ライフサイエンスコーパス: chemical oxygen demand

1 iomass, total and volatile suspended solids, chemical oxygen demand).

2 al fuel cell with high removal efficiency of chemical oxygen demand.

3 characterized by elevated concentrations of chemical oxygen demand (13.1-59.6 mg/L), biochemical oxy

4 thickness as well as the maximum removal of chemical oxygen demand (94.8%), linear alkylbenzenesulfo

5 nal MBR, with removals of 97% of the soluble chemical oxygen demand, 97% NH3-N, and 91% of total bact

6 ion, the IPB system removed more than 92% of chemical oxygen demand, 98% of ammonium nitrogen, and 82

7 However, chemical oxygen demand, a common measure of gross residu

8 , the main agricultural pollution emissions (Chemical Oxygen Demand, ammonia nitrogen, and agricultur

9 In concentrated centrate, 95% of the chemical oxygen demand and 93% of total PFAS were remove

10 Chemical oxygen demand and dissolved organic carbon conc

11 A significant correlation of HAAs with chemical oxygen demand and THMs with FC was observed.

12 Chemical oxygen demand, biological oxygen demand, and to

13 rbidity), TSS (total suspended solids), COD (chemical oxygen demand), BOD (biochemical oxygen demand)

14 on the precedent determinations, theoretical chemical oxygen demand (COD(th)) as well as theoretical

15 al suspended solids (TSS) < 30 mg L(-1), and chemical oxygen demand (COD) < 150 mg L(-1).

16 L(-1) and high biological elimination rates (chemical oxygen demand (COD) 90-95%, biological oxygen d

17 ce-to-water ratio (R(2) = 0.87), and between chemical oxygen demand (COD) and AA concentrations (R(2)

18 Treatment efficiency (chemical oxygen demand (COD) and ammonia removal), Ag di

19 Greater than 95% reductions in chemical oxygen demand (COD) and ammonium ion were achie

20 Traditional load-based indicators (Chemical Oxygen Demand (COD) and Biological Oxygen Deman

21 quantified the 24-h and 7-day Pb toxicity to chemical oxygen demand (COD) and NH3-N removal, bacteria

22 he HiCS system oxidized only 10% of influent chemical oxygen demand (COD) and recovered up to 55% of

23 Both MFCs removed 65-70% chemical oxygen demand (COD) at a hydraulic retention ti

24 With an average removal rate of 94.23% for Chemical Oxygen Demand (COD) compared to 88.76% for stan

25 For nearly a century, chemical oxygen demand (COD) has been widely used for as

26 paration method for the determination of the chemical oxygen demand (COD) in heterogeneous solid or s

27 re widely used and mainly contribute to high chemical oxygen demand (COD) in textile effluents.

28 cal sensors applied to the rapid analysis of chemical oxygen demand (COD) in urban waste waters.

29 g substrate, the SCMFC acted as a sensor for chemical oxygen demand (COD) in water.

30 ic loading rate (OLR) from 2.5 to 15 g total chemical oxygen demand (COD) L.d(-1).

31 Condensate pH was 6.2 and its chemical oxygen demand (COD) level was 36,000 ppm.

32 ay sludge retention time (SRT), matching the chemical oxygen demand (COD) loading rate to the removal

33 y for 88 weeks, with a mass balance based on chemical oxygen demand (COD) of 100 +/- 2% (COD(out)/COD

34 ays with synthetic acetate solution having a chemical oxygen demand (COD) of 320 mg/L.

35 The model was able to predict the chemical oxygen demand (COD) removal efficiency and meth

36 r the levelized cost and carbon intensity of chemical oxygen demand (COD) removal.

37 articularly from wastewater streams with low chemical oxygen demand (COD) to nitrogen (C/N) ratios.

38 onditions of initial pH (pH 4, 5, and 7) and chemical oxygen demand (COD) to nitrogen (COD/N) ratio o

39 , pH, EC time and EO time, on the removal of chemical oxygen demand (COD), colour, turbidity, and tot

40 ), salinity, biological oxygen demand (BOD), chemical oxygen demand (COD), electrical conductivity (E

41 on to their impact on key indicators such as Chemical Oxygen Demand (COD), NH(4)(+)-N, Total Phosphor

42 y expressed as total organic carbon (TOC) or chemical oxygen demand (COD), though these parameters do

43 unds identified accounted for only 2.1 mg of chemical oxygen demand (COD)/L (16% of total SMP as COD)

44 on, with the highest solubilization (0.16 mg chemical oxygen demand (COD)/mg volatile solids (VS), at

45 y, and a VFA yield of 0.55 +/- 0.12 g VFA as chemical oxygen demand g volatile solids (VS)(fed)(-1) w

46 s, freshwater consumption, discharge of COD (chemical oxygen demand) in effluent water, cumulative CO

47 0.05) with the influent total phosphorus and chemical oxygen demand instead of geographical factors (

48 of methanogens, which led to the decrease in chemical oxygen demand removal.

49 ncentrations significantly decreased soluble chemical oxygen demand (S(COD)) removal efficiency (11%

50 The response variables analyzed were soluble chemical oxygen demand (sCOD) and volatile suspended sol

51 nt research aims to predict effluent soluble chemical oxygen demand (SCOD) in anaerobic digestion (AD

52 s C) with domestic wastewater having a total chemical oxygen demand (tCOD) of 210 +/- 11 mg/L.

53 m UFO-MBR investigation illustrated that the chemical oxygen demand, total nitrogen, and total phosph

54 oval efficiencies of total suspended solids, chemical oxygen demand, total phosphorus, and total nitr

55 val efficiency of total suspended solids and chemical oxygen demand was observed for recovered alumin