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008 100205t2009 my a f m 001 0 eng d
020 _aTHE0004712(Local)
039 9 _a201905131613
_bsmfh
_c201108030929
_dFida
_c201107132306
_dVLOAD
_c201002081448
_dkam
_y201002051059
_zkam
040 _aUMP
090 _aTP360 .F56 2009 rs Bc.
100 0 _aFlorina Geduin
245 1 0 _aUp-scale study on ultrasonically assisted of biodiesel production from waste cooking oil (WCO) /
_cFlorina Geduin
246 3 _aUp-scale study on ultrasonically assisted of biodiesel production from waste cooking oil (WCO)
_h[computer file]
260 _aKuantan :
_bUMP,
_c2009
300 _a52 p. :
_bill. (some col. ) ;
_c30 cm. +
_e1 computer disc
502 _aProject paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang - 2009
520 3 _aUp-scale for the production of biodiesel from waste cooking oil (WCO) and Refined-Bleached-Deodorized (RBD) under ultrasonic condition was studied. The effects of sodium hydroxide as a catalyst and time on the biodiesel conversion were investigated. Experiments have been performed to determine the optimum condition for this alkali-catalyzed transesterification process where the temperature is fixing at 40ºC and the stirring rpm are 1000 rpm. The results showed that transesterification process under ultrasonic condition was proved to be time and energy saving. Gas Chromatography (GC) is used to study the formation of methyl ester of waste cooking oil and combustion test to study the combustion characteristic of biodiesel. The optimum experimental condition for catalyst concentration is 1 wt% sodium hydroxide (NaOH) and the reaction time is 40 minutes for WCO while 0.75 wt % sodium hydroxide (NaOH) and the reaction time is 30 minutes for RBD. The level of carbon dioxide (CO2) and carbon monoxide (CO) in biodiesel from WCO are low compare to the RBD and diesel fuel.
650 0 _aBiodiesel fuels
650 0 _aWaste products as fuel
650 0 _aDiesel motor
_xAlternative fuels
999 _aVIRTUA40
_c1693
_d1699
999 _aVTLSSORT0080*0200*0400*0900*1000*2450*2460*2600*3000*5020*5200*6500*6501*6502*9992