Published at : 31 Mar 2026
Volume : IJtech
Vol 17, No 2 (2026)
DOI : https://doi.org/10.14716/ijtech.v17i2.8009
| Tri Widjaja | Chemical Engineering Department, Sepuluh Nopember Institute of Technology, Sukolilo, Surabaya 60111, Indonesia |
| Ali Altway | Chemical Engineering Department, Sepuluh Nopember Institute of Technology, Sukolilo, Surabaya 60111, Indonesia |
| Shofia Khoirunnisa | Chemical Engineering Department, Sepuluh Nopember Institute of Technology, Sukolilo, Surabaya 60111, Indonesia |
| Dinda Amelia Nurhanifa | Chemical Engineering Department, Sepuluh Nopember Institute of Technology, Sukolilo, Surabaya 60111, Indonesia |
| Mahfud Mahfud | Chemical Engineering Department, Sepuluh Nopember Institute of Technology, Sukolilo, Surabaya 60111, Indonesia |
| Hendro Juwono | Chemistry Department, Sepuluh Nopember Institute of Technology, Sukolilo, Surabaya 60111, Indonesia |
| Joni Prasetyo | Research Center for Molecular Chemistry, National Research and Innovation Agency (BRIN), Tangerang Selatan 15314, Indonesia |
| Deliana Dahnum | Research Center for Molecular Chemistry, National Research and Innovation Agency (BRIN), Tangerang Selatan 15314, Indonesia |
| Aisyah Alifatul Zahidah Rohmah | Chemical Engineering Department, East Java Veterans National Development University, Gunung Anyar, Surabaya 60294, Indonesia |
This study investigated the
synthesis and application of Cu-MOF/K2O catalysts for pyrolytic catalytic
cracking (PCC) of waste cooking oil (WCO) to produce biofuels. Cu-MOF/K2O
catalysts were synthesized via a facile temperature method by incorporating
copper as the metal center and 2-methylimidazole as the organic ligand
with varying K2O concentrations (3, 5, and 10 wt%), followed by thermal
treatment at 500 oC. WCO was reacted under atmospheric pressure with N2
gas at various temperatures to produce an oil-liquid product (OLP).
Characterization by FT-IR and XRD confirmed the decomposition of Cu-MOF
into CuO and Cu2O, while XRF revealed the increase in K2O concentration in
Cu-MOF/K2O as a result of varying the base. SEM imaging demonstrated a
uniform particle size distribution in Cu-MOF/K2O, while the BET surface area
analysis indicated a reduction in the surface area due to K2O
incorporation. The NH3 and CO2-TPD confirmed the coexistence of several types
of acidic and basic sites in the catalyst. GC-MS analysis of OLP revealed
a significant enhancement in hydrocarbon content following PCC, with
Cu-MOF/10-K2O achieving a maximum hydrocarbon yield exceeding >99.9% at
400 °C, containing 53% biogasoline, 29% biokerosene, and 18% green diesel,
indicating high selectivity toward transportation-range fuels. This study
highlights the potential of a cost-effective catalyst, Cu-MOF/K2O, in
advancing sustainable biofuel production, thereby reducing reliance on
fossil fuels and promoting environmental sustainability.
Biofuel; Cu-MOF/K2O; Deoxygenation; Pyrolytic catalysis cracking; Waste cooking oil
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