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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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5.2.2 Co-precipitation<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 DocumentCo-precipitation has been the most frequently used method to treat arsenic contam<strong>in</strong>atedwater <strong>in</strong> numerous pilot- <strong>and</strong> full-scale applications. This technology can typically reducearsenic concentrations to less than 50 µg/L <strong>and</strong> <strong>in</strong> some cases below 10 µg/L. In order to removearsenic by co-precipitation, coagulant is to be added. Water treatment with coagulants, such asalum [Al 2(SO 4) 3.18H2O], ferric chloride [FeCl 3] <strong>and</strong> ferric sulfate [Fe 2(SO 4) 3.7H 2O], areeffective <strong>in</strong> remov<strong>in</strong>g arsenic from water. Ferric salts have been found to be more effective <strong>in</strong>remov<strong>in</strong>g arsenic than alum on a weight basis <strong>and</strong> effect over a wider range <strong>of</strong> pH. In bothcases, pentavalent arsenic can be more effectively removed than trivalent arsenic. Thefollow<strong>in</strong>g steps are <strong>in</strong>volved <strong>in</strong> the co-precipitation process for removal <strong>of</strong> arsenic:• Addition <strong>of</strong> bleach<strong>in</strong>g powder / hypochlorite,• Addition <strong>of</strong> alum / ferric sulphate,• Rapid mix<strong>in</strong>g <strong>of</strong> chemical followed by slow mix<strong>in</strong>g,• Sedimentation, <strong>and</strong>• Filtration.In the coagulation-flocculation process, alum<strong>in</strong>um sulfate or ferric chloride or ferricsulfate is added <strong>and</strong> dissolved <strong>in</strong> water by stirr<strong>in</strong>g for few m<strong>in</strong>utes. Alum<strong>in</strong>um or ferric hydroxidemicro-flocs are formed rapidly. The water is, then, gently stirred for few m<strong>in</strong>utes foragglomeration <strong>of</strong> micro-flocs <strong>in</strong>to larger easily settable flocs. Dur<strong>in</strong>g this flocculation process, allk<strong>in</strong>ds <strong>of</strong> micro-particles <strong>and</strong> negatively charged ions are attached to the flocs by electrostaticattachment. <strong>Arsenic</strong> is also adsorbed onto coagulated flocs. As trivalent arsenic occurs <strong>in</strong>non-ionized form, it is not subject to significant removal. Oxidation <strong>of</strong> As (III) to As (V) is, thus,required as a pretreatment for efficient removal. This can be achieved by addition <strong>of</strong> bleach<strong>in</strong>gpowder (chlor<strong>in</strong>e) or potassium permanganate. The follow<strong>in</strong>g three chemical precipitationprocesses are normally used:i) Enhanced Lime S<strong>of</strong>ten<strong>in</strong>g,ii) Conventional Gravity Coagulation/Filtration, <strong>and</strong>iii) Coagulation Assisted Micro-filtration.5.2.2.1 Enhanced Lime S<strong>of</strong>ten<strong>in</strong>gLime s<strong>of</strong>ten<strong>in</strong>g is a chemical-physical treatment process used to remove calcium <strong>and</strong>magnesium from solution. The addition <strong>of</strong> lime <strong>in</strong>creases the pH <strong>of</strong> solution, thereby, causes ashift <strong>in</strong> the carbonate equilibrium <strong>and</strong> the formation <strong>of</strong> calcium carbonate <strong>and</strong> magnesiumhydroxide precipitates. These precipitates are amenable to removal by clarification <strong>and</strong> filtration.Lime s<strong>of</strong>ten<strong>in</strong>g solely, for arsenic removal, is uneconomical <strong>and</strong> is generally consideredcost-prohibitive. However, for water systems that use lime s<strong>of</strong>ten<strong>in</strong>g to reduce hardness, theNIH & CGWB 83

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