Micropollutant abatement with UV/H2O2 oxidation or low-pressure reverse osmosis? A comparative life cycle assessment for drinking water production
Christine Roth
<p><span class="fontstyle0">Micropollutants (MP) are undesired in drinking water. Advanced oxidation processes (AOP) or low-pressure reverse osmosis membrane filtrations (LPRO) can be used to remove them during the water purification process. For a specific case, two treatment scenarios were compared with a life cycle assessment (LCA), using three impact assessment methods (Ecological Scarcity 2013, ILCD 2011, EDIP 2003). Scenario 1 (AOP-based) was a UV/H</span><span class="fontstyle0" style="font-size:6pt;">2</span><span class="fontstyle0">O</span><span class="fontstyle0" style="font-size:6pt;">2 </span><span class="fontstyle0">oxidation with a subsequent granular activated carbon (GAC) filter to remove excess H</span><span class="fontstyle0" style="font-size:6pt;">2</span><span class="fontstyle0">O</span><span class="fontstyle0" style="font-size:6pt;">2 </span><span class="fontstyle0">before soil infiltration. Scenario 2 (LPRO-based) was a side-stream treatment with an ultrafiltration (UF) and low-pressure reverse osmosis (LPRO) filtration before soil infiltration and the LPRO retentate was treated with O</span><span class="fontstyle0" style="font-size:6pt;">3</span><span class="fontstyle0">/H</span><span class="fontstyle0" style="font-size:6pt;">2</span><span class="fontstyle0">O</span><span class="fontstyle0" style="font-size:6pt;">2 </span><span class="fontstyle0">and subsequent granular activated carbon (GAC) filter before discharge back into Rhine. Sensitivity analyses were performed on the relevant contributors to evaluate the robustness of the results. LCA results showed that in the base-line scenario (electricity from renewable energy sources) the LPRO-based treatment had notably fewer environmental impacts than the AOP-based treatment, which was confirmed with three impact assessment methods. Key contributors to the impacts were mostly operating resources, i.e., electricity, H</span><span class="fontstyle0" style="font-size:6pt;">2</span><span class="fontstyle0">O</span><span class="fontstyle0" style="font-size:6pt;">2</span><span class="fontstyle0">, liquid O</span><span class="fontstyle0" style="font-size:6pt;">2 </span><span class="fontstyle0">for ozone generation and GAC, but also construction resources in the LPRO process. The electrical energy source was decisive for the results: with a share of renewable energy sources </span><span class="fontstyle2"><</span><span class="fontstyle0">80%, the AOP-based treatment was the better option due to its lower specific energy demand. The optimization of treatment conditions, such as lower H</span><span class="fontstyle0" style="font-size:6pt;">2</span><span class="fontstyle0">O</span><span class="fontstyle0" style="font-size:6pt;">2 </span><span class="fontstyle0">concentration at an increased UV fluence; different H</span><span class="fontstyle0" style="font-size:6pt;">2</span><span class="fontstyle0">O</span><span class="fontstyle0" style="font-size:6pt;">2</span><span class="fontstyle0">:O</span><span class="fontstyle0" style="font-size:6pt;">3 </span><span class="fontstyle0">molar ratios; or extended GAC utilization time could influence the environmental impact within a range of </span><span class="fontstyle3">±</span><span class="fontstyle0">10</span><span class="fontstyle4">–</span><span class="fontstyle0">30%. Environmental benefits, i.e. the reduction of potential hazardous effects of 21 MPs, were determined with EDIP 2003 and USEtox for both treatment scenarios. The estimated benefits were negligible in comparison to the environmental burden caused by the treatments, thus would not be justified from a global LCA impact-benefit perspective. However, because of several uncertainties and lack of data, the inclusion of treatment benefits in LCAs for drinking water purification requires further research.</span>
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