Sains Malaysiana 55(4)(2026): 634-644
http://doi.org/10.17576/jsm-2026-5504-04
Sulfur Resistance
of Ba-Pt/γ-Al2O3 Pellets for Carbonyl Sulfide
Hydrolysis
(Rintangan Sulfur Pelet Ba-Pt/γ- Al2O3 untuk Hidrolisis Karbonil Sulfida)
KANNAPORN NIMTHUPHARIYHA1,2, PUNYAPHAT JINJO3,
SARTTRAWUT TULAPHOL4, NURAK GRISDANURAK3,* & PUMMARIN KHAMDAHSAG5
1International
Program in Hazardous Substance and Environmental Management, Graduate School,
Chulalongkorn University, Bangkok 10330, Thailand
2Center
of Excellence on Hazardous Substance Material (HSM), Chulalongkorn University,
Bangkok 10330, Thailand
3Center
of Excellence in Environmental Catalysis and Adsorption, Faculty of
Engineering, Thammasat University, Pathum Thani 12121, Thailand
4Sustainable
Polymer & Innovative Composite Materials Research Group, Department of
Chemistry, Faculty of Science, King Mongkut’s University of Technology Thonburi
Bangkok 10140, Thailand
5Sustainable
Environment Research Institute, Chulalongkorn University, Bangkok 10330,
Thailand
Received: 17
September 2025/Accepted: 31 March 2026
Abstract
The
catalytic hydrolysis of carbonyl sulfide (COS) was studied using γ-Al2O3 pellets promoted with platinum (Pt) and barium (Ba). A series of catalysts,
including γ-Al2O3, 0.1Pt/γ-Al2O3,
and Ba-promoted Pt/γ-Al2O3 with varying Ba loadings
(0.5-3.0 wt%) were evaluated in terms of catalytic
activity and sulfur tolerance. Catalyst deactivation after 180 min was
quantified and correlated with sulfur retention determined by CHNS analysis.
Bare γ-Al2O3resulted in the most severe deactivation (25.56%), whereas the Pt modification markedly improved the catalyst durability, reducing the degree of deactivation to
7.78%. Among the Ba-promoted catalysts, 0.5Ba-0.1Pt/γ-Al2O3 exhibited the best performance, showing the lowest deactivation (7.73%) and the
lowest sulfur retention (0.0427 wt%). In contrast, higher Ba loadings increased
sulfur accumulation (up to 0.1259 wt%) and resulted in moderately higher
deactivation (9.14-10.04%). TGA/DTG analysis of fresh and spent catalysts
further supported the sulfur retention mechanism. This suggests that Pt improves sulfur tolerance by facilitating a more uniform
distribution of sulfur species, whereas Ba
enhances resistance by stabilizing and trapping sulfur species on the catalyst
surface. These findings demonstrate that an appropriate balance of Pt and Ba
loading is essential for improving catalyst durability, with
0.5Ba-0.1Pt/γ-Al2O3 identified as the optimal
composition for COS hydrolysis.
Keywords:
Barium promotion; catalyst deactivation; COS hydrolysis; platinum catalyst;
sulfur poisoning; γ-Al2O3 pellets
Abstrak
Hidrolisis pemangkin karbonil sulfida (COS) telah dikaji menggunakan pelet γ-Al2O3 yang dipromosikan dengan platinum (Pt)
dan barium (Ba). Satu siri pemangkin, termasuk γ-Al2O3,
0.1Pt/γ-Al2O3 dan Pt/γ-Al2O3 yang dipromosikan oleh Ba dengan pelbagai beban Ba (0.5-3.0 wt%) telah dinilai dari segi aktiviti pemangkin dan toleransi sulfur. Penyahaktifan pemangkin selepas 180 minit telah diukur dan dikaitkan dengan pengekalan sulfur yang ditentukan oleh analisis CHNS. γ-Al2O3 kosong menghasilkan penyahaktifan yang paling teruk (25.56%), manakala pengubahsuaian Pt telah meningkatkan ketahanan pemangkin dengan ketara, mengurangkan tahap penyahaktifan kepada 7.78%.
Antara mangkin yang digalakkan oleh Ba, 0.5Ba-0.1Pt/γ-Al2O3 mempamerkan prestasi terbaik, menunjukkan penyahaktifan terendah (7.73%) dan pengekalan sulfur terendah (0.0427 wt%). Sebaliknya, pemuatan Ba
yang lebih tinggi meningkatkan pengumpulan sulfur (sehingga 0.1259 wt%)
dan mengakibatkan penyahaktifan yang agak tinggi (9.14-10.04%). Analisis TGA/DTG bagi mangkin segar dan terpakai menyokong lagi mekanisme pengekalan sulfur. Ini menunjukkan bahawa Pt meningkatkan toleransi sulfur dengan memudahkan taburan spesies sulfur yang lebih seragam, manakala Ba meningkatkan rintangan dengan menstabilkan dan memerangkap spesies sulfur pada permukaan mangkin. Penemuan ini menunjukkan bahawa keseimbangan pemuatan Pt dan Ba yang sesuai adalah penting untuk meningkatkan ketahanan mangkin dengan 0.5Ba-0.1Pt/γ-Al2O3 dikenal pasti sebagai komposisi optimum untuk hidrolisis COS.
Kata kunci: Hidrolisis COS; keracunan sulfur; mangkin platinum; pelet γ-Al2O3; penyahaktifan mangkin; promosi Barium
REFERENCES
Zhang et al. 2018
Feng, X., Zhao, C., Chen, Z., Yun, J., Zhao, Y., Zheng,
H., Wei, N., Tong, Z. & Chen, Z. 2025. Research on a novel ZSM-5@Al2O3 compound catalyst for the hydrolysis of carbonyl sulfide from blast furnace gas
and in situ reaction mechanism. Journal of Environmental Chemical
Engineering 13: 116885.
