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Ferrous Sulphate From Titanium Dioxide Industry in Organic and Inorganic Contaminant Removal from Petroleum Refinery Wastewater

机译:石油炼油厂废水中有机和无机污染物中的二氧化钛行业的硫酸亚铁

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The capability of FeSO4 in the treatment of petroleum refinery wastewater was studied. The removal/reduction efficiency for color, total suspended solids, turbidity and chemical oxygen demand were calculated. The coagulation-flocculation process can be monitored through the measurement of zeta potential and z-average hydrodynamic diameter. At very low pH, charge neutralization is responsible for the particle aggregation while at high pH, sweep flocculation mechanism is responsible for the particle aggregation. At high pH and high coagulant dosages, FeSO4 formed solid iron (II) hydroxide and colloidal particles were 'swept out' from the wastewater and settled. Response surface methodology was applied to obtain the optimum pH and coagulant dosage. Quadratic models indicated that 623 mg/L of FeSO_4 at pH 11 achieved 73.2% color removal, 96.6% TSS removal, 79.4% turbidity removal and 42.7% COD reduction.
机译:研究了FeSO4在处理石油炼油废水中的能力。计算颜色,总悬浮固体,浊度和化学需氧量的去除/减少效率。可以通过测量Zeta电位和Z平均水动力直径来监测凝固 - 絮凝过程。在非常低的pH下,电荷中和在高pH时对颗粒聚集负责,扫描絮凝机制负责颗粒聚集。在高pH和高凝结剂剂量下,FeSO4形成的固体铁(II)氢氧化铁和胶体颗粒从废水中“扫过”并沉降。施加响应面方法是应用以获得最佳pH和凝结剂剂量。二次模型表明,在pH11的623mg / L的FeSO_4实现了73.2%的颜色去除,96.6%TSS去除,浊度79.4%和42.7%COD减少。

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