Improved biogas production of dry anaerobic digestion of swine manure

2019 ◽  
Vol 294 ◽  
pp. 122188 ◽  
Author(s):  
Youqian Xiao ◽  
Hongnan Yang ◽  
Han Yang ◽  
Hong Wang ◽  
Dan Zheng ◽  
...  
2017 ◽  
Vol 5 (1) ◽  
pp. 32-37
Author(s):  
Ondiba Hesborn Andole ◽  
Zhongfang Lei ◽  
Zhenya Zhang ◽  
James Raude ◽  
Christopher Kanali

2021 ◽  
Author(s):  
Akinola David Olugbemide ◽  
Blaž Likozar ◽  
Ana Oberlintner ◽  
Uroš Novak ◽  
Ekebafe Lawrence

Abstract In this research study, the impact of the feedstock to the inoculum (F/I) amount ratio in the dry anaerobic digestion (DAD) of Hura crepitans leaves was evaluated. Measured biogas volumes, as well as the chemical kinetic predictions for exponential, logistic and Gompertz model, depicting the agreement of the simulations over time, were also determined. From the F/I equivalents 2, 4 and 6 at 22 % of packed total solids, which were considered in analysis test procedure, the DAD digester with F/I number 4 was the most promising in terms of biogas’ production rate. Its daily methane/carbon dioxide was 690 mL, while cumulative generation productivity was greater than 2 L/sample, respectively. On the other hand, the DAD reaction with F/I contained 6, recorded the lowest related expressed primary matter of < 1 L. An associated early commencement of the organic material breakdown in all bio vessels was indicative of a good start-up phase, which is one of the challenges, often encountered in DAD process. Furthermore, applied experimental methods revealed the direct correlation phenomena between biodegradability physical constants, measured molecular CH4/CO2 synthesis and simulations. Hura crepitans being an invasive plant species makes its lignocellulosic fractions desired in terms of valorisation, as it is not competing with agricultural crop products. Modelling can, moreover, contribute to consecutive operation optimisation, scaling and integrating, also taking dynamics under consideration. As opposed to bio-refining wood residues, where individual cellulose, hemicellulose or lignin biopolymers can be attained, degradation to yield CH4 is robust, as well as compatible in combustion.


2012 ◽  
Vol 32 (3) ◽  
pp. 404-409 ◽  
Author(s):  
Yun Xia ◽  
Daniel I. Massé ◽  
Tim A. McAllister ◽  
Carole Beaulieu ◽  
Emilio Ungerfeld

2019 ◽  
Vol 10 (1) ◽  
pp. 136 ◽  
Author(s):  
Fasil Ayelegn Tassew ◽  
Wenche Hennie Bergland ◽  
Carlos Dinamarca ◽  
Rune Bakke

Influences of temperature (25–35 °C) and substrate particulate content (3.0–9.4 g total suspended solids (TSS)/L) on granular sludge bed anaerobic digestion (AD) were analyzed in lab-scale reactors using manure as a substrate and through modeling. Two particle levels were tested using raw (RF) and centrifuged (CF) swine manure slurries, fed into a 1.3-L lab-scale up-flow anaerobic sludge bed reactor (UASB) at temperatures of 25 °C and 35 °C. Biogas production increased with temperature in both high- and low-particle-content substrates; however, the temperature effect was stronger on high-particle-content substrate. RF and CF produced a comparable amount of biogas at 25 °C, suggesting that biogas at this temperature came mainly from the digestion of small particles and soluble components present in similar quantities in both substrates. At 35 °C, RF showed significantly higher biogas production than CF, which was attributed to increased (temperature-dependent) disintegration of larger solid particulates. Anaerobic Digestion Model No.1 (ADM1) based modeling was carried out by separating particulates into fast and slow disintegrating fractions and introducing temperature-dependent disintegration constants. Simulations gave a better fit for the experimental data than the conventional ADM1 model.


2013 ◽  
Vol 726-731 ◽  
pp. 2875-2880
Author(s):  
Wen Hao Liu ◽  
Shi Jie Tian ◽  
Shu Biao Wu ◽  
Xiao Qian Zhang ◽  
Chang Le Pang ◽  
...  

The possible exploitation of two-phase anaerobic digestion for swine manure was investigated in this study. One-phase and two-phase anaerobic digestion process were investigated in continuous stirred-tank reactor with hydraulic retention times 15 days (hydrolysis and acidification for 3 days and methanogenic12 days in two-phase). When the organic loading rates were equal to or less than 4 g VS/L day, the biogas yield and volumetric production of two processes were no significant difference. However, in the case of organic loading rates being equal to or higher than 5.0 g VS/L day, two-phase biogas yield and volumetric biogas production averaged 0.294 L CH4/g VS added and 2.218 L/L day, compared with one-phase averaged 0.255L CH4/g VS added and 2.168 L/L day, respectively. Significant advantages in saving cost of biogas project were indicated by the comparison of biogas production and COD degradation in the one-phase and two-phase processes.


2021 ◽  
pp. 126438
Author(s):  
Shichao Zheng ◽  
Fei Yang ◽  
Wenli Huang ◽  
Zhongfang Lei ◽  
Zhenya Zhang ◽  
...  

2019 ◽  
Vol 282 ◽  
pp. 353-360 ◽  
Author(s):  
Yu-ying Hu ◽  
Jing Wu ◽  
Huai-zhi Li ◽  
Souhila Poncin ◽  
Kai-jun Wang ◽  
...  

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