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Conditioning and dewatering of sludge from a Bangkok waterworks | |
Author | Teerawat Luangurai |
Call Number | AIT Thesis no.EV-90-8 |
Subject(s) | Sewage--Purification--Activated sludge process |
Note | A thesis submitted in partial fulfillment of the requirements for the degree of Master of Engineering, School of Environment, Resources and Development |
Publisher | Asian Institute of Technology |
Abstract | This study aimed to investigate the use of sand-drying beds in dewatering sludges generated from the Bangkhen Water Treatment Plant of the Metropolitan Waterworks Authority(MWA) ,Thailand. The combined sludges from the clarifiers and filter backwashing were collected and transported to the Asian Institute of Technology (AIT) for analysis and experiments. The Buchner funnel tests revealed the optimum dosages of lime, Magnafloc LT26 and ferric chloride to be 16, 0.06 and 8 % TS, respectively. With these dosages, the above conditioners yielded the maximum sludge solids of 11.81, 14.81 and 4.31 kg/(m2 .h) respectively, while the ·nonconditioned sludges had the maximum sludge solids yield of 2.83 kg/(m2 .h). Rainfalls did not appear to significantly affect the performance of the sand-drying beds in dewatering the non-conditioned and conditioned sludges. This was due to the rapid development of cracks in the sludge cakes within one day of dewatering, where the rai~ water could pass through and became the filtrate. The experiments on sand-drying beds suggested that Magnafloc LT26 was a better conditioner than lime and ferric chloride in dewatering this sludge on sand-drying beds. The optimum sludge loading rate for the Magnafloc LT26 conditioned sludge was found to be 3. 27 kg/ (m2 . d), while for the non-conditioned , lime conditioned and ferric chloride conditioned sludge, the optimum solid loading rates were 2.73, 2.14 and 2.57 kg/(m2 .d), respectively. A comparison between the cost of using sand-drying beds and sludge lagoons (which are presently employed at the Bangkhen Water Treatment Plant) for dewatering indicated that it was more expensive to use sludge lagoons than sand-drying beds. For a comparison between the cost of non-conditioned and Magnafloc conditioned sludges on sand-drying beds, the Magnafloc LT26- conditioned sludge required less capital cost but more operation and maintenance cost than that of the non-conditioned sludge. |
Year | 1990 |
Type | Thesis |
School | School of Environment, Resources, and Development (SERD) |
Department | Other Field of Studies (No Department) |
Academic Program/FoS | Environmental Engineering and Management (EV) |
Chairperson(s) | Chongrak Polprasert |
Examination Committee(s) | Vigneswaran, Saravanamuthu ;Kiran Bhattarai |
Scholarship Donor(s) | Government of Australia |
Degree | Thesis (M.Eng.) - Asian Institute of Technology, 1990 |