Design of γ-Alumina-Supported Phosphotungstic Acid-Palladium Bifunctional Catalyst for Catalytic Liquid-Phase Citral Hydrogenation

• Published in: Catalysts Vol. 12; no. 9; p. 1069
• Main Authors: Shah, Abdul Karim, Bukhari, Syed Nizam-uddin Shah, Shah, Ayaz Ali, Jatoi, Abdul Sattar, Usto, Muhammad Azam, Hashmi, Zubair, Shah, Ghulam Taswar, Park, Yeung Ho, Choi, Moo-Seok, Iqbal, Arshad, Seehar, Tahir Hussain, Raza, Aamir
• Format: Journal Article
• Language: English
• Published: Basel MDPI AG 01.09.2022
• Subjects: Acids; Alumina; Aluminum compounds; Aluminum oxide; bifunctional catalysts; Catalysis; Catalysts; Chemical reactions; Chemicals; Chloride; Citral; citral hydrogenation; Dehydration; Design; Fourier transforms; Gas pressure; heteropoly acids; Hydrogenation; Liquid phases; Loading rate; Mass transfer; Menthol; Metals; Palladium; Palladium catalysts; Phosphates; Precursors; Reaction time; Silicon; Substrates; Titration; Transitional aluminas; Tungsten compounds
• ISSN: 2073-4344; 2073-4344
• DOI: 10.3390/catal12091069

This study primarily addresses the development of dynamic, selective and economical metal–acid (bifunctional) catalysts for one-pot menthol production by citral hydrogenation. Specifically, various metals such as Pd, Pt, Ni, Cs and Sn were doped over alumina support. Additionally, bifunctional composite catalysts were also prepared with the impregnation of heteropoly acids and Pd precursors over alumina support. Analytical techniques (e.g., BET, PXRD, FT-IR, pyridine adsorption and amine titration methods) were applied for characterization of the most efficient and selective catalysts (e.g., Al2O3 and PTA-Cat-I). Similarly, most of the essential operational variables (e.g., loading rate of metal precursor, type of heteropoly acid, temperature, gas pressure and reaction time) were examined during this study. The experimental data shows that the bifunctional catalyst (PTA-Cat-I) produced 45% menthol at full citral substrate conversion (r = 0.038 mmoles.min−1) in liquid-phase citral hydrogenation (at optimized operating conditions: 70 °C, 0.5 MPa and 8 h). However, the heteropoly acid-supported bifunctional catalysts (e.g., PTA-Cat-I, PMA-Cat-I, SMA-Cat-I and STA-Cat-I) resulted in cracking and the dehydration of isopulegol/menthol by the generation of side products (e.g., 4-isopropyl-1-methyl, cyclohex-1-ane/ene); therefore, menthol yield was extensively diminished. On the other hand, non-acidic catalysts (e.g., Cat-I, Cat-II, Cat-III, Cat-IV and Cat-V) readily promoted hydrogenation reactions. The optimum menthol yield occurred due to the presence of strong Lewis and weak Bronsted acid sites. Mass transfer and reaction rate were substantially diminished due to acidity strength, heteropoly acid type and blockage of pores by the applied bifunctional catalysts.