Modeling of the methane production and pH value during the anaerobic co-digestion of dairy manure and spent mushroom substrate

被引:59
作者
Shi, Xiao-Shuang [1 ,3 ]
Yuan, Xian-Zheng [1 ]
Wang, Yu-Ping [1 ,2 ]
Zeng, Shu-Juan [1 ,3 ]
Qiu, Yan-Ling [1 ]
Guo, Rong-Bo [1 ]
Wang, Li-Sheng [1 ]
机构
[1] Chinese Acad Sci, Qingdao Inst Bioenergy & Bioproc Technol, Key Lab Biofuels, Qingdao 266101, Shandong, Peoples R China
[2] Jiangnan Univ, Sch Environm & Civil Engn, Wuxi 214122, Jiangsu, Peoples R China
[3] Chinese Acad Sci, Grad Univ, Beijing 100049, Peoples R China
基金
美国国家科学基金会;
关键词
Anaerobic co-digestion; Spent mushroom substrate; Dairy manure; Anaerobic Digestion Model No. 1 (ADM1); Hydraulic retention time (HRT); NO; 1; ADM1; MILL WASTE-WATER; SOLID-WASTE; RECIRCULATION; CATTAIL; REACTOR;
D O I
10.1016/j.cej.2014.02.007
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A dynamic mathematical model, based on the IWA Anaerobic Digestion Model No. 1 (ADM1), was used to predict the methane production and pH value during anaerobic co-digestion of dairy manure (DM) and spent mushroom substrate (SMS) under different hydraulic retention times (HRT). In this model the degradation of DM was modeled according to classical ADM1, while SMS was divided into inert part as well as biodegradation parts of slowly hydrolysable fraction (SHF) and readily hydrolysable fraction (RHF). The data from lab-scale experiment was used to calibrate and validate this model. The results showed that the model was able to predict reasonably well the steady-state results of methane production and pH value at HRT of 12, 20 and 28 d. The results also indicated that the model suitability to assess the combined effects of HRT and substrate ratio on the methane production and pH value. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:258 / 263
页数:6
相关论文
共 29 条
[1]  
[Anonymous], 2002, WATER INTELL ONLINE, DOI DOI 10.2166/9781780403052
[2]  
[Anonymous], FAO PROD YB
[3]   Co-digestion of pig manure and glycerine: Experimental and modelling study [J].
Astals, S. ;
Ariso, M. ;
Gali, A. ;
Mata-Alvarez, J. .
JOURNAL OF ENVIRONMENTAL MANAGEMENT, 2011, 92 (04) :1091-1096
[4]   The influence of substrate kinetics on the microbial community structure in granular anaerobic biomass [J].
Batstone, DJ ;
Keller, J ;
Blackall, LL .
WATER RESEARCH, 2004, 38 (06) :1390-1404
[5]   Steady-state analysis of the Anaerobic Digestion Model No. 1 (ADM1) [J].
Bornhoeft, Astrid ;
Hanke-Rauschenbach, Richard ;
Sundmacher, Kai .
NONLINEAR DYNAMICS, 2013, 73 (1-2) :535-549
[6]   Modelling of the mesophilic anaerobic co-digestion of olive mill wastewater with olive mill solid waste using anaerobic digestion model No. 1 (ADM1) [J].
Boubaker, Fezzani ;
Ridha, Ben Cheikh .
BIORESOURCE TECHNOLOGY, 2008, 99 (14) :6565-6577
[7]   EFFECT OF HYDRAULIC RETENTION TIME ON UP-FLOW ANAEROBIC STAGE REACTOR PERFORMANCE AT CONSTANT LOADING IN THE PRESENCE OF ANTIBIOTIC TYLOSIN [J].
Chelliapan, S. ;
Wilby, T. ;
Sallis, P. J. .
BRAZILIAN JOURNAL OF CHEMICAL ENGINEERING, 2011, 28 (01) :51-61
[8]   Application of the IWA ADM1 model to simulate anaerobic co-digestion of organic waste with waste activated sludge in mesophilic condition [J].
Derbal, K. ;
Bencheikh-Iehocine, M. ;
Cecchi, F. ;
Meniai, A. -H. ;
Pavan, P. .
BIORESOURCE TECHNOLOGY, 2009, 100 (04) :1539-1543
[9]   Modelling the effect of the OLR and OFMSW particle size on the performances of an anaerobic co-digestion reactor [J].
Esposito, G. ;
Frunzo, L. ;
Panico, A. ;
Pirozzi, F. .
PROCESS BIOCHEMISTRY, 2011, 46 (02) :557-565
[10]   Implementation of IWA anaerobic digestion model No. 1 (ADM1) for simulating the thermophilic anaerobic co-digestion of olive mill wastewater with olive mill solid waste in a semi-continuous tubular digester [J].
Fezzani, Boubaker ;
Ben Cheikh, Ridha .
CHEMICAL ENGINEERING JOURNAL, 2008, 141 (1-3) :75-88