Effect of oxidated golden shower on the adsorption of diclofenac sodium in wastewater

Author:

Arliyani Isni12ORCID,Syaifuddin Mohammad1,Ni'am Achmad Chusnun3,Murti Restu Hikmah Ayu4,Jawwad Muhammad Abdus Salam4,You Sheng‐Jie5,Kuncoro Eko Prasetyo6,Wang Ya‐Fen5

Affiliation:

1. Department of Environmental Engineering Institut Teknologi Sepuluh Nopember Surabaya Indonesia

2. Bioinformatics Research Center INBIO Indonesia Malang Indonesia

3. Department of Environmental Engineering Institut Teknologi Adhi Tama Surabaya Surabaya Indonesia

4. Department of Environmental Engineering University of Pembangunan Nasional Veteran Jawa Timur Surabaya Indonesia

5. Department of Environmental Engineering Chung Yuan Christian University Zhongli Taiwan

6. Department of Biology Airlangga University Surabaya Indonesia

Abstract

AbstractThis research aimed to modify activated carbon into oxidated activated carbon because it can effectively remove diclofenac sodium (DCF) and increase the adsorption capability. In this study of the several variations of initial concentration and contact time, those variations affected the optimal result. To determine, the removal efficiency of diclofenac sodium used Golden Shower Activated Carbon based on the contact time variation and the optimum contact time compared to Golden Shower Oxidated Activated Carbon as adsorbent on the batch method and to know the isotherm model and the kinetic model of the adsorbent on the adsorption in diclofenac sodium solution. The pHPZC for GSHAC and GSHOAC were 2.4 and 9.3. The optimum contact time for GSHAC was 225 min with the capacity (qt = 184.71 mg/g). The optimum contact time for GSHOAC was 169 min with the capacity (qt = 188.34 mg/g). The Isotherm model, kinetics model, and the physical characterization of the biosorbent were thoroughly investigated. The isotherm model chosen in the adsorption process for GSHAC and GSHOAC was the Langmuir model (R2 = 0.985 and R2 = 0.973). The pseudo‐second‐order for GSHAC and GSHOAC was confirmed to be a kinetic pseudo‐second‐order model of the adsorption with R2 values of 0.9566 and 0.9986. The model represents that the reaction from the adsorbent to the solution was double the initial concentration. Based on SEM analysis after the adsorption process, it was found that flakes of adsorbent before adsorption had many layers of pores, causing an irregular texture after adsorption showed that GSHAC and GSHOAC were fragmented and had many layers of pores that were closed and tight because it adsorbed DCF.

Publisher

Wiley

Subject

Management, Monitoring, Policy and Law,Public Health, Environmental and Occupational Health,Pollution,Waste Management and Disposal

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