02977nam a2200301 a 4500001001400000003000700014005001700021008004000038020002200078039010300100040000800203090003000211100002300241245015700264246015300421260003400574300005900608502009000667504002900757520145800786650002002244650001702264650001902281952012402300952013402424999002502558999009202583vtls000045125KUKTEM20251114204458.0100218t2009    my a   f m    000 0 engd  aTHE0004599(Local) 9a201905171032bazharc201108030934dFidac201107132353dVLOADc201010221305diday201002181021zida  aUMP  aTP359.B46 B79 2009 rs Bc.0 aBryan Lester Binar10aEsterification of octanoic acid and ethanol using sulfated zirconia in the presence of triglycerides :bkinetic and modelling study/cBryan Lester Binar3 aEsterification of octanoic acid and ethanol using sulfated zirconia in the presence of triglycerides :bkinetic and modelling studyh[computer file]  aKuantan, Pahang :bUMP,c2009  a57 p. :bill. (some col.) ;c30 cm. +e1 computer disc  aProject paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang - 2009  aBibiliography : p. 45-473 aThe  esterification  of  octanoic  acid  and  ethanol  using  sulfated  zirconia  in  the presence of  triglycerides  is one of  the methods  to produce biodiesel. As  the  fuel used today, petroleum is estimated depleted around 30-45 years in the future, Biodiesel is an alternative biofuel that can be produced using esterification method. The esterification of octanoic acid is done to determine the best operation condition to yield better conversion of  octanoic  acid.  The  operation  conditions  for  the  esterification  of  octanoic  acid  are temperature  of  reaction,  amount  of  sulfated  zirconia  used,  amount  of  triglycerides presence and molar ratio of octanoic acid to ethanol. The temperature of reaction ranged from 30ºC to 50ºC. The amount of sulfated zirconia used ranged from 0.5g to 1.5g. The amount of triglycerides presence ranged from 30ml to 70ml. The molar ratio of octanoic acid  to  ethanol  ranged  to  1:1  to  1:5.  The  best  operating  condition  achieved  for  the esterification of octanoic acid and ethanol were 30ºC reaction temperature, 1.5g sulfated zirconia  used,  1:1  molar  ratio  of  octanoic  acid  to  ethanol  and  50ml  of  triglycerides presence  in  the  esterification.  The  kinetic  model  been  used  is  pseudo-homogeneous kinectic model based on the experimental data gained. The pseudo-homogeneous kinetic model gives a good agreement between the experimental data and the model used. 0aBiodiesel fuels 0aTriglyceride 0aEsterification  00104071a10000b10000d2019-09-04l0oTP359.B46 B79 2009 rs Bc.p0000043005r2019-09-04 00:00:00t1w2019-09-04yPSM  00104071a10000b10000d2019-09-04l0oCD 4034 | TP359.B46 B79 2009 rs Bc.p0000043006r2019-09-04 00:00:00t1w2019-09-04yPSM  aVIRTUA40c2746d2752  aVTLSSORT0080*0200*0400*0900*1000*2450*2460*2600*3000*5020*5040*5200*6500*6501*6502*9992