首页> 外文会议>International Biohydrometallurgy Symposium, IBS-2001 Sep 16-19, 2001, Ouro Preto, Minas Gerais, Brazil >Sulfate-reducing suspension and biofilm reactors for acidic sulfate and metal containing wastewaters
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Sulfate-reducing suspension and biofilm reactors for acidic sulfate and metal containing wastewaters

机译:用于酸性硫酸盐和含金属废水的硫酸盐还原悬浮液和生物膜反应器

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Sulfate-reducing suspension and biofilm processes were studied for treatment of synthetic wastewater containing sulfate, zinc and iron. With lactate supplemented upflow anaerobic sludge blanket (UASB) and fluidized bed reactors (FBR) the following precipitation rates were obtained: 300-400 mg/l*d for Zn and 80 mg/l*d for Fe with hydraulic retention time of 16 h. The alkalinity produced in the process neutralized the pH from 2,5-3. The highest achieved sulfate reduction rate was 2000-2500 mg/l*d. In terms of sulfate reduction, hydrogen sulfide production and effluent alkalinity, the start-up of the FBR with the 10 % fluidization rate was superior to the FBRs with 20-30 % fluidization rates. With increased loading rates, high recycling rate became an advantage. After process failure caused by overloading, the sulfate reduction recovered within two weeks. Metal precipitates in the reactors were predominantly FeS_2, ZnS and FeS.
机译:研究了减少硫酸盐的悬浮液和生物膜工艺,用于处理含有硫酸盐,锌和铁的合成废水。使用乳酸补充的上流厌氧污泥层(UASB)和流化床反应器(FBR),可获得以下沉淀速率:Zn为300-400 mg / l * d,Fe为80 mg / l * d,水力停留时间为16 h 。在该过程中产生的碱度将pH从2,5-3中和。最高的硫酸盐还原速率为2000-2500 mg / l * d。在硫酸盐还原,硫化氢生成和废水碱度方面,流化率为10%的FBR的启动要优于流化率为20-30%的FBR。随着装载率的提高,高回收率成为优势。由于过载导致的过程失败后,硫酸盐还原量在两周内恢复。反应器中的金属沉淀主要是FeS_2,ZnS和FeS。

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