摘要
采用化学破乳-Fenton试剂处理乳化液废水,考察了相关因素对处理效果的影响特点和规律。实验结果表明,酸化作用中,静电作用对破乳有着关键性影响,降低乳化液废水p H值,有利于乳化液废水的油水分离;混凝剂投加量和废水p H值直接决定着破乳效果,油滴分散体系脱稳的适宜p H值既能使油滴间静电斥力较小,又能使大分子量的、大比表面积的多核络合离子通过电中和、吸附架桥、卷扫的作用来强化油水分散体系脱稳。Fenton氧化中,对于特定的Fe2+浓度,随着n(H2O2)/n(Fe2+)增加,COD去除程度增加,但增加的幅度越来越小,同时COD去除率达到稳定所需要的时间相应增加,适宜的摩尔比为20;废水Fenton体系H2O2开始阶段急速降低然后趋于平缓,体系Fe2+反应开始很短时间内急剧降低并趋于某一稳定值,H2O2浓度、Fe2+浓度随时间变化遵循一级反应动力学模型。
The chemical demulsification-Fenton oxidation was used for the treatment of emulsion wastewater. The characteristics and laws of related factors on treatment effect were investigated. The results showed that electrostatic effect had a critical impact on demulsification,and low p H was advantageous to the oilwater separation of emulsion wastewater in acidification. The dosing amount of coagulant and the p H value of wastewater had a critical impact on demulsification. The appropriate p H value condition of unstability of oil droplets dispersed system should be as follows: smaller electrostatic repulsion between oil droplets,the existence of multi-core complexing ions having large molecular weight and specific surface. The multi-core complexing ions could strengthen the unstability of oil-water dispersions by charge neutralization,adsorption bridging and furl mechanism. In the Fenton oxidation system,the COD removal rate increased with the increase of H2O2/ Fe2 +ratio for a certain Fe2 +dosage,but the increase rate tended to be reduced. Meanwhile,the required time of COD removal rate reaching stability increased correspondingly,and the suitable molar ratio of the H2O2/ Fe2 +was 20. In the wastewater Fenton system,H2O2 concentration decreased drastically and then began to flatten,and Fe2 +concentration fell sharply in a very short time and tended to be a stable value. The change of H2O2,Fe2 +concentration with time conformed to the first order reaction kinetics model.
引文
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