三相生物流化床处理高浓度丙烯酸丁酯生产废水

采用三相生物流化床工艺处理模拟丙烯酸丁酯生产废水,考察了进水丙烯酸浓度、对甲基苯磺酸浓度、容积负荷、水力停留时间对废水处理效果的影响.结果表明,该工艺适合于丙烯酸丁酯废水的高负荷处理.进水中100 mg/L丙烯酸及50 mg/L的对甲基苯磺酸对生物流化床中未经驯化的微生物具有明显的毒害作用,经过2周左右的驯化,毒害作用...

Treatment of High-Concentration Butyl-Acrylate-Production Wastewater by A Three-Phase Biological Fluidized Bed Reactor

The butyl-acrylate-production wastewater was treated by a three-phase biological fluidized bed reactor. The influences of acrylic acid concentrations, p-toluenesulfonic acid concentrations, volumic load and hydraulic retention time on pollutants removal efficiencies were investigated. It was indicated that the reactor was suitable for the treatment of butyl-acrylate-production wastewater at a high loading rate. Acrylic acid of 100 mg/L or p-toluenesulfonic acid of 50 mg/L in the influent can inhibit the unacclimated microorganisms in the fluidized bed reactor. The inhibition effects were eliminated after an acclimation of two weeks. Acrylic acid and p-toluenesulfonic acid could be removed completely at COD loading rates up to 11.56-13.56 kg/(m3 x d). The effluent COD could satisfy the demand of Class II in Chinese Integrated Wastewater Discharge Standard (GB 8978-1996) at COD loading rates up to 8.86 kg/(m3 x d) when influent COD concentration is below 2000 mg/L. When the influent COD concentration was increased to 9550-11,800 mg/L(acrylic acid of 6244 mg/L and p-toluenesulfonic acid of 1000 mg/L), the effluent COD was 271-360 mg/L, which satisfied the demand of Class III in Chinese Integrated Wastewater Discharge Standard (GB 8978-1996) at COD loading rates of 7.96-9.83 kg/(m3 x d).