mine drainage containing heavy metals and soluble contaminants is provided. In one embodiment, at least a metal cation is added to the acid mine drainage at a pre-select pH to form insoluble heavy metal complexes. In one embodiment, the metal cation is a trivalent metal i

A process for treating acid mine drainage containing heavy metals and soluble contaminants is provided. In one embodiment, at least a metal cation is added to the acid mine drainage at a pre-select pH to form insoluble heavy metal complexes. In one embodiment, the metal cation is a trivalent metal ion, e.g., ferric iron such as in ferric sulfate. In another embodiment, a divalent metal ion such as in ferrous sulfate is used. After the removal of the heavy metal complexes, the effluent water is treated with at least a phosphate additive to remove remaining soluble contaminants, thus producing a treated water stream with reduced levels of contaminants.

대표청구항 ▼

1. A method for treating acid mine drainage to reduce the concentration of heavy metals and soluble contaminants, the acid mine drainage contains at least a heavy metal selected from molybdenum, tungsten, chromium, manganese, nickel, arsenic, and vanadium, and at least a soluble anionic species sele

1. A method for treating acid mine drainage to reduce the concentration of heavy metals and soluble contaminants, the acid mine drainage contains at least a heavy metal selected from molybdenum, tungsten, chromium, manganese, nickel, arsenic, and vanadium, and at least a soluble anionic species selected from nitrate, nitrite, sulfate, fluoride, and chloride, the method comprising: contacting the acid mine drainage with an effective amount of at least a trivalent metal cation selected from ferric chloride and ferric sulfate at a pH of 6 or less for the at least a trivalent metal cation to form at least a complex with at least one of the heavy metals;performing a liquid solid separation to remove the at least a complex forming a first effluent containing less than 0.08 ppm molybdenum, wherein the liquid solid separation is via flocculation and clarification in an inclined plate settler and wherein at least a flocculent is added to the inclined plate settler to bind the at least a complex;adding at least a phosphate additive to the first effluent at an alkaline pH between 9 and 13 to obtain a soluble phosphrous concentration of less than 1 ppm, and a soluble sulfate concentration of less than 630 ppm, and at least one of the at least a soluble anionic species forms a precipitate;performing a liquid solid separation to remove the precipitate, forming a second effluent. 2. The method of claim 1, wherein contacting the acid mine drainage with the at least a trivalent metal cation is at a pH between 3.0 and 6.0. 3. The method of claim 2, wherein contacting the acid mine drainage with the at least a trivalent metal cation is at a pH between 3.0 and 5.0. 4. The method of claim 3, wherein contacting the acid mine drainage with the at least a trivalent metal cation is for a sufficient amount of time for at least 50% of the heavy metals to form an insoluble complex with the at least a trivalent metal cation. 5. The method of claim 1, wherein the effective amount of the at least a trivalent metal cation ranges from 6 to 50 ppm of the at least a trivalent metal cation to each ppm of heavy metals contained in the acid mine drainage. 6. The method of claim 1, wherein the acid mine drainage contains manganese and the second effluent contains less than 0.005 ppm manganese. 7. The method of claim 1, wherein the acid mine drainage contains nickel and the second effluent contains less than 0.010 ppm nickel. 8. The method of claim 1, wherein the acid mine drainage contains zinc and the second effluent contains less than 0.05 ppm zinc. 9. The method of claim 1, wherein the acid mine drainage contains aluminum and the second effluent contains less than 0.02 ppm aluminum. 10. The method of claim 1, wherein the at least a phosphate additive comprises a mixture of phosphoric acid and at least a salt of calcium bicarbonate. 11. The method of claim 1, wherein the flocculent is an anionic polymer. 12. The method of claim 1, wherein the liquid solid separation to remove the heavy metal complex is via coagulation. 13. The method of claim 1, wherein the pH of the first effluent is adjusted to 9.0 to 12.0 by adding lime. 14. The method of claim 1, wherein the at least a phosphate additive is selected from the group of hydroxyapatite, hexametaphosphate, polyphosphate, monocalcium phosphate, dicalcium phosphate, tricalcium phosphate, calcium orthophosphates, calcium dihydrogen phosphate monohydrate, phosphate fertilizers, phosphate rock, pulverized phosphate rock, calcium orthophosphates, animal bone phosphate, and combinations thereof. 15. The method of claim 14, wherein the at least a phosphate additive is a phosphate fertilizer selected from monoammonium phosphate (MAP), diammonium phosphate (DAP), single superphosphate (SSP), triple superphosphate (TSP), and combinations thereof. 16. The method of claim 14, wherein the at least a phosphate additive is calcium dihydrogen phosphate monohydrate. 17. The method of claim 1, wherein the at least a phosphate additive is added in an amount sufficient to provide 500 to 2000 ppm of phosphrous content. 18. The method of claim 1, wherein the acid mine drainage contains fluoride, and a sufficient amount of the at least a phosphate additive is added to the first effluent to reduce the concentration of fluoride in the first effluent to less than 1 ppm. 19. The method of claim 1, wherein the acid mine drainage contains sulfate, and a sufficient amount of the at least a phosphate additive is added to the first effluent to reduce the concentration of sulfate in the first effluent to less than 300 ppm. 20. The method of claim 1, further comprising adjusting the pH of the second effluent to less than 9 for on-site or off-site reuse or discharge. 21. The method of claim 20, wherein the pH of the second effluent is adjusted by addition of carbon dioxide. 22. A method for treating effluent water from excavations and extractions to reduce the concentration of heavy metals and soluble contaminants in the effluent water, comprising: providing effluent water having a pH from 2.0 to 10.0, one or more heavy metal ions or metal salts selected from molybdenum, tungsten, manganese, nickel, chromium, arsenic, and vanadium, and at least a soluble anionic species selected from nitrate, nitrite, sulfate, fluoride, and chloride;contacting the effluent water with ferric ion in an amount effective and at a pH of 6 or less for the ferric iron to form at least an insoluble complex with at least one of the heavy metals;performing a liquid solid separation to remove the at least a insoluble complex forming a first effluent containing less than 0.08 ppm molybdenum, wherein the liquid solid separation is via flocculation and clarification in an inclined plate settler and wherein at least a flocculent is added to the inclined plate settler to bind the at least an insoluble complex;adding at least a phosphate fertilizer to the first effluent for a soluble phosphrous concentration of less than 1 ppm, and a soluble sulfate concentration of less than 630 ppm, and at least one of the at least a soluble anionic species forms a precipitate at an alkaline pH between 9 and 13; andperforming a liquid solid separation to remove the precipitate, forming a second effluent. 23. The method of claim 22, wherein the at least a phosphate fertilizer is selected from the group of single superphosphate and triple superphosphate.