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42                          Life Cycle Assessment of Wastewater Treatment




                 With GHG



              Without GHG


                       0.00      0.15      0.30      0.45      0.60      0.75
                                                       3
                                          GWP (kg CO  [eq]/m )
                                                  2


                 With GHG



              Without GHG

                      0.00      0.15       0.30      0.45      0.60      0.75
                                                       3
                                          GWP (kg CO  [eq]/m )
                                                  2
                              Sluge management  Sluge line  Secondary treatment
                              Primary treatment  Pretreatment


           FIGURE 3.4  Contribution to GWP in scenarios with GHG measurements.

           technologies based on biological and/or chemical processes from an environmental
           perspective by Coats et al. (2011), who highlighted the benefits of biological treat-
           ments over chemical processes.
              Rodriguez-Garcia et al. (2011) performed a broader analysis of 24 WWTPs,
           which were classified into six types according to their quality requirements for
           their final discharge or reuse. This report introduced the novelty of using two
           different FUs: one based on volume (cubic meters) and the other on eutrophica-
           tion reduction (kilograms PO 4 3−  eq. removed). The FU of kilograms PO 4 3−  eq
           removed reflects the real objective of a WWTP and the sustainability among the
           different options. Those WWTPs designed for organic matter removal showed
           better performance in both environmental and economic terms if the volume was
           used as the FU, whereas more complex types such as reuse plants showed vari-
           able results: lower eutrophication but higher cost and global warming. The use
           of the second FU showed the superior performance of those configurations that
           allowed water reuse.
              A stream with high characteristic values of N and P is the centrate that comes
           from the anaerobic digester. Nitritation, Anammox, and nitrite shortcut technologies
           presented lower environmental impacts than struvite crystallization (Rodriguez-
           Garcia et al., 2014a). However, when the three options are presented in their context
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