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  4. Diesel-like hydrocarbon production from hydroprocessing of relevant refining palm oil
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Diesel-like hydrocarbon production from hydroprocessing of relevant refining palm oil

Author(s)
Kiatkittipong, Worapon
Phimsen, Songphon
Kiatkittipong, Kunlanan
Wongsakulphasatch, Suwimol
Laosiripojana, Navadol
Assabumrungrat, Suttichai
Date Issued
May 22, 2013
Type
Article
DOI
10.1016/j.fuproc.2013.04.018
Abstract
This paper demonstrates the initiated use of relevant refining palm oil for bio-hydrogenated diesel production. The conversions of crude palm oil (CPO) and its physical refining including degummed palm oil (DPO) and palm fatty acid distillate (PFAD) to diesel fuel by hydroprocessing were studied. The effects of operating parameters (i.e. reaction time, operating temperature, and pressure) and catalyst (i.e. Pd/C and NiMo/γ-Al2O3) were examined in order to determine suitable operating condition for each feedstock. It was found that the hydroprocessing of CPO with Pd/C catalyst at 400 C, 40 bar, and reaction time of 3 h provides the highest diesel yield of 51%. When gum which contains phospholipid compounds is removed from CPO, namely DPO, the highest diesel yield of 70% can be obtained at a shorter reaction time (1 h). In the case of PFAD, which consists mainly of free fatty acids, a maximum diesel yield of 81% could be observed at milder conditions (375 C with the reaction time of 0.5 h). The main liquid products are n-pentadecane and n-heptadecane, having one carbon atom shorter than the corresponding fatty acids according to decarboxylation/decarbonylation pathways. Pd/C catalyst shows good catalytic activity for fatty acid feedstocks but becomes less promising for triglyceride feedstocks when compared to NiMo/γ-Al2O3. © 2013 Elsevier B.V.
Citation
Fuel Processing Technology, 116, 16-26, 2013
Subjects

Bio-hydrogenated dies...

Deoxygenation

Green diesel

Hydrotreated vegetabl...

Phosphorous

Renewable liquid fuel...

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