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    Metal removal byelectro-coagulation

    Guided by:Prof. Nikita Chokshi

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    Need for the removal of metal

    y Nowdays in this era of industrialisation large amount amount of toxic metals copper,

    sulphate, arsenic etc. are released from industrial activites which can lead to

    contamination of ground water as well as surface water if released without any

    treatment because of it there is always a need to treat this effluents of industries before

    releasing them to the environment.

    y Also many trace element like arsenic present in ground as well as surface water has

    became a major unavoidable threat for the life of human beings and useful

    microorganisms.

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    Methods available for metal removal

    y Chemical coagulation

    y Adsorption

    y

    Electrocoagulation

    y Reverse osmosis

    y Nano filtration

    y electrodialysis

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    Electrocoagulation process

    y In the electrocoagulation process, the coagulant is generated in situ by the electrolytic

    oxidation of an appropriate anode material.

    y In this process charge ionic species like metals or otherwise are removed from

    wastewater by allowing it to react with an ion having opposite charge or with floc of

    metallic hydroxides generated within the effluent.

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    Comparison of chemical coagulation

    y Main advantages of EC over conventional coagulation are as follows:

    No alkalinity consumption

    No change in bulk pH

    Direct handling of corrosive chemical is eliminated

    Can be easily adapted for use in portable water treatment unit especially

    during emergencies

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    Metal removal using organic adsorbents

    y We have to find a suitable a adsorbent for each and every specific metal to be removed

    from waste water while we can use any of the iron, aluminium or steel elctrode in

    general to remove metal from water.

    y Also the adsorbent used for process should be recovered because of the cost of

    adsorbent used and so the total cost including the recovery cost makes it an ineffective

    option.

    y For example for arsenic removal activated carbon specifically named As-GAC

    (granular activated carbon) that contained iron by Gu et al has a working range of 5-

    20 mg/l at pH 7 and can remove only As (III) and not As (V) only upto 1.393 mg/g

    y For the regeneration of sorbents used sorbing arsenic they need to wash with alkali

    such as casutic soda and neutralising using HCl or H2SO4 and thus results in alkaline

    waste sludge due to alkali to acid ratio

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    EC process setup

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    Factors affecting electrocaogulation

    y Major factors affecting the electrocogulation seperation are :

    Area of the metal plate used as electrode

    pH of the medium

    Current density

    Concentration of the metal in the inlet water/wastewater

    total time of the process

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    Overview of arsenic removal from water

    y Sources of arsenic in water are :

    natural occurrence in ground as well as surface water

    copper smelting industrial effluent

    metal plating effluent

    other types of industrial effluents

    y Because of high toxicity of arsenic its standard has been set to 2-20 g/l for drinking

    purpose.

    y Arsenic may present in two states in water i.e. arsenite or arenate depending on th pH

    of the medium.

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    Reaction mechanism of arsenic removal by EC

    y Consider aluminium electrodes :

    Al Al3+ + 3e-

    Al3+ + 3H2O Al(OH)3 + 3H+

    Al(OH)3 + AsO43- Al(OH)3 *AsO4

    3-

    y Finally the compund formed in the last reaction produced gets aggregate and can be

    removed with suitable method.

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    Results of arsenic remval using aluminium electrode

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    List of analytical methods

    y Mass spectrometry

    y Powered x-ray diffraction

    y

    X-ray photoelectron spectroscopy

    y Scanning electron microscope and energy dispersive x-ray analyzer

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    Disposal methods for arsenic containing treated water

    y Landfill

    y Mixing with livestock waste

    y Incorporating within construction material

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    Future goal

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    References

    y M.Yousuf A. Mollah , Robert Schennach, Jose R. Parga, David L. Cocke,

    Electrocoagulation (EC) Science and applications, journal of Hazardous Material B84

    (2001) 29-41

    y Dinesh Mohan, charles U. Pittman Jr., Arsenic removal from water/wastewater using

    adsorbents A critical review, journal of Hazardous Materials 142 (2007) 1-53

    y Jochen Bundschuh, Marta Litter, Virginia S.T. Ciminelli, Maria Eugenia Morgada,

    Lorena Cornejo, Sofia Garrido Hoyos, Jan Hoinkis, Ma. Teresa Alarcon-Herrera, Maria

    Aurora Armienta, prosun Bhattacharya, Emerging mitigation needs and sustainable

    options for solving the arsenic problems of rural and isolated urban areas inL

    atinAmerica- A critical analysis, Water research (2010) 1-18

    y Jewel A.G. Gomes, Praveen Daida, Mehmet Kesmez, Michael Weir, Hector Moreno,

    Jose R. Parga, George Irwin, Hylton McWhinney, Tony Grady, Eric Peterson, David L.

    Cocke, Arsenic removal by electrocoagulation using combined Al-Fe electrode system

    and characterization of products, Journal of Hazardous Materials B139 (2007) 220-231

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    Continued

    y Ashima Baggaa, Shankararaman Chellam , Dennis A. Clifford, Evaluation of iron

    chemical coagulation and electrocoagulation pretreatment for surface water

    microfiltration, Journal of Membrane Science 309 (2008) 8293.

    y Ilona Heidmann, Wolfgang Calmano, Removal of Zn(II), Cu(II), Ni(II), Ag(I) and

    Cr(VI) present in aqueous solutions by aluminium electrocoagulation, Journal of

    Hazardous Materials 152 (2008) 934-941.

    y Isik Kabdasah, Tulin Arslan, Tugba Olmez-Hanci, Idli Arslan-Alaton, Olcay Tunnay,

    Complexing agent and heavy metal removals from metal plating effluent by

    electrocoagulation with stainless steel electrodes, Journal of Hazardous Materials, 165(2009) 838-845.

    y Colin Sullivan, Mark Tyrer, Christopher R. Cheeseman, Nigel J.D. Graham, Disposal

    of water treatment wastes containing arsenic- A review, Science of the total

    environment 408 (2010) 1770-1778.