Investigating the Result of Current Density, Temperature, and Electrolyte Concentration on COD: Subtraction of Petroleum Refinery Wastewater Using Response Surface Methodology

被引:10
作者
Chakawa, Sharon [1 ]
Aziz, Mujahid [1 ]
机构
[1] Cape Peninsula Univ Technol, Environm Engn Res Grp EnvERG, Dept Chem Engn, Fac Engn & Built Environm, POB 1906, ZA-7535 Cape Town, South Africa
关键词
box-behnken design; electrochemical oxidation; petroleum refinery wastewater; chemical oxygen demand; response surface methodology; remediation; dimensional stable anode; ELECTROCHEMICAL OXIDATION PROCESS; OPTIMIZATION; DEGRADATION; PERFORMANCE; REMOVAL; PHENOL; PARAMETERS; EFFLUENT; AMMONIA; ANODES;
D O I
10.3390/w13060835
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Electrochemical oxidation (EO) investigated chemical oxygen demand (COD) subtraction from petroleum refinery wastewater (PRW) as a capable remediation process. Titanium substrates coated with iridium-tantalum oxide mixtures (Ti/IrO2-Ta2O5) were used as the dimensional stable anode (DSA). The Box-Behnken Design (BBD), a statistical experimental design and response surface methodology (RSM), was used to matrix the current density, temperature, and electrolyte (NaCl) concentration variables, with COD removal efficiency as the response factor. A second-order verifiable relationship between the response and independent variables was derived where the analysis of variance displayed a high coefficient of determination value (R-2 = 0.9799). The predicted values calculated with the model equations were very close to the experimental values where the model was highly significant. Based on the BBD for current density, the optimum process conditions, temperature and electrolyte (NaCl) concentration were 7.5 mA/cm(2), 42 degrees C and 4.5 g/L, respectively. They were resulting in a COD removal efficiency of 99.83% after a 12-hour EO period.
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页数:11
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