<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 Documentarsenic-rich m<strong>in</strong>e dra<strong>in</strong>age <strong>and</strong> the subsequent decrease <strong>of</strong> arsenic content, down gradient fromwhere discharges crossed limestone outcrops, <strong>in</strong>dicated that limestone is a possible arsenicremoval medium (Davis et al., 1999). Surface area <strong>of</strong> the limestone is a key parameter,controll<strong>in</strong>g the efficiency <strong>of</strong> the process. The smaller gra<strong>in</strong> sizes have provided a greater surfacearea per unit weight. Thus, better arsenic removal has been demonstrated.The areas <strong>of</strong> major concern, regard<strong>in</strong>g feasibility <strong>of</strong> a limestone-based arsenic removalprocess, are ionic <strong>in</strong>terference, the stability <strong>and</strong> disposal <strong>of</strong> arsenic-saturated limestone, <strong>and</strong> therate at which the process can treat water. Each <strong>of</strong> these concerns should be addressed. Theprocess should be studied at the molecular level, regard<strong>in</strong>g what compound is formed on orwith<strong>in</strong> the limestone. A better underst<strong>and</strong><strong>in</strong>g <strong>of</strong> the entire process <strong>and</strong> the composition <strong>of</strong> thearsenic-rich limestone waste product would likely result from such a study. Perhaps a material,other than limestone, needs to be added to the process to enhance waste product stability. Basedon previous research, iron oxide seems an appropriate choice. Other lime stones should betested. A rock unit can conta<strong>in</strong> various constituents <strong>and</strong> still qualify for classification aslimestone. One <strong>of</strong> these m<strong>in</strong>or constituents could greatly enhance the process. Various othernatural waters should be used <strong>in</strong> upcom<strong>in</strong>g work with a batch reactor. Chemical analyses <strong>of</strong>these natural waters should be done <strong>in</strong> an attempt to identify as to which ions preferentially<strong>in</strong>terfere. Column experiments, us<strong>in</strong>g a constant flow rate, are needed. Underst<strong>and</strong><strong>in</strong>g the flowmechanics <strong>of</strong> the process will be essential to the development <strong>of</strong> a prototype.A prototype cartridge must be designed. Experimental data regard<strong>in</strong>g mass adsorptionratios <strong>and</strong> necessary residence times, <strong>in</strong>dicat<strong>in</strong>g an appropriate cartridge size <strong>and</strong> flow rate,would assist <strong>in</strong> the design <strong>of</strong> a prototype. The <strong>in</strong>tent <strong>of</strong> any design should be to maximize theefficiency <strong>of</strong> the limestone-based arsenic removal process, with regard to both limestone mass<strong>and</strong> water volume or flow rate. This assumes the use <strong>of</strong> 58 smallest feasible limestone gra<strong>in</strong>sizes. Cost <strong>and</strong> availability factors could affect that assumption. Initial experimental work hasbeen successful <strong>in</strong> demonstrat<strong>in</strong>g the use <strong>of</strong> limestone to reduce the arsenic concentrations <strong>of</strong> aprepared st<strong>and</strong>ard solution. Prototype design <strong>and</strong> arsenic-rich limestone disposal must be addressed,before the ultimate feasibility <strong>of</strong> apply<strong>in</strong>g limestone-based arsenic removal systems,can be determ<strong>in</strong>ed. Further work should focus on exp<strong>and</strong><strong>in</strong>g the applications <strong>of</strong> the process,namely, to <strong>in</strong>clude remov<strong>in</strong>g arsenic from natural waters as well as st<strong>and</strong>ard solutions.6.3.3 Remediation <strong>of</strong> <strong>Arsenic</strong> contam<strong>in</strong>ated Soils by <strong>in</strong> situ Chemical FixationSubsurface soils, from several <strong>in</strong>dustrial facilities, are contam<strong>in</strong>ated with arsenicbecause <strong>of</strong> the application <strong>of</strong> arsenic conta<strong>in</strong><strong>in</strong>g herbicide. Low cost <strong>in</strong> situ chemical fixationtreatment is designed to react with contam<strong>in</strong>ated soils directly, aga<strong>in</strong>st the treatment solutions tocause the formation <strong>of</strong> <strong>in</strong>soluble arsenic-bear<strong>in</strong>g phases, <strong>and</strong> thereby, decreases theenvironmental leachability <strong>of</strong> arsenic (Xang, Li et al). Comb<strong>in</strong>ations <strong>of</strong> ferrous sulfate, potassiumpermanganate <strong>and</strong> calcium carbonate are used as major reagents for the chemical fixationNIH & CGWB 117
