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1 al fuel cell with high removal efficiency of chemical oxygen demand.
2 nal MBR, with removals of 97% of the soluble chemical oxygen demand, 97% NH3-N, and 91% of total bact
3 ion, the IPB system removed more than 92% of chemical oxygen demand, 98% of ammonium nitrogen, and 82
4                                     However, chemical oxygen demand, a common measure of gross residu
5                                              Chemical oxygen demand and dissolved organic carbon conc
6       A significant correlation of HAAs with chemical oxygen demand and THMs with FC was observed.
7 L(-1) and high biological elimination rates (chemical oxygen demand (COD) 90-95%, biological oxygen d
8                        Treatment efficiency (chemical oxygen demand (COD) and ammonia removal), Ag di
9               Greater than 95% reductions in chemical oxygen demand (COD) and ammonium ion were achie
10 quantified the 24-h and 7-day Pb toxicity to chemical oxygen demand (COD) and NH3-N removal, bacteria
11 he HiCS system oxidized only 10% of influent chemical oxygen demand (COD) and recovered up to 55% of
12                     Both MFCs removed 65-70% chemical oxygen demand (COD) at a hydraulic retention ti
13 paration method for the determination of the chemical oxygen demand (COD) in heterogeneous solid or s
14 re widely used and mainly contribute to high chemical oxygen demand (COD) in textile effluents.
15 cal sensors applied to the rapid analysis of chemical oxygen demand (COD) in urban waste waters.
16 g substrate, the SCMFC acted as a sensor for chemical oxygen demand (COD) in water.
17                Condensate pH was 6.2 and its chemical oxygen demand (COD) level was 36,000 ppm.
18 ays with synthetic acetate solution having a chemical oxygen demand (COD) of 320 mg/L.
19 y expressed as total organic carbon (TOC) or chemical oxygen demand (COD), though these parameters do
20 unds identified accounted for only 2.1 mg of chemical oxygen demand (COD)/L (16% of total SMP as COD)
21 on, with the highest solubilization (0.16 mg chemical oxygen demand (COD)/mg volatile solids (VS), at
22 s, freshwater consumption, discharge of COD (chemical oxygen demand) in effluent water, cumulative CO
23 0.05) with the influent total phosphorus and chemical oxygen demand instead of geographical factors (
24 of methanogens, which led to the decrease in chemical oxygen demand removal.
25 s C) with domestic wastewater having a total chemical oxygen demand (tCOD) of 210 +/- 11 mg/L.
26 m UFO-MBR investigation illustrated that the chemical oxygen demand, total nitrogen, and total phosph
27 oval efficiencies of total suspended solids, chemical oxygen demand, total phosphorus, and total nitr
28 val efficiency of total suspended solids and chemical oxygen demand was observed for recovered alumin

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