02492nam a2200277 a 4500001001400000003000700014005001700021008004100038020002200079039011000101040000800211090003200219100002000251245015700271246016100428260003400589300004700623502009100670520104200761650002001803650002401823952012601847952013601973999002302109999008202132vtls000031350KUKTEM20251114204354.0080902t2008    my a   f m    000 0 eng|d  aTHE0004144(Local) 9a201905132128bfarhanac201107132104dVLOADc200908141515dVLOADc200908141445dVLOADy200809021243zida84  aUMP  aTP156.F5 S58 2008 rs Thesis0 aSiti Marni Aziz10aRole of electrokinetic parameters on asymmetric ultrafiltration membrane flux and rejection during separation of bovine serum albumin /cSiti Marni Aziz3 aRole of electrokinetic parameters on asymmetric ultrafiltration membrane flux and rejection during separation of bovine serum albuminh[electronic resource]  aKuantan, Pahang :bUMP,c2008  a76 p. :bill. ;c30 cm. +e1 computer disc  aProject paper (Bachelor of Chemical Engineering) --- Universiti Malaysia Pahang - 20083 aThe protein concentration involves the removal of solvent (usually water) from protein solution. There will be various methods that can be used for this protein concentration process. One of the methods is by using ultra filtration method. During ultra filtration, the macromolecules such as protein are retained on the membrane. The main objective in this experiment is to determine the optimum pH condition and ionic strength concentration which is give maximum permeate flux which is through the membrane. The molecular weight cut off for the membrane is 50 kDa. This study is carried out in order to know the effect of pH protein solution to the permeate flux and the percent rejection of protein molecules with the various value of pH. Besides, the effect of ionic strength concentration to the permeate flux and rejection protein molecule also had been highlight in this study.  From the result acquire, optimum flux for BSA protein filtration is been observed in pH 8 solution and in 0.5M NaCl ionic strength concentration.-Author 0aUltrafiltration 0aMembrane separation  00104071a10000b10000d2019-09-04l0oTP156.F5 S58 2008 rs Thesisp0000031397r2019-09-04 00:00:00t1w2019-09-04yPSM  00104071a10000b10000d2019-09-04l0oCD 2762 | TP156.F5 S58 2008 rs Thesisp0000031398r2019-09-04 00:00:00t1w2019-09-04yPSM  aVIRTUA40c890d896  aVTLSSORT0080*0200*0400*0900*1000*2450*2460*2600*3000*5020*5200*6500*6501*9992