Page 299 - Materials Chemistry, Second Edition
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280                         Life Cycle Assessment of Wastewater Treatment


                                      Inputs (materials, energy)


                                               Biogas                Recovered
                                                                     electricity
                                                                     and heat
            Urban wastewater
                          Anaerobic
                           tank
                                        Membrane  E uent  Methane  E uent
              Carbon source                             recovery
                                          unit






                               Digested sludge



                                           Outputs

           FIGURE 13.2  Scheme of SAnMBR process for urban WWTPs.


           the  submerged anaerobic membrane bioreactor (SAnMBR) technology, recently
            explored as a promising technology for urban wastewater treatment.
              Pretel et al. (2013) report an environmental study of SAnMBR technology at
            different temperatures using LCA analysis. The process scheme is illustrated in
            Figure 13.2.
              The reported SAnMBR system is constituted by an anaerobic reactor connected
            to two membrane tanks, which include commercial ultrafiltration membranes. The
            plant operates with an SRT of 70 days, and the studied temperatures are 20 and
            30°C.
              The following system boundaries are considered in that work in the context of
           LCA evaluation:

              •  The wastewater treatment process is included. The contribution of the
                stages involved in this phase to the environmental impact is decisive for
                LCA studies.
              •  The operating phase is also included, as it significantly contributes to envi-
                ronmental impact (the construction phase, including membrane investment
                cost, is not considered).
              •  Final effluent composition is determined to evaluate whether nutrient recov-
                ery is possible.
              •  Pre-treatment processes are not included in this LCA analysis, because they
                are well known for all the WWTP LCA studies.
              •  The demolition phase is not taken into account, as it has been demonstrated
                that it shows a negligible contribution.
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