首页> 外文期刊>Fresenius Environmental Bulletin >SUBMERGED MEMBRANE BIOREACTOR AND SECONDARY DIGESTION FOR THE TREATMENT OF WINE DISTILLERY WASTEWATER. PART Ⅰ: RAW WINE DISTILLERY WASTEWATER DIGESTION
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SUBMERGED MEMBRANE BIOREACTOR AND SECONDARY DIGESTION FOR THE TREATMENT OF WINE DISTILLERY WASTEWATER. PART Ⅰ: RAW WINE DISTILLERY WASTEWATER DIGESTION

机译:浸没式膜生物反应器和二次消化处理酒厂废水。第一部分:原酒蒸馏废水的消化

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摘要

A combination of a submerged membrane bioreactor (SMBR) and a secondary digester was tested for the treatment of wine distillery wastewater (WDW). The experimental system, consisting of four individual reactors, was tested during a 30-days study. Buffering of pH was achieved by mixing the feed stream of the system with 1000 mg/l of CaCO_3 and K_2HPO_4 for the initial 10 days of the bioreactor system operation, and with 8000 mg/l of CaCO_3 and 4000 mg/l of K_2HPO_4 for the remainder of the study. Buffering proved to be significant for optimum performance of the system in removal of soluble chemical oxygen demand (COD_S), and volatile fatty acids (VFAs). Different batches of WDW used for feeding the reactor had variable compositions with respect to concentrations of nitrates, ammonium and the total concentration of phenolic compounds. Ammonium accumulated in the secondary digester after 14 days of treatment system operation, indicating the time required for the establishment of anaerobic conditions in the system. An additional step would be required for removal of phosphates from the effluent of the bioreactor, e.g., reverse osmosis, if the effluent is to be reused in production or other applications.
机译:测试了浸没式膜生物反应器(SMBR)和二级消化池的组合,用于处理酒厂废水(WDW)。在为期30天的研究中,对由四个单独的反应器组成的实验系统进行了测试。在生物反应器系统运行的最初10天,将系统的进料流与1000 mg / l的CaCO_3和K_2HPO_4混合,并与8000 mg / l的CaCO_3和4000 mg / l的K_2HPO_4混合,实现pH缓冲。研究的其余部分。事实证明,缓冲对于系统在去除可溶性化学需氧量(COD_S)和挥发性脂肪酸(VFA)方面的最佳性能至关重要。用于进料反应器的不同批次的WDW在硝酸盐,铵的浓度和酚类化合物的总浓度方面具有可变的组成。处理系统运行14天后,二级消化池中积累的铵盐表明系统中建立厌氧条件所需的时间。如果废水要在生产或其他应用中重复使用,则需要额外的步骤从生物反应器的废水中除去磷酸盐,例如,反渗透。

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