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

作者：Kiatkittipong Worapon^*; Phimsen Songphon; Kiatkittipong Kunlanan; Wongsakulphasatch Suwimol; Laosiripojana Navadol; Assabumrungrat Suttichai

来源：Fuel Processing Technology, 2013, 116: 16-26.

DOI：10.1016/j.fuproc.2013.04.018

• Bio-hydrogenated diesel (BHD)
• Hydrotreated vegetable oil (HVO)
• Green diesel
• Renewable liquid fuel
• Deoxygenation
• Phosphorous

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 NiMoty-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 degrees 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 degrees 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/gamma-Al2O3.

• 出版日期2013-12