Gao, S., Zhao, S., Tang, X., Wang, Y. & Yi, H. 2024. Mechanics
of COS removal by adsorption and catalytic hydrolysis: Recent developments. Fuel 359: 130394.
Jia, T., Guan, J., Qin, Z., Wu, M., Chang, L., Zhai, Z.,
Lin, G. & Du, Z. 2025. Correlation between alkaline characteristics and
catalytic performance of K2CO3/Al2O3 in carbonyl sulfide hydrolysis. Results in Chemistry 18: 102755.
Kim, D.H., Kwak, J.H., Szanyi, J. & Peden, C.H.F. 2012. Isothermal desulfation of pre-sulfated Pt–BaO/γ-Al2O3 lean NOx trap catalysts with H₂: The effect of H₂ concentration
and the roles of CO2 and H2O. Applied Catalysis B:
Environmental111-112: 342-348.
Kim, J., Do, J.Y., Park, N-K., Hong, J-P. & Kang, M.
2018. Adsorption/desorption behavior of carbonyl sulfide gas on scheelite type
MWO4 adsorbent. Separation and Purification Technology 207:
58-67.
Lei, G., Zheng, Y., Cao, Y., Shen, L., Wang, S., Liang,
S., Zhan, Y. & Jiang, L. 2023. Deactivation mechanism of COS hydrolysis
over potassium modified alumina. Acta Physico-Chimica Sinica 39(9): 2210038.
Nimthuphariyha, K., Usamani, A., Grisdanurak, N., Kanchanatip, E.,
Suthirakune, S., Yan, M. & Tulaphol, S. 2021. Hydrolysis of carbonyl
sulfide over modified Al2O3 by platinum and barium in a
packed-bed reactor. Chemical Engineering Communications 208(4): 539-548.
Renda, S., Barba, D. & Palma, V. 2022. Recent
solutions for efficient carbonyl sulfide hydrolysis: A review. Industrial
& Engineering Chemistry Research 61: 5685-5697.
Song, X., Chen, X., Sun, L., Li, K., Sun, X., Wang, C.
& Ning, P. 2020. Synergistic effect of Fe2O3 and CuO
on simultaneous catalytic hydrolysis of COS and CS2: Experimental
and theoretical studies. Chemical Engineering Journal 399: 125764.
Song, X., Ning, P., Wang, C., Li, K., Tang, L-H., Sun, X.
& Ruan, H-T. 2017. Research on the low temperature catalytic hydrolysis of
COS and CS2 over walnut shell biochar modified by Fe–Cu mixed metal
oxides and basic functional groups. Chemical Engineering Journal 314:
418-433.
Sun, J., Du, X., Li, Z., Yu, H., Hong, Y., Pan, M., Nie,
G., Fan, W., Gao, F., Wu, F., Li, L., Deng, G., Sun, Z. & Duan, L. 2024.
Rational design of poisoning-resistant catalyst based on γ-Al2O3 for hydrolysis of carbonyl sulfide. Chemical Engineering Science 295:
120150.
Sun, X., Ning, P., Tang, X-L., Yi, H-H., Li, K., He, D.,
Xu, X-M., Huang, B. & Lai, R-Y. 2014. Simultaneous catalytic hydrolysis of
carbonyl sulfide and carbon disulfide over Al2O3-K/CAC
catalyst at low temperature. Journal of Energy Chemistry 23(2): 221-226.
Wang, H., Liu, C., Gong, Z., Jiang, H., Gao, W., Guo, G.,
Yang, F., Wu, Q., Mertsoy, E.Y., Zhao, J., Liu, J.,
Ling, H., Shen, B., Wu, D. & Sun, H. 2024. CuY@NiAl-Layered double oxides bi-functional composites for “Catalytic–Adsorptive” removal of
carbonyl sulfide. Chemical Engineering Journal 493: 151992.
Wang, H.Y., Yi, H.H., Ning, P., Tang, X.L., Yu, L.L., He,
D. & Zhao, S. 2011. Calcined hydrotalcite-like compounds as
catalysts for hydrolysis of carbonyl sulfide at low temperature. Chemical
Engineering Journal166(1):
99-104.
Wang, X., Ma, Y., Ning, P., Qiu, J., Ren, X., Li, Z.,
Chen, W. & Liu, W. 2014. Adsorption of carbonyl sulfide on modified
activated carbon under low-oxygen content conditions. Adsorption 20(4):
623-630.
West, J., Williams, B.P., Young, N., Rhodes,
C. & Hutchings, G.J. 2001. Ni- and Zn-promotion of γ-Al2O3 for the hydrolysis of carbonyl sulfide under mild conditions. Catalysis
Communications2(3-4): 135-138.
West, J., Williams, B.P., Young, N.C., Rhodes, C. &
Hutchings, G.J. 1998. New directions for COS hydrolysis: Low temperature
alumina catalysts. Studies in Surface Science and Catalysis 119: 373-378.
Zhao, S., Yi, H., Tang, X., Jiang, S., Gao, F., Zhang,
B., Zuo, Y. & Wang, Z. 2013. The hydrolysis of carbonyl sulfide at low
temperature: A review. The Scientific World Journal 2013: 739501.
Zi, S., Li, K., Wang, X., Sun, L., Tian, Y., Huang, B.,
Zeng, H. & Ma, Y. 2024. Influence of surface basic sites and oxygen
vacancies on the performance of metal-modified rod-like ceria catalysts for
low-temperature hydrolysis of carbonyl sulfide. Chemistry – An Asian Journal 19: e202400235.
*Corresponding
author; email: gnurak@engr.tu.ac.th