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Full-scale treatment of wastewater from a biodiesel fuel production plant with alkali-catalyzed transesterification

机译:用碱催化的酯交换反应对生物柴油燃料生产厂的废水进行全面处理

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The treatment of wastewater derived from a biodiesel fuel (BDF) production plant with alkali-catalyzed transesterification was studied at full scale. The investigated wastewater treatment plant consisted of the following phases: primary adsorption/coagulation/flocculation/sedimentation processes, biological treatment with the combination of trickling filter and activated sludge systems, secondary flocculation/sedimentation processes, and reverse osmosis (RO) system with spiral membranes. All the processes were developed in a continuous mode, while the RO experiment was performed with batch tests. Two types of BDF wastewater were considered: the first wastewater (WW_i) had an average total chemical oxygen demand (COD), pH and feed flow rate of 10,850.8 mg/L, 5.9 and 2946.7 L/h, respectively, while the second wastewater (WW2) had an average total COD, pH and feed flow rate of 43,898.9 mg/L, 3.3 and 2884.6 L/h, respectively. The obtained results from the continuous tests showed a COD removal percentage of more than 90% for the two types of wastewater considered. The removal of biorefractory COD and salts was obtained with a membrane technology in order to reuse the RO permeate in the factory production cycle. The rejections percentage of soluble COD, chlorides and sulphates were 92.8%, 95.0% and 99.5%, respectively. Because the spiral membranes required a high number of washing cycles, the use of plane membranes was preferable. Finally, the RO reject material should be evaporated using the large amount of inexpensive heat present in this type of industry.
机译:大规模研究了用碱催化的酯交换反应处理生物柴油(BDF)生产厂产生的废水。所研究的废水处理厂包括以下阶段:初级吸附/混凝/絮凝/沉降过程,滴滤池和活性污泥系统相结合的生物处理,次级絮凝/沉降过程以及带有螺旋膜的反渗透(RO)系统。所有过程均以连续模式开发,而RO实验则采用批处理测试。考虑了两种类型的BDF废水:第一种废水(WW_i)的平均总化学需氧量(COD),pH和进料流速分别为10,850.8 mg / L,5.9和2946.7 L / h,而第二种废水(第二次世界大战(WW2)的平均总COD,pH和进料流速分别为43,898.9 mg / L,3.3和2884.6 L / h。连续测试获得的结果表明,考虑的两种废水的COD去除率均超过90%。通过膜技术去除了生物难降解的COD和盐,以便在工厂生产周期中重新使用RO渗透液。可溶性COD,氯化物和硫酸盐的拒绝率分别为92.8%,95.0%和99.5%。因为螺旋膜需要大量的洗涤循环,所以优选使用平面膜。最后,应使用此类工业中存在的大量廉价热量蒸发RO废料。

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