Two-Stage Anaerobic Codigestion of Crude Glycerol and Micro-Algal Biomass for Biohydrogen and Methane Production by Anaerobic Sludge Consortium

被引:15
|
作者
Sittijunda, Sureewan [1 ]
Sitthikitpanya, Napapat [2 ]
Plangklang, Pensri [2 ]
Reungsang, Alissara [2 ,3 ,4 ]
机构
[1] Mahidol Univ, Fac Environm & Resource Studies, Salaya 73170, Nakhon Pathom, Thailand
[2] Khon Kaen Univ, Fac Technol, Biotechnol Program, Khon Kaen 40002, Thailand
[3] Khon Kaen Univ, Res Grp Dev Microbial Hydrogen Prod Proc Biomass, Khon Kaen 40002, Thailand
[4] Royal Soc Thailand, Acad Sci, Bangkok 10300, Thailand
来源
FERMENTATION-BASEL | 2021年 / 7卷 / 03期
关键词
renewable energy; third generation biomass; anaerobic mixed cultures; dark fermentation; waste utilization; HYDROGEN-PRODUCTION; SEWAGE-SLUDGE; CO-DIGESTION; FOOD WASTE; FERMENTATION; BIOGAS; OPTIMIZATION; IMPROVEMENT; VALORIZATION; ENHANCEMENT;
D O I
10.3390/fermentation7030175
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Optimization of factors affecting biohydrogen production from the codigestion of crude glycerol and microalgal biomass by anaerobic sludge consortium was conducted. The experiments were designed by a response surface methodology with central composite design. The factors affecting the production of hydrogen were the concentrations of crude glycerol, microalgal biomass, and inoculum. The maximum hydrogen production (655.1 mL-H-2/L) was achieved with 13.83 g/L crude glycerol, 23.1 g-VS/L microalgal biomass, and 10.3% (v/v) inoculum. The hydrogenic effluents obtained under low, high, and optimal conditions were further used as substrates for methane production. Methane production rates and methane yield of 868.7 mL-CH4/L and 2.95 mL-CH4/L-h were attained with the effluent produced under optimum conditions. The use of crude glycerol and microalgal biomass as cosubstrates had an antagonistic effect on biohydrogen production and a synergistic effect on methane fermentation. The two-stage process provided a more attractive solution, with a total energy of 1.27 kJ/g-VSadded, than the one-stage process.
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页数:17
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