Direct application of tungstosilicic acid hydrate for the treatment of high free fatty acid in acidic crude palm oil and for biodiesel production

Author:

Hayyan Adeeb123ORCID,Abed Khalid M.14ORCID,Hayyan Maan56,Ali Ahmed Jawad7,Basirun Wan Jefrey8,Putra Sharifah Shahira Syed1ORCID,Alias Yatimah38,Alanazi Yousef Mohammed9,Saleh Jehad9,Hashim Mohd Ali1,Gupta Bhaskar Sen10

Affiliation:

1. Department of Chemical Engineering, Faculty of Engineering Universiti Malaya Kuala Lumpur Malaysia

2. Sustainable Process Engineering Centre (SPEC), Faculty of Engineering Universiti Malaya Kuala Lumpur Malaysia

3. University of Malaya Centre for Ionic Liquids (UMCiL), Faculty of Science Universiti Malaya Kuala Lumpur Malaysia

4. Department of Chemical Engineering, College of Engineering University of Baghdad Baghdad Iraq

5. Renewable Energy Engineering Program, Faculty of Engineering and Technology Muscat University Muscat Oman

6. Chemical Engineering Program, Faculty of Engineering and Technology Muscat University Muscat Oman

7. College of Engineering Al‐Turath University Baghdad Iraq

8. Department of Chemistry, Faculty of Science Universiti Malaya Kuala Lumpur Malaysia

9. Department of Chemical Engineering, College of Engineering King Saud University Riyadh Saudi Arabia

10. Institute of Infrastructure and Environment, School of Energy, Geoscience, Infrastructure and Society Heriot‐Watt University Edinburgh UK

Abstract

AbstractThis study explored the use of industrial acidic crude palm oil (ACPO) for biodiesel production, facing a significant obstacle due to its high free fatty acid (FFA) content, which complicates the biodiesel production process. Typically, esterification is employed to convert FFAs into fatty acid methyl ester (FAME). Herein, the effectiveness of tungstosilicic acid hydrate (TSAH) as an unsupported heteropoly acid (HPA) catalyst for FFA esterification in ACPO was investigated. The FFA content was reduced from 8.43% to 0.95% under optimum conditions (4 wt% catalyst dosage, a methanol to oil molar ratio of 10:1, 150 min and a temperature of 60°C). Noteworthy, the TSAH catalyst showed stability over 7 cycles. The kinetic analysis revealed that the FFA esterification process closely followed pseudo first‐order kinetics, with an R2 value of 0.94. Furthermore, the biodiesel produced from TSAH‐treated ACPO meets the standard specifications outlined by ASTM D6751 and EN 14214. This research highlights the effectiveness of TSAH in catalyzing FFA esterification without the need for additional support materials or modifications.

Funder

King Saud University

Publisher

Wiley

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