A Critical Appraisal- Future Risk, Scope to Remediate, Technological Competence, etc.solutions. Sequential leach<strong>in</strong>g, with an extraction fluid described <strong>in</strong> the EPA syntheticprecipitation leach<strong>in</strong>g procedure (SPLP), has been used to simulate the long-term leach<strong>in</strong>gbehavior <strong>of</strong> treated soils under natural conditions. The results <strong>in</strong>dicate that the fixation solution,with only ferrous sulfate, have the best effect among all the reagent comb<strong>in</strong>ations, reduc<strong>in</strong>gSPLP-leachable arsenic by as much as 90%.A modified 4-step sequential extraction procedure can be used to further study thechemical fractionation <strong>of</strong> soil As, before <strong>and</strong> after chemical treatment. Sequential extractiondata would likely show that the soil treatment has greatly reduced the most readily labile portion<strong>of</strong> arsenic which is extracted <strong>in</strong> the 1st step <strong>of</strong> the sequential extraction, with its value lowered toless than one tenth than that <strong>of</strong> untreated soil. The potentially mobile fraction <strong>of</strong> soil arsenic,extracted <strong>in</strong> the 2nd step <strong>of</strong> the sequential extraction, is also considerably smaller. It is shownthat after treatment; most <strong>of</strong> the As <strong>in</strong> the soil is transferred to amorphous Fe oxyhydroxideswhich are the major phases extracted <strong>in</strong> the 3rd step. X-ray absorption near edge spectra showAs is present as As (V) <strong>in</strong> the treated soil. Extended X-ray absorption f<strong>in</strong>e structure (EXAFS)spectral analysis <strong>in</strong>dicates that a large portion <strong>of</strong> the total soil arsenic is co-precipitated <strong>and</strong><strong>in</strong>corporated <strong>in</strong>to newly formed amorphous Fe oxides after treatment.6.4 Experiences dur<strong>in</strong>g <strong>Arsenic</strong> Removal Technology Evaluation <strong>in</strong> Technology ParkSchool <strong>of</strong> Fundamental Research has been entrusted to conceptualize, execute <strong>and</strong>manage the evaluation programme <strong>of</strong> <strong>Arsenic</strong> Removal Technologies, us<strong>in</strong>g an <strong>Arsenic</strong>Technology Park dur<strong>in</strong>g August 2001 to September 2003. It has ga<strong>in</strong>ed some knowledge aboutthe problems <strong>and</strong> genesis <strong>of</strong> arsenic mitigation <strong>in</strong> dynamic field conditions. Some <strong>of</strong> which arementioned below.(i)Tube-well: The probable scenario has been <strong>in</strong> operation for more than a decade, withmost <strong>of</strong> the tube-wells, which have been selected, based on their contam<strong>in</strong>ation level,<strong>and</strong> has practically concluded their critical life span. These have been found to be thesame <strong>in</strong> all cases. Re-s<strong>in</strong>k<strong>in</strong>g <strong>of</strong> all the tube wells, due to sudden heavy drawl <strong>of</strong> water,becomes a necessity.S<strong>in</strong>ce most <strong>of</strong> the lift pumps are used to pump water for gravitational drawdown throughthe media column natural system, resistance seems to affect the performance <strong>of</strong> thetube wells, which are otherwise meant for free lift<strong>in</strong>g <strong>of</strong> water without any resistance <strong>in</strong>the path. Thus, difference <strong>in</strong> pull-push process <strong>in</strong>teraction with<strong>in</strong> the tube well generatesa resultant back-pressure. Cont<strong>in</strong>uous over use disturbs the performance <strong>of</strong> the liftpumps as well as creates an impact on the <strong>in</strong>terface mechanism. It is one <strong>of</strong> the criticalissues that seem to affect the overall performance <strong>of</strong> ARPs.118NIH & CGWB