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Experimental and CFD simulation study on anaerobic digestion using dextran pharmaceutical wastewater based on cyclic fluidization hydraulic mixing
Environmental Progress & Sustainable Energy ( IF 2.1 ) Pub Date : 2021-04-21 , DOI: 10.1002/ep.13656
Langui Xu 1 , Luqian Yang 2 , Shurui Guo 3 , Jiawei Zhou 1 , Tao Luo 4, 5 , Yi Ran 4 , Jiang Li 3, 4 , Enshen Long 3 , Zili Mei 4 , Ruyi Huang 1, 2, 4
Affiliation  

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.

中文翻译:

基于循环流化水力混合的葡聚糖制药废水厌氧消化实验及CFD模拟研究

制药废水是一种高危废物。为了实现无废物生产,进行了实验和计算流体动力学 (CFD) 模拟,以揭示混合模式的液压机制。0#(无口)、1#(一口)、4#(四口)三个消化池,用葡聚糖制药废水进行消化。消化器0#为未混合的对照组。1#和4#采用底部进水和高位出水混合方式,1#和4#出口分别为单口集中出口和四口分布式出口。实验结果表明,1#和4#沼气日产量比0#提高45%和58%,污染物去除率分别提高20%和24%。
更新日期:2021-04-21
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