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Experimental and CFD simulation study on anaerobic digestion using dextran pharmaceutical wastewater based on cyclic fluidization hydraulic mixing

机译:对厌氧实验和CFD仿真研究使用右旋糖酐制药废水消化基于循环流化液压混合

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摘要

Pharmaceutical wastewater is a kind of high-hazardous waste. To realize non-waste production, experiment and computational fluid dynamics (CFD) simulation were performed to reveal the hydraulic mechanism of mixing modes. Three digesters, numbered 0# (no-port), 1# (one-port), and 4# (four-port), were conducted by dextran pharmaceutical wastewater. Digester 0# is the control group without mixing. Mixing mode of bottom inlet and high-position outlet is employed to 1# and 4#, the outlets of 1# and 4# are centralized outlet with only one port and distributed outlets with four ports, respectively. Experiment result shows the daily biogas production of 1# and 4# are 45% and 58% higher than 0#, and the pollutants removal rate increased 20% and 24%, respectively. CFD simulation shows the second phase (dextran wastewater) of 4# failing to form a complete hydraulic path like the first phase (water), which explain the mixing modes can greatly improve the biogas yield, but the four-port mode has a weaker advantage than the one-port.
机译:制药废水是一种high-hazardous浪费。生产、试验和计算流体动力学模拟(CFD)进行揭示了液压混合机制模式。三个消化器,编号0 #(没有端口),1 #(单端),4 #(四个端口),是由右旋糖酐制药废水。对照组没有混合。底部采用进口和近出口1 #和4 #,1 #和4 #的网点只有一个港口和集中的出口分布式媒体有四个港口,分别。沼气生产1 #和4 #分别是45%和58%高于0 #,污染物去除率分别增加了20%和24%。模拟显示第二阶段(右旋糖酐废水)的4 #未能形成一个完整的液压路径像第一阶段(水),这解释混合模式可以大大吗提高沼气产量,但四个端口的模式有一个比孔性较弱的优势。

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