02394nam a2200277 a 4500001001400000003000700014005001700021008004100038020002200079039008300101040000800184090002900192100002700221245014200248246013500390260002600525300005900551502009200610520101900702650001501721650001701736952012301753952013301876999002502009999008202034vtls000045146KUKTEM20251114204452.0100219t2009    my ao  f m    000 0 eng d  aTHE0002123(Local) 9a201905131647byusric201203151642didac201107132102dVLOADy201002191150zkam  aUMP  aQD305.A2 N53 2009 rs Bc.0 aNurul Liana Abd Rahman10aConcentration of biopetrol synthesized from oleic acid through catalytic cracking using zeolite as catalyst /cNurul Liana Bte Abd Rahman3 aConcentration of biopetrol synthesized from oleic acid through catalytic cracking using zeolite as catalysth[electronic resource]  aKuantan :bUMP,c2009  a95 p. :bill. (some col.) ;c30 cm. +e1 computer disc  aProject paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang – 20093 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. 0aOleic acid 0aEthylhexanol  00104071a10000b10000d2019-09-04l0oQD305.A2 N53 2009 rs Bc.p0000042927r2019-09-04 00:00:00t1w2019-09-04yPSM  00104071a10000b10000d2019-09-04l0oCD 3991 | QD305.A2 N53 2009 rs Bc.p0000042928r2019-09-04 00:00:00t1w2019-09-04yPSM  aVIRTUA40c2564d2570  aVTLSSORT0080*0200*0400*0900*1000*2450*2460*2600*3000*5020*5200*6500*6501*9992