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Subsurface Iron and Arsenic Removal

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<strong>Subsurface</strong> iron <strong>and</strong> arsenic removal for drinking water treatment in Bangladesh<br />

2<br />

[PO 4<br />

-3 ] in mmol.L-1<br />

0.05<br />

0.04<br />

0.03<br />

0.02<br />

0.01<br />

0<br />

0<br />

0 100,000 200,000 300,000 400,000<br />

0.1<br />

0.08<br />

0.06<br />

0.04<br />

0.02<br />

[As] in µmol.L -1<br />

did not exceed 0.01 mmol.L -1 , which is far below the<br />

concentrations measured during cycle 1 (Figure 2.10).<br />

<strong>Arsenic</strong> concentrations remained below 0.1 µmol.L -1<br />

<strong>and</strong> were thus also not found to remobilize after SIR<br />

was stopped at WTP Lekkerkerk.<br />

Pumped volume (m 3 )<br />

Conclusions<br />

Phosphate <strong>Arsenic</strong><br />

Figure 2.13 Phosphate <strong>and</strong> arsenic measurements once subsurface<br />

iron removal had stopped after 18 injectionabstraction<br />

cycles (WTP Lekkerkerk)<br />

suddenly change (e.g., pH), which is not likely in a<br />

normal well field. Exchange of the adsorbed anion with<br />

other passing anions with higher affinity could promote<br />

the release of retained arsenic or phosphate from the soil<br />

grain surface. However, once groundwater conditions<br />

stabilize around the stopped SIR well no large water<br />

quality variations are expected. Re-crystallization<br />

of (amorphous) iron or manganese oxides to oxides<br />

of higher crystallinity is a slow process, but could<br />

release small amounts of trace elements. Although<br />

Figure 2.13 shows some variations in the arsenic <strong>and</strong><br />

phosphate concentrations, it is obvious that high peak<br />

concentrations are not observed. It may be concluded<br />

that the retained phosphate was not mobilized to<br />

elevated solute concentrations once injection was no<br />

longer applied. Phosphate concentrations generally<br />

During subsurface iron removal at WTP Lekkerkerk,<br />

iron, manganese, phosphate <strong>and</strong> arsenic were measured<br />

to be retained in the aquifer at varying efficacies. SIR<br />

technology was found to improve in efficacy with<br />

every successive cycle, which correlates well with<br />

findings in other literature. No peak concentrations<br />

of the studied constituents were observed in the<br />

abstracted groundwater once SIR was stopped <strong>and</strong><br />

therefore not threatening the sustainability of the<br />

groundwater production well. pH was shown to be the<br />

most pronounced water quality parameter determining<br />

the efficacy of SIR, the operational V/Vi ratio more<br />

than doubled between pH 7.0 <strong>and</strong> 7.4 at WTP Corle.<br />

The experiences in the Netherl<strong>and</strong>s have shown<br />

that subsurface iron removal is an effective, robust<br />

<strong>and</strong> sustainable iron removal technology with great<br />

potential for worldwide application.<br />

34

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