Hydrogen fermentation of organic wastewater with high ammonium concentration via electrodialysis system

被引:7
|
作者
Xia, Ao [1 ,2 ]
Wei, Pengfei [1 ,2 ]
Sun, Chihe [1 ,2 ]
Show, Pau-Loke [3 ]
Huang, Yun [1 ,2 ]
Fu, Qian [1 ,2 ]
机构
[1] Chongqing Univ, Key Lab Low Grade Energy Utilizat Technol & Syst, Minist Educ, Chongqing 400044, Peoples R China
[2] Chongqing Univ, Inst Engn Thermophys, Sch Energy & Power Engn, Chongqing 400044, Peoples R China
[3] Univ Nottingham Malaysia Campus, Fac Engn, Dept Chem & Environm Engn, Jalan Broga Semenyih, Selangor 43500, Darul Ehsan, Malaysia
基金
美国国家科学基金会;
关键词
Hydrogen production; Ammonium removal; Organic wastewater; Electrodialysis reactor; Advanced fermentation system; VOLATILE FATTY-ACIDS; BIOFILM REACTOR; INHIBITION; RECOVERY; REMOVAL; MICROALGAE; NUTRIENTS;
D O I
10.1016/j.biortech.2019.121560
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
An advanced electrodialysis fermentation system was set up to remove ammonium during hydrogen fermentation. When the voltage was increased from 0 to 6 V, the average ammonium removal rate was improved from 8.7 to 31.1 mg/L/h at an initial ammonium concentration of 3000 mg/L. A model based on the Nernst-Plank equation and porous media properties of ion exchange membranes was successfully implemented to predict the ammonium removal performance. When such a system was fed with synthetic wastewater at an ammonium concentration of 3000 mg/L for hydrogen fermentation, a significant increase in specific hydrogen yield was observed in the experiment group at 4 V. Specific hydrogen yield was 225.0 mL/g glucose, this value is 47.9% higher than the control. Moreover, ammonium concentration in experiment group was reduced to 701.6 mg/L at 72 h when voltage was set at 4 V, which is 63.7% lower than that in 0 V experiment group.
引用
收藏
页数:9
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