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碱催化酯交换法全规模处理生物柴油燃料生产厂废水。

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

机构信息

ENEA (Italian National Agency for New Technologies, Energy and Sustainable Economic Development), Environment Department, Water Resource Management Laboratory, Bologna, Italy.

出版信息

Environ Technol. 2013 Mar-Apr;34(5-8):861-70. doi: 10.1080/09593330.2012.720717.

Abstract

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 (WW1) 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.

摘要

采用碱催化酯交换法处理生物柴油燃料(BDF)生产厂的废水在全规模下进行了研究。所研究的废水处理厂由以下几个阶段组成:初级吸附/混凝/絮凝/沉淀工艺、滴滤器和活性污泥系统相结合的生物处理、二级絮凝/沉淀工艺和螺旋膜反渗透(RO)系统。所有过程均以连续模式进行,而 RO 实验则采用间歇测试。考虑了两种类型的 BDF 废水:第一种废水(WW1)的平均总化学需氧量(COD)、pH 值和进料流量分别为 10,850.8 mg/L、5.9 和 2946.7 L/h,而第二种废水(WW2)的平均总 COD、pH 值和进料流量分别为 43,898.9 mg/L、3.3 和 2884.6 L/h。连续测试得到的结果表明,对于所考虑的两种类型的废水,COD 去除率均超过 90%。采用膜技术去除生物难降解 COD 和盐,以便将 RO 渗透物再用于工厂生产循环。可溶性 COD、氯化物和硫酸盐的截留率分别为 92.8%、95.0%和 99.5%。由于螺旋膜需要大量的清洗循环,因此使用平面膜更为可取。最后,RO 废物应利用该类型工业中存在的大量廉价热量进行蒸发。

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