M. Krapivina, Tõnu Kurissoo, Viktoria Blonskaja, S. Zub, R. Vilu
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引用次数: 8
摘要
采用厌氧序批式反应器(ASBR)对含硫酸盐酵母工业废水进行了厌氧中温发酵。研究了三种不同的处理方案——加和不加聚合物填料的ASBR和耦合的微氧/厌氧SBR (CSBR)。确定了反应器中污泥的最佳浓度(总固体量17.3 g L -1)和最佳反应时间(22 h)。结果表明,在体积加载速率为7.7 ~ 8.0 kgCOD m -3 d -1、COD/(SO4) 2-比为8.0时,ASBR处理的化学需氧量(COD)去除率为75 ~ 82%。在最佳条件下,沼气的甲烷含量为60%。在CSBR中,当反应器出水硫化物浓度约为10 mg L -1时,硫酸盐脱除效果最佳(99%)。由于不溶性沉积物(可能是caco3和Ca3(PO4)2)的形成,这些反应器长期开采后处理效率下降。
Treatment of sulphate containing yeast wastewater in an anaerobic sequence batch reactor; 38–52
Anaerobic mesophilic fermentation of sulphate containing yeast industry wastewaters at laboratory scale with anaerobic sequence batch reactors (ASBR) was studied. Three different treat- ment schemes were investigated - ASBR with and without a polymeric filler and coupled micro- aerophilic/anaerobic SBR (CSBR). The optimal concentration of sludge (total solids 17.3 g L -1 ) in the reactor and the optimal reaction time (22 h) were determined. It was shown that in the case of ASBR efficient treatment characterized by chemical oxygen demand (COD) removal of 75-82% took place at volume loading rates up to 7.7-8.0 kgCOD m -3 d -1 and at COD/(SO4) 2- ratio 8.0. In optimal conditions the methane content of the biogas was 60%. The best results for sulphate removal (99%) were achieved in the CSBR with the concentration of sulphide in the reactor effluent being a bout 10 mg L -1 . Decreasing treatment efficiency after a long-time exploitation of these reactors occurred as a result of the formation of insoluble sediment (presumably CaCO 3 and Ca3(PO4)2).