02150nam a2200253 a 4500 vtls000031063 KUKTEM 20251114204451.0 080821t2008 my a f m 000 0 eng|d THE0004433(Local) 201905161527 rohana 201107132227 VLOAD 200908141511 VLOAD 200908141441 VLOAD 200808211017 ida84 UMP TP248.25.M46 N87 2008 rs Thesis Nur Sharlinawati Md. Said Separation of lysozyme using ultrafiltration membrane, effect of ph and ionic strength on flux and rejection / Nur Sharlinawati Md. Said Separation of lysozyme using ultrafiltration membrane, effect of ph and ionic strength on flux and rejection [electronic resource] Kuantan, Pahang : UMP, 2008 100 p. : ill. ; 30 cm. + 1 computer disc Project paper (Bachelor of Chemical Engineering) --- Universiti Malaysia Pahang - 2008 The separation of solid, macro molecule and non-dissolve particle results from the fermentation process which contains the desired product is a first step to get the product for the industry. One of the methods to separate this non-dissolve is by using ultrafiltration membrane. The main objective of this research is to investigate the effect of pH and ionic strength on membrane flux and rejection as well as to determine the optimum pH and ionic strength in order to obtain high flux and high lysozyme rejection by using ultrafiltration membrane. The range of pH that has been used is between 5 until 8. From the result, the alkaline conditions of the lysozyme solution resulted maximum membrane flux and rejection. This was due to the absorption of lysozyme onto the membrane and the charges between the membrane and the lysozyme solution itself. The optimum pH for high membrane flux and rejection and rejection is pH 8 while the optimum ionic strength for membrane flux is 0.5 M NaCl. -Author Membrane separation Membranes (Technology) 0 0 0 1 10000 10000 2019-09-04 0 TP248.25.M46 N87 2008 rs Thesis 0000031485 2019-09-04 00:00:00 1 2019-09-04 PSM 0 0 0 1 10000 10000 2019-09-04 0 CD 2806 | TP248.25.M46 N87 2008 rs Thesis 0000031486 2019-09-04 00:00:00 1 2019-09-04 PSM VIRTUA40 2542 2548 VTLSSORT0080*0200*0400*0900*1000*2450*2460*2600*3000*5020*5200*6500*6501*9992