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Download file - Ayuntamiento de Zaragoza

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4.00E-033.50E-03ExperimentalMo<strong>de</strong>l3.00E-032.50E-032.00E-031.50E-031.00E-035.00E-040.00E+00151101151201251301351401E(t)451501551601651701751801851901Time (min)FIG.42. Experimental and mo<strong>de</strong>l RTD curves of the aeration tank.FIG.43. Mo<strong>de</strong>l of the aeration tank. V1 = 80 m 3 , V2 = 101 m 3 , V3 = 100 m 3 , V4 = 100 m 3 ,V5 = 97.7 m 3 , V6 = 106.7 m 3 .The mo<strong>de</strong>l consists of five perfect mixers in series with back mixing and connected with a plugflow reactor at the beginning. After the injection point, the incoming wastewater passes through anarrow duct before it enters into the series of tanks through small holes. Because of this reason, a plugflow reactor is used between no<strong>de</strong> no. 1 and no<strong>de</strong> no. 2. Back mixing ratio of the tanks connected inseries is found to be 2.7.The volume of the aeration tank was 567.5 m 3 and the volumetric flow rate during theexperiment was 2.08 ± 0.08 m 3 /min. It gives the theoretical mean resi<strong>de</strong>nce time of 272.8 min. Theexperimental mean resi<strong>de</strong>nce time of the unit was estimated as 271.9 min with a very small <strong>de</strong>advolume (0.32%). Therefore, almost negligible amount of <strong>de</strong>ad volume was estimated in the aerationtank. This is due to the vigorous mixing process insi<strong>de</strong> the aeration tank.Due to high gas flow rate, tracer experiments conducted in aeration tank have shown that waterand sludge have generally similar flow behavior. Radiotracer investigation in aeration tank has shownthat the fluid flow can be mo<strong>de</strong>led either by perfect mixing cells in series or by perfect mixing cells inseries with back mixing. The number of mixing cells found by RTD mo<strong>de</strong>ling was J=5, in fact numberJ is a function of both gas and water flowrates as well as of the geometrical configuration. The resultsof this experiment showed that the aeration tank was achieving the <strong>de</strong>signed resi<strong>de</strong>nce time and wasworking efficiently as far as resi<strong>de</strong>nce time is concerned.(c) Secondary clarifierThe experimental RTD curve obtained at the output of the secondary clarifier is given in theFig. 44. Figure 45 shows the best mo<strong>de</strong>l found using RTD software simulation.47

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