Modification of NiW/Al₂O₃ Bimetallic Catalysts by ZSM-5, HY Zeolite, and Amorphous Silica Additions for Heavy Gas Oil (HGO) Hydrotreating

Authors

  • Sarwan Sarwan Department of Chemistry, Faculty of Science and Technology, Syarif Hidayatullah State Islamic University Jakarta
  • Isalmi Aziz Department of Chemistry, Faculty of Science and Technology, Syarif Hidayatullah State Islamic University Jakarta
  • Wawan Rustyawan Technology Innovation & Implementation, PT. Pertamina
  • Fuady Hanief Technology Innovation & Implementation, PT. Pertamina
  • Nurhasni Nurhasni Department of Chemistry, Faculty of Science and Technology, Syarif Hidayatullah State Islamic University Jakarta
  • Siti Nurbayti Department of Chemistry, Faculty of Science and Technology, Syarif Hidayatullah State Islamic University Jakarta
  • Yulyani Nur Azizah Department of Chemistry, Faculty of Science and Technology, Syarif Hidayatullah State Islamic University Jakarta

DOI:

https://doi.org/10.15408/jkv.v12i1.49693

Keywords:

Additive, hydrotreating, hydrodesulfurization, heavy gas oil, NiW/γ-Al2O3

Abstract

The NiW/γ-Al₂O₃ bimetallic catalyst is widely used in the hydrotreating of heavy gas oil (HGO) fractions to remove impurities, particularly sulfur-containing compounds (hydrodesulfurization, HDS) and polycyclic aromatic hydrocarbons (hydrodearomatization, HDA). The incorporation of additives into the alumina support can enhance catalytic activity by increasing surface acidity and improving textural properties. This study aims to synthesize, characterize, and evaluate the performance of NiW/γ-Al₂O₃ catalysts modified with zeolitic (ZSM-5 and HY zeolite) and amorphous silica additives on HDS and HDA of HGO. Catalysts were prepared via the wet impregnation method using supports containing 3 wt% additive. Among the synthesized materials, the NiW/γ-Al₂O₃ catalyst incorporating ZSM-5 exhibited the highest crystallinity, with metal loadings of 4.960 wt% Ni and 16.269 wt% W. This catalyst showed a surface area of 153.415 m²/g, a pore diameter of 116.643 Å, and a total acidity of 0.496 mmol/g. Hydrotreating evaluation demonstrated that the ZSM-5–modified NiW/γ-Al₂O₃ catalyst yielded a product with 4.50 ppm sulfur (99.96% HDS conversion) and 10.66% aromatics (54.10% HDA conversion) at 360 oC.

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References

1. Szewczyńska M, Dąbrowska J, Pyrzyńska K. Polycyclic aromatic hydrocarbons in the particles emitted from the diesel and gasoline engines. Pol J Environ Stud. 2017;26(2):801-807. doi:10.15244/pjoes/64914

2. Speight J. In The Refinery of the Future . In: Thermal Cracking. Elsevier Inc; 2020:1.

3. Abdrassilova A, Vassilina G, Abdildina K, Briones L, Peral A, Escola JM. The notable features of mesoporous aluminosilicates as catalytic supports for hydrodearomatization and hydrodesulfurization of fuels. Microporous and Mesoporous Materials. Elsevier B.V. 2025;384. doi:10.1016/j.micromeso.2024.113457

4. Meng XY, Zhao Y, Peng C, Liu P, Men YL, Pan YX. Boosting ultra-deep hydrodesulfurization of diesel by tuning sulfidation degree of metals on NiMo/AlOOH catalyst. Chem Eng Sci. 2024;287. doi:10.1016/j.ces.2024.119718

5. Keivanimehr F, Habibzadeh S, Mokhtarian M. Enhanced product quality through hydrodesulfurization of pyrolysis gasoline over a mixed metal oxide catalyst: An experimental and DFT study. Fuel. 2022;317. doi:10.1016/j.fuel.2022.123458

6. González-Ildelfonso M, Escobar J, Gordillo-Cruz E, del Ángel P, Suárez-Toriello VA, De los Reyes JA. RuS2-modified NiW/Al2O3 catalysts for refractory 4,6-dimethyl-dibenzothiophene hydrodesulfurization. Mater Chem Phys. 2022;278. doi:10.1016/j.matchemphys.2021.125568

7. Jeong HR, Lee YK. Comparison of unsupported WS2 and MoS2 catalysts for slurry phase hydrocracking of vacuum residue. Appl Catal A Gen. 2019;572:90-96. doi:10.1016/j.apcata.2018.12.019

8. Fang M, Ma S, Wang T, et al. Hydrotreatment of model compounds with catalysts of NiW/Al2O3 and NiWP/Al2O3 to simulate low temperature coal tar oil. RSC Adv. 2017;7(86):54512-54521. doi:10.1039/c7ra10317d

9. Nguyen TT, Qian EW. Synthesis of mesoporous Ti-inserted SBA-15 and CoMo/Ti-SBA-15 catalyst for hydrodesulfurization and hydrodearomatization. Microporous and Mesoporous Materials. 2018;265:1-7. doi:10.1016/j.micromeso.2018.01.026

10. Bing L, Tian A, Li J, et al. The Effects of Chelating Agents on CoMo/TiO2–Al2O3 Hydrodesulfurization Catalysts. Catal Letters. 2018;148(5):1309-1314. doi:10.1007/s10562-018-2331-6

11. Ulfiati R. Catalytic Performance Of ZSM-5 Zeolite In Heavy Hydrocarbon Catalytic Cracking: A Review. Scientific Contributions Oil and Gas. 2019;42(1):29-34.

