LaMnO3 Perovskite Activation of Peroxymonosulfate for Catalytic Palm Oil Mill Secondary Effluent Degradation

Panca Setia Utama (Department of Chemical Engineering, Universitas Riau, Pekanbaru, Indonesia, 28293)
Wahyu Bambang Widayatno (Research Center for Physics, Indonesian Institute of Science (LIPI), Serpong, 15314, Indonesia)
Muhammad Rizwan Azhar (School of Engineering, Edith Cowan University, 270 Joondalup Drive, Joondalup, WA, Australia)
Hussein Rasool Abid (Chemical Engineering, WA School of Mines: Minerals, Energy and Chemical Engineering, Curtin University, Australia)
Wenchao Peng (School of Chemical Engineering and Technology, Tianjin University, Tianjin 300350, China)
Oki Muraza (Center of Excellence in the Department of Nanotechnology and Chemical Engineering, King Fahd University of Petroleum and Minerals, Dhahran, 31261, Saudi Arabia)
Edy Saputra (Department of Chemical Engineering, Universitas Riau, Pekanbaru, Indonesia, 28293)

Journal of Applied Materials and Technology
Vol. 2 No. 1 (2020): September 2020

The LaMnO3 perovskite catalyst was successfully synthesized using a simple solid-state reaction method. This catalyst is used to activate PMS in the organic content's degradation process in the secondary effluent palm oil mill (POMSE). The organic content in POMSE is equivalent to the COD value; thus the COD value is used as a parameter for the process's success. The catalyst performance test shows that the catalyst effectively reduces COD, and the waste meets the maximum threshold allowed by government regulations. The variables that affect the catalyst's effectiveness were the calcination temperature of the catalyst, catalyst loading, PMS concentration, and temperature. The temperature of calcination affects the perovskite crystal formation; the higher the temperature, the more active catalyst obtained. The catalyst loading and PMS concentration variables affect the degradation process of organic levels in POMSE; at low levels, the higher the catalyst loading and PMS concentrations will increase the effectiveness of the degradation process, but at certain levels, the addition of catalysts and PMS reduces the effectiveness of the process. LaMnO3-800oC catalyst presents the highest activity of 92.7% and met the allowable threshold of COD < 300 mg/L. The sequence for removal of COD among the three catalysts with an order of LaMnO3-800oC > LaMnO3-700oC > LaMnO3-600 oC. The pseudo-second-order kinetics equation fits the experimental data. The effect of temperature on the kinetics constant follows the Arrhenius equation. Furthermore, the catalyst obtained was stable, with no significant decrease in catalysts activity up to three runs.