| 000 | 03879cas|a2200421 i 4500 | ||
|---|---|---|---|
| 005 | 20260817162954.0 | ||
| 008 | 230399s1993 th uzm rtt 00| a1eng d | ||
| 035 | _a.b10089238 | ||
| 099 | 9 | _aAIT Thesis no.EV-93-26 | |
| 100 | 1 | _aWerellagama, D. R. Induka B. | |
| 245 | 1 | 0 | _aApplication of the floto filter unit for contact flocculation filtration of surface waters |
| 260 |
_aBangkok : _bAsian Institute of Technology, _c1993 |
||
| 300 |
_a141 leaves + _e1 online resource |
||
| 490 | 1 |
_aThesis ; _vno. EV-93-26 |
|
| 500 | _aA thesis submitted in partial fulfillment of the requirement for the degree of Master of Engineering | ||
| 502 | _aThesis (M.Eng.) - Asian Institute of Technology, 1993 | ||
| 520 | _aLaboratory scale experiments were carried out in contact flocculation filtration using a dual media filter. The objective of the research was to find an optimum synthetic media combination which would give acceptable quality water under varying conditions while maintaining a low headloss. The media was lighter than water hence the bed was floating. Since coarse media remained at the bottom the flow direction was upflow which had the added advantage that the flow was in the direction of grain compression. Polypropylene and Polystyrene were selected as the optimum combination of media which due to their large . density difference did not intermix even under severe agitation. Spherical fine media performed better than angular fine media giving lower headloss and better effluent quality. The dual media combination and the higher rates of filtration are in line with the current trends in the water industry. The influent concentrations were kept constant and the flow velocity and filter media size were varied. The headloss variation along the filter, the influent quality to the two filter layers and the effluent quality were studied. The filter performed for over 40 hours producing acceptable quality water at conventional rapid sand filtration rates, also having low headloss development. Another major advantage was the ease and economy in backwashing. The filter media did not mix even during or after backwashing, thereby eliminating the most common problem encountered in conventional multi media filters. The Floto Filter operation was compared with upflow sand filtration. The headloss development curves for Floto filter showed a characteristic shape easily identifiable from that for sand. The existing mathematical model was able to predict the headloss profile but the concentration profile was not predicted. The necessity of particle size data for mathematical modelling of filtration of heterodisperse suspensions is emphasized. | ||
| 650 | 0 |
_aWater _xPurification _xFiltration |
|
| 700 | 1 |
_aVisvanathan, C., _eChairperson |
|
| 700 | 1 |
_aFujii, Shigeo, _eExamination committee |
|
| 700 | 0 |
_aSamorn Muttamara, _eExamination Committee |
|
| 710 | 2 |
_aSwedish International Development Agency (SIDA), _eScholarship donor |
|
| 810 | 2 |
_aAsian Institute of Technology. _tThesis ; _vno. EV-93-26 |
|
| 856 |
_3Full-Text _uhttp://203.159.5.9/ait-thesis/detail.php?q=B16676 |
||
| 907 |
_a.b10089238 _bmnait _cx |
||
| 902 | _a240411 | ||
| 998 |
_b2 _c951012 _dm _ea _fx _g0 |
||
| 945 | _lmnait | ||
| 945 | _lmnait | ||
| 945 | _lmnarc | ||
| 942 | _c20 | ||
| 942 | _c22 | ||
| 942 | _c40 | ||
| 909 |
_aBarcode : 30050120806087 _bCREATED : 1994-05-16 _cRECORD # : i10095366 _dLPATRON : 0 _eLCHKIN : - _f# RENEWALS : 0 _g# OVERDUE : 0 _hIUSE3 : 0 _iTOT CHKOUT : 0 _jTOT RENEW : 0 |
||
| 909 |
_aBarcode : a _bCREATED : 1995-10-13 _cRECORD # : i10095378 _dLPATRON : 0 _eLCHKIN : - _f# RENEWALS : 0 _g# OVERDUE : 0 _hIUSE3 : 0 _iTOT CHKOUT : 0 _jTOT RENEW : 0 |
||
| 909 |
_aBarcode : 30050160055728 _bCREATED : 2016-11-05 _cRECORD # : i12975187 _dLPATRON : 0 _eLCHKIN : - _f# RENEWALS : 0 _g# OVERDUE : 0 _hIUSE3 : 0 _iTOT CHKOUT : 0 _jTOT RENEW : 0 |
||
| 999 |
_c6880 _d6880 |
||