Feasibility of microalgae cultivation system using membrane-separated CO2 derived from biogas in wastewater treatment plants

被引:4
作者
Takabe, Yugo [1 ,3 ]
Himeno, Shuji [2 ]
Okayasu, Yuji [1 ]
Minamiyama, Mizuhiko [1 ,4 ]
Komatsu, Toshiya [2 ]
Nanjo, Kouhei [2 ]
Yamasaki, Yukiyo [1 ]
Uematsu, Ryuji [1 ]
机构
[1] Publ Works Res Inst, Innovat Mat & Resources Res Ctr, Mat & Resources Res Grp, 1-6 Minamihara, Tsukuba, Ibaraki 3058516, Japan
[2] Nagaoka Univ Technol, Dept Civil & Environm Engn, 1603-1 Kamitomiokamachi, Nagaoka, Niigata 9402188, Japan
[3] Tottori Univ, Grad Sch Engn, 4-101 Koyamae Minami, Tottori 6808552, Japan
[4] Publ Works Res Inst, Water Qual Res Team, 1-6 Minamihara, Tsukuba, Ibaraki 3058516, Japan
关键词
CO2; Biogas; Membrane separation; Wastewater treatment plant; Indigenous microalgae; Energy balance analysis; INDIGENOUS MICROALGAE; BIOMASS PRODUCTION; MODEL; OPTIMIZATION;
D O I
10.1016/j.biombioe.2017.09.004
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Utilising CO2 from biogas as a carbon source can introduce energy production systems incorporating microalgae cultivation into wastewater treatment plants (WWTPs). In this study, the effects of utilising membrane-separated CO2 (MSC; CO2 content: 983 +/- 11 dm(3) m(-3))-obtained from biogas using a newly developed separation system-on indigenous microalgae cultivation with treated effluents was investigated. Assuming model cultivation systems, energy balance analysis was conducted to evaluate the feasibility of MSC utilisation and its superiority over flue gas CO2 (FC) from power plants (PPs). Scenarios 1 and 2 used generated biogas of 11.6 and 116 dm(3) s(-1), and produced MSC (carbon based) were 0.802 and 8.02 g s(-1), respectively. Experiments comparing MSC (suspended solids (SS): 166 +/- 23 mg dm(-3); higher heating value (HHV): 21.1 +/- 0.46 kJ g(-1)) with commercial CO2 (SS: 176 +/- 16 mg dm(-3); HHV: 21.2 +/- 0.90 kJ g(-1)) revealed no negative effects on microalgae activity, biomass production, or energy content. Energy revenue of the MSC utilisation system was 27.0 MJ per 1 kg injected MSC, which is greater than the energy costs (18.2 and 17.1 MJ kg(-1) in scenarios 1 and 2, respectively). MSC utilisation is energetically feasible, and energetically superior to FC utilisation when the PPto-WWTP distance is over 0.6 and 1.9 km in scenarios 1 and 2, respectively. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:191 / 198
页数:8
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