Wang Zhengjian, Banks Charles J
School of Civil Engineering and Environment, University of Southampton, Southampton, SO17 1BJ, UK.
Waste Manag Res. 2006 Jun;24(3):289-93. doi: 10.1177/0734242X06065232.
The effect of different dose concentrations of FeCl3 on the performance of a mesophilic anaerobic digester treating a highly alkaline, high-strength and sulphate-rich landfill leachate was tested. The results indicated that sulphate reduction was the predominant reaction and methanogenic processes were entirely inhibited in the reactor without FeCl3 addition. Adding FeCl3 into the reactor restored some methanogenic activity and also improved the rates of sulphate reduction. A combination of sulphate reduction and methanogenic activity resulted in up to 75% chemical oxygen demand (COD) removal and 85% sulphate removal. Sulphate reduction remained the principle mechanism by which COD removal took place with a methane yield of only between 0.14 and 0.18 m3 CH4 kg(-1) COD removed being achieved. The process was, however, stable and offered advantages for the further treatment or conveyance of the anaerobically treated leachate.
测试了不同剂量浓度的FeCl3对处理高碱性、高强度和富含硫酸盐的垃圾渗滤液的中温厌氧消化器性能的影响。结果表明,在不添加FeCl3的反应器中,硫酸盐还原是主要反应,产甲烷过程完全受到抑制。向反应器中添加FeCl3恢复了一些产甲烷活性,同时也提高了硫酸盐还原速率。硫酸盐还原和产甲烷活性的结合导致化学需氧量(COD)去除率高达75%,硫酸盐去除率达85%。硫酸盐还原仍然是COD去除的主要机制,实现的甲烷产量仅为每去除1 kg COD产生0.14至0.18 m3 CH4。然而,该过程是稳定的,为厌氧处理后的渗滤液的进一步处理或输送提供了优势。