Thesis - faculty.ait.ac.th - Asian Institute of Technology
Thesis - faculty.ait.ac.th - Asian Institute of Technology
Thesis - faculty.ait.ac.th - Asian Institute of Technology
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Table 2.8 Summary <strong>of</strong> Biokinetic Coefficient <strong>of</strong> Activated Sludge Process for Landfill<br />
Le<strong>ac</strong>hate Treatment<br />
So(BOD5)<br />
(mg/L)<br />
k<br />
(d -1 )<br />
Ks<br />
(mg/L)<br />
Y<br />
(mg/mg<br />
)<br />
kd<br />
(d -1 )<br />
19<br />
θc<br />
(d)<br />
T<br />
(°C)<br />
Reference<br />
36,000 0.75 200.0 0.33 0.0002 6.5 23 to 25 Ulo<strong>th</strong> and<br />
5<br />
Mavinic, 1977<br />
15,800* 0.6 175.0 0.40 0.050 - 22 to 24 Cook and<br />
Foree, 1974<br />
13,640 0.77 20.4 0.39 0.022 3.6 23 to 25 Zapf –Gilje and<br />
0.71 29.5 0.63 0.075 - 16 Mavinic, 1981<br />
0.46 14.6 0.50 0.028 - 9 Graham and<br />
0.29 11.8 0.43 0.008 7.5 5 Mavinic, 1979<br />
8,090 1.16 81.8 0.49 0.009 1.8 22 to 23 Wong and<br />
1.12 63.8 0.51 0.018 1.8 15 Mavinic, 1984<br />
0.51 34.6 0.51 0.006 4.0 10<br />
0.34 34.0 0.55 0.002 5.4 5<br />
1,000 4.50 99.0 0.59 0.040 0.42 22 to 23 Lee, 1979<br />
365 1.80 182.0 0.59 0.115 - 21 to 25 Palit and<br />
Qasim, 1977<br />
3,000 - - 0.44 - 1 to 20 10 Robinson and<br />
Marais, 1983<br />
2,000 0.46 180.0 0.50 0.100 2 to 10 25 Gaudy, et al.,<br />
1986<br />
Domestic 2-10 25-100 0.4-0.8 0.025- - - Tchobanoglous,<br />
Wastewater<br />
0.075<br />
et al., 2003<br />
So = BOD5 (* COD) k = substrate removal rate Ks = half-velocity constant<br />
Y = yield coefficient kd = endogenous decay coefficient Θc = solid retention time<br />
T = temperature<br />
Keenan, et al. (1984) investigated <strong>th</strong>e combined physico-chemical process wi<strong>th</strong><br />
<strong>ac</strong>tivated sludge process. It was observed <strong>th</strong>at <strong>th</strong>e reduction in ammonia by stripping and<br />
neutralization wi<strong>th</strong> H2SO4 and H3PO4 after <strong>th</strong>at entered to <strong>ac</strong>tivated sludge process. The<br />
organic matter in terms <strong>of</strong> BOD was reduced 99% and <strong>th</strong>e corresponding COD removal<br />
was 95%. The effluent BOD to COD ratio was 0.16. The reduction in ammonia was 90%<br />
and heavy metals removal ranged from 27% to 75%.<br />
Dzombak, et al. (1990) had studied <strong>th</strong>e treatment <strong>of</strong> le<strong>ac</strong>hate in an extended aeration<br />
system. The BOD/COD ratio <strong>of</strong> <strong>th</strong>e le<strong>ac</strong>hate was below 0.1 which is a char<strong>ac</strong>teristic <strong>of</strong> old<br />
landfill le<strong>ac</strong>hate containing mainly refr<strong>ac</strong>tory organic compounds. Different mean-cell<br />
residence times from 15 to 60 days were investigated. It was observed <strong>th</strong>at maximum<br />
COD removal <strong>of</strong> 40% could be <strong>ac</strong>hieved wi<strong>th</strong> mean-cell residence time <strong>of</strong> 60 days. This<br />
suggested <strong>th</strong>at le<strong>ac</strong>hate from young landfills wi<strong>th</strong> organic matter containing high volatile<br />
<strong>ac</strong>ids can be more easily treated wi<strong>th</strong> an <strong>ac</strong>tivated sludge process <strong>th</strong>an old landfill le<strong>ac</strong>hate.<br />
Doyle, et al. (2001) performed <strong>th</strong>e sludge char<strong>ac</strong>terization studies in <strong>th</strong>e nitrification<br />
process used for ammonia removal in an “old” landfill le<strong>ac</strong>hate. Whilst most researchers<br />
(Knox, 1985; Robinson and Maris, 1983; Str<strong>ac</strong>han, et al., 2000) reported poor settleability