ORIGINAL RESEARCH
Preliminary Study of Methyl Orange Removal Using a Persulfate-Based Advanced Oxidation Process with Indonesian Palm Kernel Shell-Based Activated Carbon as an Activator: Experiment and Sorption-Oxidation Kinetic Analyses
 
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1
Research Center for Environmental and Clean Technology, National Research and Innovation Agency (BRIN), Building 720, K.S.T. B.J Habibie, Serpong, South Tangerang 15314, Indonesia
 
2
Graduate School of Environmental Studies, Diponegoro University, Jl. Prof. Soedarto SH Tembalang, Semarang 50275, Indonesia
 
3
Chemical Engineering Diponegoro University, Jl. Prof. Soedarto SH Tembalang, Semarang 50275, Indonesia
 
4
Environment Engineering Diponegoro University, Jl. Prof. Soedarto SH Tembalang, Semarang 50275, Indonesia
 
5
Directorate for Environment, Maritime, Natural Resources, and Nuclear Policy, National Research and Innovation Agency (BRIN), Gedung B.J. Habibie, Jl. M.H. Thamrin No. 8, Jakarta, Indonesia
 
6
Program Studi Teknik Kimia, Sebelas Maret University, Jl. Ir. Sutami No. 36, Surakarta, Indonesia
 
7
Research Center for PreClinical and Clinical Medicine, National Research and Innovation Agency (Badan Riset dan Inovasi Nasional, BRIN), Jl. Raya Bogor KM. 46, Cibinong 16911, Indonesia
 
 
Submission date: 2024-10-05
 
 
Final revision date: 2024-12-05
 
 
Acceptance date: 2024-12-16
 
 
Online publication date: 2025-03-17
 
 
Corresponding author
Ardie Septian   

Research Center for Environmental and Clean Technology, National Research and Innovation Agency, Jl. Raya Serpong, 15314, South Tangerang, Indonesia
 
 
 
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ABSTRACT
Two types of activated carbon (AC), namely Indonesian palm kernel shell-based AC (ZnCl2-AC) and commercial AC, were introduced to activate persulfate (PS) for catalytic degradation of methyl orange (MO) in water. This is the first attempt to apply the coupled sorption-oxidation kinetic model to the kinetic data of MO removal in the PS/AC system. The PS activated by AC removed more MO than the AC-only or PS activated by Fe2+. In the PS/AC system, to get maximum MO removal (100%), the use of commercial AC needed higher AC and PS dosages ([AC] = 185 mg L-1, and [PS] = 346 mg L-1) than the use of ZnCl2-AC ([AC] = 770 mg L-1, and [PS] = 1728 mg L-1). The MO removal in the PS/AC system fitted with the coupled sorption–oxidation kinetic model. Compared to the AC-only system, the PS/AC system enhanced the oxidation mechanism but depressed the sorption mechanism. The O2 •– played a dominant role in the oxidation mechanism. The MO was degraded through demethylation, carboxylation, ring opening, azo bond breakage, asymmetric cleavage, and aromatic ring removal.
eISSN:2083-5906
ISSN:1230-1485
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