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Combining submerged membrane technology with anaerobic and ...

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TMP (kPa)<strong>Combining</strong> UASB <strong>and</strong> MBR for the treatment of low-strength wastewater at environmental temperaturesThe low OLR applied to the MBR had a great impact on MLVSS concentration. Asmentioned before, temperature also played an important role in the <strong>membrane</strong>performance. COD removal efficiency in the methanogenic reactor increased <strong>with</strong>temperature, causing a diminution of the biodegradable COD supplied to the aerobic MBR,<strong>and</strong>, as a consequence, leading to a lower MLVSS. The beginning of period II coincided<strong>with</strong> the beginning of the springtime. Therefore, higher temperatures observed from periodII onwards provoked an improvement of COD removal in the methanogenic reactor <strong>and</strong>hence, a decrease in the OLR applied to the MBR (figure 4.2a). Therefore, the supply of aminimum OLR in the MBR was shown to be of prime importance in order to maintainMLVSS, <strong>and</strong> hence to control <strong>membrane</strong> fouling rate. In this sense, the proposed systemcould be modified in order to allow the feeding of a small fraction of the raw influent directlyinto the aerobic biofilm chamber, in order to assure a minimum biodegradable CODsupply, <strong>and</strong> thus maintain F/M ratio above 0.1 kgCOD·kgMLVSS -1·d -1 (Brepols, 2006;Judd, 2011), especially when operating at higher temperatures.12111098760 2 4 6 8 10 12Time (h)Figure 4.5. TMP profiles after a physical cleaning at 3.0 gMLVSS·L -1 () <strong>and</strong> 0.5gMLVSS·L -1 (•) during operating days 145 <strong>and</strong> 319, respectively.4.5. Conclusions The combination of UASB <strong>and</strong> aerobic MBR technologies in one single system oras a post-treatment, presented a good performance for the treatment of low-strengthwastewaters at ambient temperatures. Both proposed configurations presented an125

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