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.