Abstract
Oily wastewater management became a critical consideration in recent years particularly in the oil and gas industry. This is due to the fact that oily wastewater contains harmful compounds such as oil and grease, and heavy metals that may harm the environment. Therefore, the aim of this study is to develop the composite reverse osmosis membrane in treating the oily wastewater from the specific oil refinery. The membrane consists of Polysulfone (PSF) as the main polymer, while Polyvinyl pyrrolidone (PVP) and bentonite acted as an additive and inorganic material. The solvent and non-solvent used are N-methyl pyrrolidone (NMP) and water. The reverse osmosis membrane was casted manually via phase inversion method. The oily wastewater sample was characterized in terms of conductivity, total dissolved solid (TDS), salinity, pH and temperature. Meanwhile, membrane performance studies were carried out in -terms of permeate flux and solute rejection at the operating pressure of 1.5 to 4.0 bar. The effect of the operating pressure and composition of PVP and bentonite towards membrane performances has been observed. The findings were supported by the membrane characterizations which consist of Fourier Transform Infrared (FTIR) analysis, contact angle measurement, Thermogravimetric (TGA) analysis, X-ray Diffraction (XRD) analysis and Field Emission Scanning Electron Microscopy (FESEM) analysis to investigate the change of the membrane properties with the presence of those two materials. Then, modeling was computed using Design Expert 6.0.10 software. From the experiments, it can be concluded that the addition of PVP and bentonite enhanced the membrane performance in terms of membrane permeate flux and solute rejection, and also membrane properties such as hydrophilicity, thermal behaviour, crystallinity and membrane structure thereby suggested that the PSF-PVP-bentonite membrane is viable to treat the oily wastewater from the specific oil refinery. The best membrane candidate is M23 membrane sample (10 wt% of PVP and 5 wt% of bentonite) that recorded excellent value of permeate flux and solute rejection at 0.00183 m3 /m2 .s and 99.05%. Meanwhile, at the optimum value of 4 bar (operating pressure) and, 9.86 wt% and 4.56 wt% for the composition of PVP and bentonite, the membrane was able to achieve the permeate flux value of 0.00171 m3 /m2 .s and the solute rejection of 97.01%.
Metadata
Item Type: | Thesis (Masters) |
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Creators: | Creators Email / ID Num. Shahruddin, Munawar Zaman 2009210622 |
Contributors: | Contribution Name Email / ID Num. Thesis advisor Syed Abdul Kadir, Sharifah Aishah ( Prof. Dr.) UNSPECIFIED |
Subjects: | T Technology > TP Chemical technology > Biotechnology T Technology > TP Chemical technology > Fuel > Biomass T Technology > TP Chemical technology > Oils, fats, and waxes |
Divisions: | Universiti Teknologi MARA, Shah Alam > Faculty of Chemical Engineering |
Programme: | Master of Science (Chemical Engineering) |
Keywords: | oily, wastewater, reverse osmosis |
Date: | December 2011 |
URI: | https://ir.uitm.edu.my/id/eprint/39736 |
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