12. Rahma A. Sintesis Dan Karakterisasi Katalis NiMo/g-Al2O3 Dengan Penambahan Zeolit HY, Zeolit Hierarki HY Dan Silika. UIN Syarif Hidayatullah Jakarta; 2019.

13. Kurniawan AA, Rustyawan W, Ibadurrohman M. Performance Test of Various Indonesian Natural Zeolites as Composite Components of NiMo/Al2O3-Zeolite Catalysts for Hydrocracking Used Cooking Oil into Biohydrocarbons. Bulletin of Chemical Reaction Engineering & Catalysis, 20 (1) 2025, 99-108. https://doi.org/10.9767/bcrec.20254

14. Pertamina. Katalis - Dasar Teori & Metoda Uji. Pertamina; 2015.

15. Riazi MR. Characterization and Properties of Petroleum Fractions, First Edition. 1st Edition.; 2005. doi:10.1520/mnl50_1st-eb

16. Ali S, Abbas Y, Zuhra Z, Butler IS. Synthesis of γ-alumina (Al2O3) nanoparticles and their potential for use as an adsorbent in the removal of methylene blue dye from industrial wastewater. Nanoscale Adv. 2019;1(1):213-218. doi:10.1039/c8na00014j

17. Hur YG, Kim MS, Lee DW, et al. Hydrocracking of vacuum residue into lighter fuel oils using nanosheet-structured WS2 catalyst. Fuel. 2014;137:237-244. doi:10.1016/j.fuel.2014.07.094

18. Tye CT. Catalysts for Hydroprocessing of Heavy Oils and Petroleum Residues. In: Processing of Heavy Crude Oils - Challenges and Opportunities. IntechOpen; 2019:1-12. doi:10.5772/intechopen.89451

19. Kurniawan T, Muraza O. Perengkahan n-Butana Menggunakan Katalis Nanopartikel Zeolit Alam Klaten. Jurnal Rekayasa Kimia & Lingkungan. 2018;13(2):182-188. doi:10.23955/rkl.v13i2.12059

20. Zhao X, Xu J, Deng F. Solid-state NMR for metal-containing zeolites: From active sites to reaction mechanism. Front Chem Sci Eng.Higher Education Press. 2020;14(2):159-187. doi:10.1007/s11705-019-1885-1

21. Wei Q, Chen J, Song C, Li G. HDS of dibenzothiophenes and hydrogenation of tetralin over a SiO2 supported Ni-Mo-S catalyst. Front Chem Sci Eng. 2015;9(3):336-348. doi:10.1007/s11705-015-1535-1

22. Minaev PP, Nikulshina MS, Gulyaeva LA, et al. Hydrotreating of Vacuum Gas Oil on NiW/Al2O3 Catalysts Prepared with the Use of Chelating Agents. Petroleum Chemistry. 2017;57(12):1161-1164. doi:10.1134/S0965544117060214

23. Nugrahaningtyas KD, Pratiwi N, Heraldy E. Desulfurisasi Katalitik Tiofen Menggunakan Katalis CoMo/USY dalam Reaktor Batch. ALCHEMY Jurnal Penelitian Kimia. 2018;14(1):119. doi:10.20961/alchemy.14.1.2368.119-130

24. Hur YG, Lee DW, Lee KY. Hydrocracking of vacuum residue using NiWS(x) dispersed catalysts. Fuel. 2016;185:794-803. doi:10.1016/j.fuel.2016.08.027

25. Ali 2020 ZFMoCo Ali A, Al-Arfaj AA, Saleh TA. Carbon nanofiber-doped zeolite as support for molybdenum based catalysts for enhanced hydrodesulfurization of dibenzothiophene. Journal of Molecular Liquids. 2020;303,112376. https://doi.org/10.1016/j.molliq.2019.112376

26. Adhani L, Susanto BH, Nasikin M. Dealumination Effect on ZSM-5 as a Bimetal Fe-Co Support for The Oxidative Desulfurization Process Catalyst. Jurnal Kimia Valensi. 2024;10(1):62-75. doi:10.15408/jkv.v10i1.38456

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Published

2026-05-31

Issue

Section

Jurnal Kimia VALENSI, Volume 12, No. 1, May 2026

How to Cite

Modification of NiW/Al₂O₃ Bimetallic Catalysts by ZSM-5, HY Zeolite, and Amorphous Silica Additions for Heavy Gas Oil (HGO) Hydrotreating. (2026). Jurnal Kimia Valensi, 12(1), 26-34. https://doi.org/10.15408/jkv.v12i1.49693