Effect of food to vegetable waste ratio on acidogenesis and methanogenesis during two-stage integration

被引:30
作者
Chakraborty, Debkumar [1 ,2 ]
Mohan, S. Venkata [1 ]
机构
[1] Indian Inst Chem Technol, CSIR, Bioengn & Environm Sci Lab, EEFF Dept, Hyderabad 500007, Andhra Prades, India
[2] Jain Univ, Dept Food Technol, Ctr Emerging Technol, Bangalore 562112, Karnataka, India
关键词
Anaerobic digestion; Food waste; Vegetable waste; Lactic acid; Rate kinetics; Methanogenesis; ANAEROBIC-DIGESTION; ACID PRODUCTION; SEWAGE-SLUDGE; HYDROLYSIS; FERMENTATION; REACTOR; DEGRADATION; BIOHYDROGEN; INHIBITION; HYDROGEN;
D O I
10.1016/j.biortech.2018.01.051
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
' The mixing ratio of food waste (FW) to vegetable waste (VW) (2:3 FW:VW similar to 152.51 g VS and 2:1 FW:VW similar to 137.03 gVS) was optimized using two-stage (LBR-UASB) experimental process depending upon volatile solid (VS) load. The effect of FW to VW ratio was studied in Leach Bed Reactor (LBR) towards leachate production. Results revealed that hydrolysis rate (73.11%), sCOD (3294.3 g/KgVS) and tVFA (2664 g/KgVS) yield was higher in 2:1 FW:VW ratio. Acetate, propionate, lactate and methane yield for 2:3 FW:VW (420 g/KgVS, 87 g/KgVS, 180 g/KgVS and 226.86 ml/gVS respectively) was different from 2:1 FW:VW (340 g/KgVS, 247 g/KgVS, 340 g/KgVS and 218.54 ml/gVS respectively). 2:3 FW:VW ratio depicted higher VS (53.96%) and COD (54.1%) removal than 2:1 FW:VW ratio 46.34% and 41.8% respectively. VW addition regulated pH, restricted propionate and lactate production with enhanced methanogenesis by improving acetate production in two-stage AD process which further boosted process stability and efficiency.
引用
收藏
页码:256 / 263
页数:8
相关论文
共 34 条
[1]   The effect of calcium on the anaerobic digestion treating swine wastewater [J].
Ahn, Johng-Hwa ;
Do, Trong Hoan ;
Kim, Sang D. ;
Hwang, Seokhwan .
BIOCHEMICAL ENGINEERING JOURNAL, 2006, 30 (01) :33-38
[2]  
AlMamun M. R, 2015, J CLEAN ENERGY TECHN, V3, P5
[3]  
[Anonymous], 2005, Standard methods for the examination of water and waste- water
[4]   Kinetic modelling of the hydrolysis, acidogenic and methanogenic steps in the anaerobic digestion of two-phase olive pomace (TPOP) [J].
Borja, R ;
Martín, A ;
Sánchez, E ;
Rincón, B ;
Raposo, F .
PROCESS BIOCHEMISTRY, 2005, 40 (05) :1841-1847
[5]   PROTEIN-DEGRADATION IN ANAEROBIC-DIGESTION - INFLUENCE OF VOLATILE FATTY-ACIDS AND CARBOHYDRATES ON HYDROLYSIS AND ACIDOGENIC FERMENTATION OF GELATIN [J].
BREURE, AM ;
MOOIJMAN, KA ;
VANANDEL, JG .
APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 1986, 24 (05) :426-431
[6]  
Chakraborty D., 2017, BIOMASS BIOENERGY
[7]   Food waste biorefinery: Sustainable strategy for circular bioeconomy [J].
Dahiya, Shikha ;
Kumar, A. Naresh ;
Sravan, J. Shanthi ;
Chatterjee, Sulogna ;
Sarkar, Omprakash ;
Mohan, S. Venkata .
BIORESOURCE TECHNOLOGY, 2018, 248 :2-12
[8]   Acidogenic fermentation of food waste for volatile fatty acid production with co-generation of biohydrogen [J].
Dahiya, Shikha ;
Sarkar, Omprakash ;
Swamy, Y. V. ;
Mohan, S. Venkata .
BIORESOURCE TECHNOLOGY, 2015, 182 :103-113
[9]   Performance of leaching bed reactor converting the organic fraction of municipal solid waste to organic acids and alcohols [J].
Dogan, E. ;
Dunaev, T. ;
Erguder, T. H. ;
Demirer, G. N. .
CHEMOSPHERE, 2009, 74 (06) :797-803
[10]  
Food and Agriculture Organization of the United Nations Rome, 2009, VIAL TERM CAR