![]() This observation proves that EFB-derived pyrolysis oil could be upgraded via heterogeneous catalytic cracking to produce gasoline.Ĭatalytic Cracking of Used Palm Oil using Composite Zeolite From the analysis that has been done, it is found that the optimum operating condition for heterogeneous catalytic cracking process is at 400 degrees C, 15min of reaction time using 30g of catalyst weight where operating at this condition produced the highest yield of gasoline fraction which is 91.67 wt.%. The main objective of this paper is to find the optimum operating condition to upgrade the EFB-derived pyrolysis oil (bio- oil) to liquid fuel, mainly gasoline using Taguchi Method. Hew, K L Tamidi, A M Yusup, S Lee, K T Ahmad, M M The reaction is discontinued at that point and the catalyst is regenerated for further use.Ĭatalytic cracking of bio- oil to organic liquid product (OLP). ![]() The reaction is allowed to proceed until consumption of the free begins. ![]() A gas containing between 20 and 90 mol % of free hydrogen is used. The reaction takes place in the presence of a solid catalyst between 700 to 900/sup 0/F under pressure between atmospheric and 400 psi. ![]() ![]() Energy Technology Data Exchange (ETDEWEB)Ī process is described for the vapor phase catalytic cracking of hydrocarbon oils boiling substantially in the gas oil range. ![]()
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