000 02421nam a2200265 a 4500
001 vtls000056165
003 KUKTEM
005 20251114204434.0
008 111121t2010 my a f m 000 0 eng d
020 _aTHE0004287(Local)
039 9 _a201905161402
_bfarhana
_c201112161145
_dfauzi
_y201111211153
_zFida
040 _aUMP
090 _aTP242 .J47 2010 rs Bc.
100 0 _aJessico Mutun
245 1 0 _aEffects of coagulation medium on asymmetric polyethersulfone membrane for carbon dioxide and methane separation /
_cJessico Mutun
260 _aKuantan, Pahang :
_bUMP,
_c2010
300 _axviii, 50 p. :
_bill. ;
_c30 cm. +
_e1 computer disc
502 _aProject paper (Bachelor of Chemical Engineering (Gas Technology)) -- Universiti Malaysia Pahang - 2010
504 _aBibliography : p. 46-47
520 3 _aThis study is concentrated on the ability and the performance of the asymmetric polyethersulfone membrane in gas separation process. Asymmetric flat sheet membranes were prepared by using a simple dry/wet phase inversion method. Experimental investigations were conducted focusing on the effect of the different coagulation medium during the phase inversion toward the permeability and the selectivity of the membrane to the carbon dioxide and methane gases. Three different coagulants medium were used which were water, methanol and water/methanol (50:50). The flats sheet asymmetric membrane then being characterized by using the scanning electron microscopy (SEM) and the Fourier transform infrared spectroscopic (FTIR). Gas permeation tests then run to examine the effect of the different coagulants toward the time of the gases pass through the membrane. From the result of the gas permeability unit calculation, membrane which immersed in water solution has shown the highest permeability. Different coagulant medium will affect the performance of the membrane toward its permeability and selectivity of gases. The water medium solution is the best coagulation medium for the asymmetric polyethersulfone membrane during the phase inversion method with the GPU value of 3.23. As for the conclusion, water is identified as the best coagulation medium for asymmetric polyethersulfone membrane.
650 0 _aGases
_xSeparation
650 0 _aGas separation membranes
650 0 _aPolymers
999 _aVIRTUA40
_c2065
_d2071
999 _aVTLSSORT0080*0200*0400*0900*1000*2450*2600*3000*5020*5040*5200*6500*6501*6502*9992