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Combining submerged membrane technology with anaerobic and ...

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Chapter 22.2.3. Sludge volumetric indexThe sludge volumetric index (SVI) determination is defined in the St<strong>and</strong>ard Methodsfor the Examination of Water <strong>and</strong> Wastewater (APHA-AWWA-WPCF, 1998) as the volumein mL occupied by 1 g of a suspension after 30 min settling.2.2.4. Sludge settling rateThe sludge settling rate (SSR) was determined by measuring the velocity ofsedimentation of the mixed liquor (1 g·L -1 ) in a 100 mL measuring cylinder.2.3. Gas phaseTo measure biogas composition a gas chromatograph HP 5890 Series II <strong>with</strong> thecolumn of Porapack Q 80/100 2m x 1/8” (SUPELCO) is used. 1 mL of well-mixed sampleshould be injected through the septum at the following conditions: oven temperature(column) at 35 °C; injector <strong>and</strong> the detector temperature at 110 °C. The obtained peakscorrespond to the percentage of the N 2, CH 4, CO 2 <strong>and</strong> H 2S content in the sample. Biogasproduction was measured using a Milli GasCounter MGC-10 (Ritter, Germany), whichbasically consists in a tilting body inside a container <strong>with</strong> a special packing liquid. Theentrance of gas bubbles led the tilting body to change its position. Each change is counted<strong>with</strong> a magnet <strong>and</strong> a counter <strong>and</strong> the internal calibration give the gas flow in the display.2.4. Membrane performance2.4.1. Flux <strong>and</strong> permeabilityMembrane flux can be calculated as:where:J: flux expressed in L·m -2 ∙h -1 ,Q: flow expressed in L·h -1 ,A: <strong>membrane</strong> area expressed in m 2 .Therefore, permeability can be calculated as:eq. 2.676

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