LaMnO3钙钛矿活化过氧单硫酸盐催化棕榈油厂二次出水降解

P. S. Utama, W. Widayatno, M. Azhar, H. Abid, W. Peng, O. Muraza, E. Saputra
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引用次数: 14

摘要

采用简单的固相反应法制备了LaMnO3钙钛矿催化剂。该催化剂用于棕榈油厂(POMSE)二次出水有机含量降解过程中活化PMS。POMSE中的有机物含量与COD值相当;因此,COD值被用作过程成功的参数。催化剂性能测试表明,该催化剂能有效降低COD,废弃物达到政府规定的最大阈值。影响催化剂效能的因素有催化剂的煅烧温度、催化剂负载、PMS浓度和温度。煅烧温度影响钙钛矿晶体的形成;温度越高,催化剂活性越强。催化剂负载和PMS浓度变量影响POMSE中有机水平的降解过程;在低水平下,越高的催化剂负载和PMS浓度会提高降解过程的有效性,但在一定水平下,催化剂和PMS的添加会降低降解过程的有效性。LaMnO3-800oC催化剂活性最高,达到92.7%,满足COD < 300 mg/L的允许阈值。三种催化剂去除COD的顺序为LaMnO3-800oC > LaMnO3-700oC > LaMnO3-600 oC。拟二级动力学方程与实验数据吻合。温度对动力学常数的影响遵循Arrhenius方程。此外,所得到的催化剂是稳定的,催化剂活性在三次运行中没有明显下降。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
LaMnO3 Perovskite Activation of Peroxymonosulfate for Catalytic Palm Oil Mill Secondary Effluent Degradation
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.
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