000 02114nam a2200253 a 4500
001 vtls000045146
003 KUKTEM
005 20251114204452.0
008 100219t2009 my ao f m 000 0 eng d
020 _aTHE0002123(Local)
039 9 _a201905131647
_byusri
_c201203151642
_dida
_c201107132102
_dVLOAD
_y201002191150
_zkam
040 _aUMP
090 _aQD305.A2 N53 2009 rs Bc.
100 0 _aNurul Liana Abd Rahman
245 1 0 _aConcentration of biopetrol synthesized from oleic acid through catalytic cracking using zeolite as catalyst /
_cNurul Liana Bte Abd Rahman
246 3 _aConcentration of biopetrol synthesized from oleic acid through catalytic cracking using zeolite as catalyst
_h[electronic resource]
260 _aKuantan :
_bUMP,
_c2009
300 _a95 p. :
_bill. (some col.) ;
_c30 cm. +
_e1 computer disc
502 _aProject paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang – 2009
520 3 _aOleic acid is one of the major fatty acid in vegetable oil. In this research, zeolite catalysts are used over the conversion of oleic acid into isooctane as the future biopetrol in a heating mantle at atmospheric pressure. The main purposed of studies is to improve the concentration of isooctane using catalytic cracking method. The effect of various amount of Zeolite catalyst at 1g, 5g, 10g and 20g and various dilution factor of isooctane to hexane at 1%, 5%, 10% and 20% are studied over the yield of biopetrol at 98o C. Gas chromatography is used for the qualitative and quantitative analysis of the samples. Backward calculation is applied to calculate the actual concentration of isooctane in the distilled oleic acid. The maximum yield of desired isooctane obtained at 20g of catalyst and dilution of 20% isooctane to hexane is recorded at 7.89%. Experimental works has successful show that catalytic cracking is greater in conversion than thermal cracking.
650 0 _aOleic acid
650 0 _aEthylhexanol
999 _aVIRTUA40
_c2564
_d2570
999 _aVTLSSORT0080*0200*0400*0900*1000*2450*2460*2600*3000*5020*5200*6500*6501*9992