(704g) Green Fuel from Hydrotreated Vegetable Oil Using Ni-Fe/Zeolite Y Catalysts
AIChE Annual Meeting
2023
2023 AIChE Annual Meeting
Catalysis and Reaction Engineering Division
Thermal and Thermocatalytic Biomass Conversion and Biorefining II
Thursday, November 9, 2023 - 1:50pm to 2:10pm
In this work, the hydrotreatment of soybean oil for green fuel was conducted by Ni-Fe bimetallic supported on zeolite Y catalysts, denoted as Ni-Fe/Y, that were successfully synthesized with incipient wetness impregnation method. Prior to the process of hydrotreatment, the Ni-Fe/Y catalyst was firstly activated in hydrogen atmosphere at 400°C to a reduced state, denoted as Ni-Fe(R)/Y. Hydrotreatment of soybean oil was performed using decalin as the solvent and various Ni-Fe(R)/Y catalysts in a semi-batch reactor equipped with a magnetic stirrer and a temperature controller. Activated and spent catalysts were characterized by XRD, SEM, XPS, ICP-OES, H2-TPR, NH3-TPD, and N2 physisorption analyzer. The determination of yield and selectivity of the product was accomplished by GC-FID, while qualitative analyses were conducted using GC-MS and FT-IR. Figure 1 illustrates the yield of deoxygenated hydrocarbons from soybean oil hydrotreated at 300°C and 40 bar H2 with Ni-Fe/Y catalysts on which the total loadings of Ni and Fe on zeolite Y were fixed at 30 wt% based on the mass of zeolite Y. Compared to the Ni monometallic catalysts, the Ni-Fe/Y(R) catalyst with a mass ratio of Ni/Fe at 4 exhibited superior catalysis in deoxygenation and gave the larger overall yield. Additionally, increasing the total metal loadings and the reaction temperature can accelerate the reaction rate of deoxygenation and cracking, respectively. As a result, the hydrotreatment of soybean oil by 28Ni-7Fe(R)/Y catalyst at 350°C and 40 bar H2 resulted in the best degree of deoxygenation and the highest yield in short-chain hydrocarbons. The reusability of the catalyst was also discussed in this work.