초록 ▼

A method of removing arsenic and fluoride from aqueous solutions in the same process is provided. Specifically, the pH of the aqueous solution is adjusted to a pH in the range of about 5 to 8. A combination of calcium salts, and ferric or aluminum salts are added to form insoluble arsenic and fluori

A method of removing arsenic and fluoride from aqueous solutions in the same process is provided. Specifically, the pH of the aqueous solution is adjusted to a pH in the range of about 5 to 8. A combination of calcium salts, and ferric or aluminum salts are added to form insoluble arsenic and fluoride bearing solids. The solids are then removed from the aqueous solution.

대표청구항 ▼

1. A method of removing arsenic and fluoride from an aqueous solution, characterized in that the aqueous solution is treated with calcium to form fluoride bearing particles and a combination of ferric or aluminum iron salts at a pH in the range of about 5 to 8 to form insoluble arsenic and fluoride

1. A method of removing arsenic and fluoride from an aqueous solution, characterized in that the aqueous solution is treated with calcium to form fluoride bearing particles and a combination of ferric or aluminum iron salts at a pH in the range of about 5 to 8 to form insoluble arsenic and fluoride bearing solids including said fluoride bearing particles; and removing said solids from the aqueous solution simultaneously reducing the level of arsenic and fluoride in said solution to a desired level by passing the aqueous solution through a microfiltration membrane having a pore size in the range from 0.5 to 10 microns at a flow rate of at least 200 gallons per square foot of membrane per day. 2. The method of claim 1 wherein the pH of the aqueous solution is maintained at about 7.5. 3. The method of claim 1 wherein the calcium salt is calcium chloride. 4. The method of claim 1 wherein the ferric salts are ferric chloride. 5. The method of claim 4 wherein the concentration of ferric salts in the aqueous solution is in the range of about 10 to 1,000 ppm. 6. The method of claim 1 wherein the pH does not exceed 8. 7. The method of claim 1 further comprising the step of: treating said aqueous solution, prior to removing said arsenic and fluoride bearing solids with a coagulant, a flocculant, or a combination thereof, to enhance formation of said solids. 8. The method of claim 7 wherein said coagulants or flocculants are selected from the group of EPI-DMA, DADMAC, copolymers of poly(acrylamide) and DADMAC, and any combination thereof. 9. The method of claim 1 wherein said treatment is carried out for a time of at least about 5 minutes. 10. The method of claim 1 wherein the mole ratio of calcium to fluoride is in the range of about 1 to 2 mole calcium to 2 mole fluoride. 11. A method of removing arsenic and fluoride from an aqueous solution, comprising the steps of: providing an aqueous solution including arsenic and fluoride; adjusting the pH of the aqueous solution to a pH in the range of about 5 to 8; adding calcium salt into the aqueous solution to form fluoride bearing particles; adding ferric or aluminum salts into the aqueous solution to form a metal hydroxide floc which absorbs both said fluoride particles and arsenic to produce insoluble arsenic and fluoride bearing solids; and removing said arsenic and fluoride bearing solids from the aqueous solution simultaneously reducing the level of arsenic and fluoride in said solution to a desired level by passing the aqueous solution through a microfiltration membrane having a pore size in the range from 0.5 to 10 microns at a flow rate of at least 200 gallons per square foot of membrane per day. 12. The method of claim 11 wherein said ferric salts are selected from the group of: ferric nitrate, ferric chloride, ferric ammonium sulfate, ferric ammonium chloride, ferric hydroxide and ferric oxide. 13. The method of claim 11 wherein said calcium salt is calcium chloride. 14. The method of claim 11 further comprising the step of: treating said aqueous solution, prior to the removing step, with coagulants, flocculants, or a combination thereof, to enhance formation of the arsenic and fluoride bearing solids. 15. The method of claim 11 wherein said method is carried out for a time of at least 5 minutes. 16. The method of claim 11 wherein the mole ratio of calcium to fluoride is in the range of about 1 to 2 mole calcium to 2 mole fluoride. 17. The method of claim 11 wherein the concentration of ferric salts in the aqueous solution is in the range of about 10 to 1,000 ppm.