000 02226nam a2200253 a 4500
001 vtls000058661
003 KUKTEM
005 20251114204547.0
008 120315t2010 my a f m 001 0 eng d
020 _aTHE0004365(Local)
039 9 _a201905161116
_brohana
_y201203151120
_zida
040 _aUMP
090 _aTP248.M46 B34 2010 rs Bc.
100 0 _aBahrun Mohd Shakir
245 1 0 _aTreatment of industrial detergent wastewater via membrane separation /
_cBahrun Mohd Shakir
260 _aKuantan, Pahang :
_bUMP,
_c2010
300 _axi, 47 p . :
_bill. (some col.) ;
_c30 cm. +
_e1 CD-ROM
502 _aProject paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang - 2010
504 _aBibliography : p. 44-47
520 3 _aThis thesis presents the experimental study of the potential of Nanofiltration membrane in treating industrial detergent wastewater that contains high Linear Alkylbenzene Sulfonate (LAS). LAS is the most common synthetic anionic surfactant used in domestic and industrial detergents and can cause significant environmental problems. This study was focused on treated wastewater sample from FPG Oleochemical Sdb Bhd based on decreasing the parameters so it can comply with the regulation of Environment Quality Act (EQA), 1974 before it can release to discharge. LAS, Chemical Oxygen Demand (COD), Total Organic Carbon (TOC), Total Suspended Solid (TSS) and Turbidity were used as a parameters used in this study. The Polyamide Nanofiltration membrane performance was characterized by varying the Trans Membrane Pressure (TMP) 3, 4, 5 and 6 bars. The results showed that the optimum operating condition of the Nanofiltration membrane was achieved at TMP 6 bar. The removal percentage of the parameters is high which is more than 88%. However, only the Turbidity and TSS has achieved the EQA regulation. It is concluded that the wastewater from the production of Dynamo in FPG Oleochemical Sdn Bhd can be fully treated by using Nanofiltration membrane in addition some pre treatment or furthertreatment.
650 0 _aMembrane separation
650 0 _aSewage
_xPurification
999 _aVIRTUA40
_c4138
_d4144
999 _aVTLSSORT0080*0200*0400*0900*1000*2450*2600*3000*5020*5040*5200*6500*6501*9992