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Mitigation and Remedy of Groundwater Arsenic Menace in India

Mitigation and Remedy of Groundwater Arsenic Menace in India

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<strong>Mitigation</strong> <strong>and</strong> <strong>Remedy</strong> <strong>of</strong> <strong>Groundwater</strong> <strong>Arsenic</strong> <strong>Menace</strong> <strong>in</strong> <strong>India</strong> : A Vision Documentstage. The optimal pH ranges for coagulation, with alum<strong>in</strong>um <strong>and</strong> ferric salts, are 5 to 7 <strong>and</strong> 5 to8, respectively. At pH values above 7, the removal performance <strong>of</strong> alum<strong>in</strong>um-based coagulantsdrops markedly. Feed water pH should be adjusted to the appropriate range, prior to coagulantaddition. Post-filtration pH adjustment may be necessary to optimize corrosion control <strong>and</strong>comply with other regulatory requirements.Several batch studies have demonstrated that As (V) removal is positively related tocoagulant dosage. However, specific dose requirements, needed to meet As (V) removalobjectives, were cont<strong>in</strong>gent upon the source water quality <strong>and</strong> pH. Effective coagulant dosageranges were 5-25 mg/L <strong>of</strong> ferric chloride <strong>and</strong> as much as 40 mg/L <strong>of</strong> alum.5.2.2.3 Coagulation Assisted Micro-filtrationCoagulation-assisted micro-filtration uses the same coagulation process described above.However, <strong>in</strong>stead <strong>of</strong> the granular media filtration step, the water is forced through asemi-permeable membrane by a pressure differential. The membrane reta<strong>in</strong>s the As (V) ladenfloc formed <strong>in</strong> the coagulation step.The use <strong>of</strong> pre-eng<strong>in</strong>eered coagulation assisted micr<strong>of</strong>iltration package plants is arealistic possibility for new <strong>in</strong>stallations, where water quality precludes the use <strong>of</strong> sorptiontreatment. The membrane must be periodically backwashed to dislodge solids <strong>and</strong> restorehydraulic capacity. Backwash water is typically a high-volume, low solids (less than 1.0%)waste stream. The specific amount <strong>of</strong> solids will depend on several factors, <strong>in</strong>clud<strong>in</strong>g coagulanttype, dosage, filter run length <strong>and</strong> ambient solids concentration.The co-precipitation technique for removal <strong>of</strong> arsenic has been applied <strong>in</strong> the follow<strong>in</strong>gsystems:• Central <strong>Arsenic</strong> Removal Plant (ARP) attached with tube wells for piped watersupply,• <strong>Arsenic</strong> Removal Plant (ARP) attached with H<strong>and</strong> Pump, <strong>and</strong>• Domestic <strong>Arsenic</strong> Removal Units us<strong>in</strong>g Earthen Pots, Plastic Buckets, BucketTreatment Units, Modified BTUs, Stevens Institute Technology, Fill <strong>and</strong> Draw Units,Naturally Occurr<strong>in</strong>g Iron, Chemical Packages, etc.5.2.3 AdsorptionAdsorption technology has been widely used to treat groundwater <strong>and</strong> dr<strong>in</strong>k<strong>in</strong>g waterconta<strong>in</strong><strong>in</strong>g arsenic. The technology can reduce arsenic concentrations to less than 50 µg/L <strong>in</strong>general <strong>and</strong> <strong>in</strong> some cases even below 10 µg/L. Its effectiveness is sensitive to a variety <strong>of</strong>untreated water contam<strong>in</strong>ants <strong>and</strong> characteristics. It is used less frequently than precipitation/co-precipitation technologies, <strong>and</strong> is most commonly used to treat groundwater <strong>and</strong> dr<strong>in</strong>k<strong>in</strong>gwater.NIH & CGWB 85

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