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MoO3 Catalyst Supported on Micro-Mesoporous Structure for Biodiesel Production
MoO3 Catalyst Supported on Micro-Mesoporous Structure for Biodiesel Production
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MoO3 Catalyst Supported on Micro-Mesoporous Structure for Biodiesel Production
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MoO3 Catalyst Supported on Micro-Mesoporous Structure for Biodiesel Production
MoO3 Catalyst Supported on Micro-Mesoporous Structure for Biodiesel Production

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MoO3 Catalyst Supported on Micro-Mesoporous Structure for Biodiesel Production
MoO3 Catalyst Supported on Micro-Mesoporous Structure for Biodiesel Production
Journal Article

MoO3 Catalyst Supported on Micro-Mesoporous Structure for Biodiesel Production

2025
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Overview
This study reports the synthesis and characterization of x_MoO 3 /H-Z/S micro-mesoporous catalyst, which combines the properties of ZSM-5 and SBA-15, as well as its performance for biodiesel production from the transesterification of soybean oil. ZSM-5 was added to the SBA-15 synthesis gel, calcinated, and molybdenum trioxide (MoO 3 ) was incorporated by incipient wetness using ammonium heptamolybdate salt [(NH 4 ) 6 Mo 7 O 24 ‧4H 2 O] as a metal precursor. The diffractograms and micrographics showed a micro-mesoporous structure of the support with the characteristic peaks of MoO 3 . The textural analysis showed that increasing the MoO 3 content decreases the specific area and the pore diameter of the catalysts. The Raman spectrum of the catalysts indicated vibration modes characteristic of the active species MoO 3 in the orthorhombic phase. The methanol/oil molar ratio was the variable that most influenced the yield of methyl esters within the levels of a design of experiments matrix. The highest biodiesel yield of 79.2% was obtained with 6 (wt.%) of MoO 3 , 4 h of reaction time, and a methanol/oil molar ratio of 20/1. This reaction condition uses a lower molybdenum content, lower catalyst load, and lower methanol/oil molar ratio than those reported in the literature, which qualitatively reduces the process costs. A quantitative economic analysis must be further performed to define the economic viability of the process. Graphical Abstract

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