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999			_c96743 _d96749
003			MY-KuUP
005			20251125110016.0
006			t||||fr|||| 000 0
008			220217s2020 my a|||fr|||| 000 0 eng d
020			_aTHE0009112(Local) _qhardback
040			_aUMP _beng _cUMP _erda
090			_aFTKKP .T64 2020 r Thesis
100	1		_aToh Kang Yang, _eauthor.
245	1	0	_aCFD and techno-economic modelling of the effect of feed spacer on reverse osmosis membrane performance / _cToh Kang Yang
264		1	_aKuantan, Pahang : _bUMP, _c2020
264		4	_c© 2020
300			_axvi, 97 pages : _billustrations (some color) ; _c30 cm. + _e1 CD-ROM
336			_atext _2rdacontent
337			_aunmediated _2rdamedia
337			_acomputer _2rdamedia
338			_avolume _2rdacarrier
338			_acomputer disc _2rdacarrier
347			_atext file _bPDF _2rda
500			_aFaculty of Chemical and Process Engineering Technology
502			_aThesis (Master of Science) -- Universiti Malaysia Pahang – 2020
504			_aIncludes bibliographical references
520	3		_aReverse osmosis (RO) processes are among the most popular solutions for brackish water and seawater desalination. One of the major issue faced in RO membrane is concentration polarisation (CP). As feed spacer geometry has major impacts on the flow and CP in the spiral wound membrane (SWM), optimizing its geometry remains an ongoing research goal. This thesis systematically investigates the effect of feed spacer geometry on RO membrane performance through computational fluid dynamics (CFD) and technoeconomic modelling. For CFD study, two different spacer designs are considered: 1) spacer with perforations and 2) spacer with different floating characteristics. The main finding from the spacer perforation is that it does not improve mass transfer for the cases simulated using conventional spacers. It was also shown that spacers with larger perforation decrease mass transfer by over 10% due to weakening of the flow velocity and suppression of vortex shedding. The simulation results also reveal that the floating ratio (Rf) is not a determining factor for permeate flux enhancement. This is because the transport mechanism is more dependent on other geometric characteristics, such as a 2 -or 3-layer design. The techno-economic modelling reveals that advanced spacers are more effective than conventional spacers in improving flux in the region close to the inlet for high-permeance membranes. This is due to the fast decrease in feed flow along the channel. This thesis found that an increase in membrane permeance (up to 10 L m−2h−1 bar−1) can reduce total processing cost of SWRO and BWRO by 7.5% and 32%, respectively regardless of spacer type used. The main finding from technoeconomic analysis is that improving spacer design is more crucial than increasing permeance at same recovery.
610	2	0	_aFaculty of Chemical and Process Engineering Technology _xDissertations
650		0	_aUniversities and colleges _xDissertations
650		0	_aTheses
942			_2lcc _cTHESIS