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Mitigation and Remedy of Groundwater Arsenic Menace in India

Mitigation and Remedy of Groundwater Arsenic Menace in India

Mitigation and Remedy of Groundwater Arsenic Menace in India

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Technological Options <strong>and</strong> <strong>Arsenic</strong> Removal TechnologiesH<strong>and</strong>pumpAttached <strong>Arsenic</strong>Removal Plant byAIIH&PH,KolkataIONOCHEM,KolkataApyron <strong>Arsenic</strong>Treatment Unitsby ApyronTechnologies (P)Ltd. Represent<strong>in</strong>g<strong>of</strong> ApyronTechnologies Inc.,USAPublic HealthEng<strong>in</strong>eer<strong>in</strong>gDepartment, Govt.<strong>of</strong> West Bengal80Oxidation +Coagulation +Flocculation/Precipitation<strong>and</strong> filtrationIon exchangeAdsorptionChlor<strong>in</strong>at<strong>in</strong>gagent (BP) +Ferric AlumFerricHydroxideAqua B<strong>in</strong>d(ActivatedAlum<strong>in</strong>a + )Adsorption Red Hematite(Fe 2O 3) lumps +quartz + s<strong>and</strong>activatedalum<strong>in</strong>aRs. 35,000 +periodicchemicalreagentsRs. 39,000Rs. 80,000 +Rs. 15,000per chargeRs. 27,000p yfirst passes through a coarse sta<strong>in</strong>lesssteel stra<strong>in</strong>er <strong>and</strong> then comes <strong>in</strong>contact with filter media <strong>in</strong> whichcatalytic precipitation takes place.The purified water from the primarychamber goes to secondary chamberfor downward filtration. Fromsecondary chambers water passesthrough micro-filtration chamber <strong>and</strong>then purified water goes through threeway valve at the outlet.The system is comprised <strong>of</strong> a nonmechanicalclari-flocculator <strong>and</strong> upflowgravel filter <strong>and</strong> it has threechambers. Bleach<strong>in</strong>g powder <strong>and</strong>alum are the two chemicals used forremoval <strong>of</strong> arsenic. In the firstchamber bleach<strong>in</strong>g powder solution isadded <strong>in</strong> appropriate dosage withpumped water where they arethoroughly mixed <strong>in</strong> presence <strong>of</strong>baffles. The chemical mixed water isthereafter passed through secondchamber for precipitation <strong>of</strong> the flocs.The clean water is collected <strong>in</strong> thelaunder chamber. From launder wateris taken to the filter (third) chamber,from where water is allowed to flow<strong>in</strong> upward direction through gradedgravel media. The arsenic safe filteredwater is f<strong>in</strong>ally collected through a tapprovided <strong>in</strong> the filtered chamber.The system is comprised <strong>of</strong> one IronRemoval Filter <strong>and</strong> one <strong>Arsenic</strong> Filter<strong>and</strong> the system is fitted with H<strong>and</strong>Pump The pr<strong>in</strong>cipal media is bondedcompound <strong>of</strong> Fe(OH) 3 <strong>and</strong> βFeOOH.When H<strong>and</strong> Pump is operated, thepressurized raw water is passed<strong>in</strong>itially through iron removal filterfilled with catalytic filter<strong>in</strong>g media<strong>and</strong> reacts with sodium arsenates <strong>and</strong>Fe(OH) 2. Due to chemisorption AS isbonded with the material <strong>and</strong> <strong>Arsenic</strong>is removed.The system is comprised <strong>of</strong> anassembly <strong>of</strong> H<strong>and</strong>pump with its outletconnected to the filter<strong>in</strong>g media.When the H<strong>and</strong> Pump is operated, theraw water passes through the filtermedia where arsenic is removed <strong>and</strong>f<strong>in</strong>ally treated water is collectedthrough an outlet pipe from the filtermedia. The filter media is comprised<strong>of</strong> manganese oxide <strong>and</strong> activatedalum<strong>in</strong>a. Manganese oxide convertsAs 3+ to As 5+ , which is adsorbed on thealum<strong>in</strong>a media. The unit also removesiron.Removal <strong>of</strong> arsenic is accomplished <strong>in</strong>4 chambers. <strong>Groundwater</strong> isabstracted by H<strong>and</strong> Pump <strong>and</strong> spray<strong>in</strong>to droplets over a bed conta<strong>in</strong><strong>in</strong>gpacked hematite lumps (Fe 2O 3) beforesend<strong>in</strong>g to first chamber forsedimentation. Sediment free water isconveyed through chambers placed <strong>in</strong>series conta<strong>in</strong><strong>in</strong>g red hematite lumps,Periodic daily dos<strong>in</strong>g<strong>of</strong> chemical reagentsare necessary. Thesystem requiresconstant vigilance <strong>and</strong>close monitor<strong>in</strong>g <strong>and</strong>chemical dos<strong>in</strong>g.Regular backwash<strong>in</strong>g<strong>of</strong> iron filter isessential, whichcaused problem <strong>of</strong>operation <strong>and</strong>ma<strong>in</strong>tenance.Otherwise, theperformance rema<strong>in</strong>edsatisfactory.Showed satisfactoryperformance, treat<strong>in</strong>garsenic levels as highas 3500 ppb to a safelevel <strong>of</strong> less than 50ppb. After use, filtermedia can be disposedsafely as ord<strong>in</strong>arysanitary waste.Reported as one <strong>of</strong> thef<strong>in</strong>est perform<strong>in</strong>gdevises <strong>and</strong> capable toremove arsenic fromvery high level <strong>of</strong>contam<strong>in</strong>ation.However, theweakness is its<strong>in</strong>ability to produceNIH & CGWB

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