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Thesis - faculty.ait.ac.th - Asian Institute of Technology

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obtain high treatment efficiencies <strong>of</strong> 76% TKN, 60% COD, 84% phosprorus removal at<br />

HRT <strong>of</strong> 7 hours and wi<strong>th</strong> a F/M ratio <strong>of</strong> 1.73 g COD/g MLSS.d. The maximum specific<br />

grow<strong>th</strong> rate <strong>of</strong> C. utilis was found to be 0.19 h -1<br />

Hu (1989) used ten different yeast strains in cultures to treat vermicelli wastewater<br />

which contained BOD ranging from 24,000 to 44,000 mg/L and high concentration <strong>of</strong><br />

starch, l<strong>ac</strong>tic <strong>ac</strong>id and protein. Based on <strong>th</strong>e ability <strong>of</strong> starch degradation, protein<br />

hydrolysis and l<strong>ac</strong>tic <strong>ac</strong>id tolerance, <strong>th</strong>ese yeast strains were screened from 391 colonies<br />

isolated from soil samples. Most <strong>of</strong> <strong>th</strong>em could grow well wi<strong>th</strong> pH range <strong>of</strong> 3.0-5.0, 4.0<br />

being <strong>th</strong>e optimum. The results shows <strong>th</strong>at <strong>th</strong>e two strains could reduce soluble COD by<br />

92% at HRT <strong>of</strong> 7 days, F/M ratio <strong>of</strong> 0.48 g COD/g MLSS.d and VLR <strong>of</strong> 1.03 kg<br />

COD/m 3 .d. Due to <strong>th</strong>e poor settling ability <strong>of</strong> yeasts, <strong>th</strong>ey could not be flocculated or<br />

settled as in a conventional <strong>ac</strong>tivated sludge process and were easily washed out wi<strong>th</strong> <strong>th</strong>e<br />

effluent. Therefore, <strong>th</strong>e HRT in <strong>th</strong>is process have to keep long and same as <strong>th</strong>e SRT. The<br />

au<strong>th</strong>or postulated <strong>th</strong>at <strong>th</strong>e fungi contamination prevented <strong>th</strong>e formation <strong>of</strong> yeast flocs.<br />

Chigusa, et al. (1996) used nine different strains <strong>of</strong> yeasts capable <strong>of</strong> decomposing<br />

<strong>th</strong>e oil to treat wastewater from oil manuf<strong>ac</strong>turing plants. A pilot scale yeast treatment<br />

system had been run for one year. According to <strong>th</strong>e results, 10,000 mg/L <strong>of</strong> hexane extr<strong>ac</strong>ts<br />

in <strong>th</strong>e raw wastewater were reduced by <strong>th</strong>e yeast mixture to about 100 mg/L.<br />

Elmaleh et al.(1996) investigated <strong>th</strong>e yeast treatment <strong>of</strong> highly concentrated <strong>ac</strong>idic<br />

wastewater from <strong>th</strong>e food processing industry. The strain Candida utilis was cultured in<br />

continuously completed mixed re<strong>ac</strong>tors. This system did not have a separate settling tank;<br />

<strong>th</strong>e SRT and HRT <strong>of</strong> <strong>th</strong>e system were identical. A mixture <strong>of</strong> <strong>ac</strong>etic <strong>ac</strong>id, propionic and<br />

butyric <strong>ac</strong>id was <strong>th</strong>e carbon source <strong>of</strong> feed wastewater. The pH was maintained at 3.5 to<br />

prevent any b<strong>ac</strong>terial contamination. The TOC removal obtained was 97% at high loading<br />

rates (30 kg TOC/m 3 .d). The grow<strong>th</strong> yield and maximum specific grow<strong>th</strong> rate <strong>of</strong> yeasts<br />

were similar to <strong>th</strong>ose for conventional <strong>ac</strong>tivated sludge (µmax = 0.5 h - ; Y = 0.85-1.05 kg<br />

SS/kg TOC for <strong>ac</strong>etic <strong>ac</strong>id).<br />

Olive mill wastewater normally contains high concentration <strong>of</strong> fats, sugars, phenols,<br />

volatile fatty <strong>ac</strong>ids which contribute to a very high COD concentration (100,000-200,000<br />

mg/L). Scioli and Vollaro (1997) reported <strong>th</strong>at Yarrowia lipolytica cultured in aerated<br />

fermenter was capable <strong>of</strong> reducing <strong>th</strong>e COD level <strong>of</strong> olive oil processing wastewater by<br />

80% in 24 h. Fats and sugars were completely assimilated while me<strong>th</strong>anol and e<strong>th</strong>anol<br />

were present. The effluent had a pleasant smell due to <strong>th</strong>e presence <strong>of</strong> <strong>th</strong>ese compounds.<br />

The au<strong>th</strong>ors asserted <strong>th</strong>at a possible appro<strong>ac</strong>h for pollution reduction in olive-oil-producing<br />

countries is to use membrane to filter effluent before discharging into <strong>th</strong>e sewage system.<br />

Useful biomass (40% protein) and valuable lipase enzyme could also be obtained in <strong>th</strong>is<br />

process.<br />

Arnold, et al. (2000) investigated <strong>th</strong>e ability <strong>of</strong> selected yeast strains (C. utilis and<br />

Gal<strong>ac</strong>tomyces geotrichum) to purify silage wastewater containing high COD concentration<br />

<strong>of</strong> 30,000 to 80,000 mg/L by using <strong>th</strong>e shaker-flask. High removal efficiencies <strong>of</strong> COD<br />

(74-95%), VFA (85-99%) and phosphate (82-99%) were obtained after 24 hrs and some<br />

ammonia was also removed. During treatment, pH rose from initial values <strong>of</strong> 3.7-5.8 to<br />

8.5-9.0. This was presumably due to removal <strong>of</strong> l<strong>ac</strong>tic <strong>ac</strong>id and VFAs. An efficient<br />

removal <strong>of</strong> P from <strong>th</strong>e system could lead to <strong>th</strong>e shortage <strong>of</strong> phosphorus.<br />

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