The effect of volatile fatty acid additions on the anaerobic digestion of cellulose and glucose in batch reactors

2005 ◽  
Vol 40 (11) ◽  
pp. 3412-3418 ◽  
Author(s):  
Irene Siegert ◽  
Charles Banks
Author(s):  
Ganesh K Veluswamy ◽  
Andy Ball ◽  
Richard Dinsdale ◽  
Alan Guwy ◽  
Kalpit Shah

Methane, the final product of methanogenesis during anaerobic digestion is a low value product (0.1$/m3). Concerns over fugitive emissions from methane coupled with recent reduction in costs of solar and...


Author(s):  
Xiaobo Zhu ◽  
Aaron Leininger ◽  
David Jassby ◽  
Nicolas Tsesmetzis ◽  
Zhiyong Jason Ren

2020 ◽  
Vol 311 ◽  
pp. 123501 ◽  
Author(s):  
Weixin Zhao ◽  
Jinhui Jeanne Huang ◽  
Binbin Hua ◽  
Zhiyong Huang ◽  
Ronald L. Droste ◽  
...  

2020 ◽  
Author(s):  
Jacob Joseph Lamb

There are many methodologies for improving the biogas output from anaerobic digestion. These techniques include physical (e.g., gas production and feedstock parameters), reactor configuration and chemical parameters (e.g., pH and volatile fatty acid concentrations) within the digester can help to link particular functions and features of the process. Using this expanse of data, mathematical models can be used to understand and forecast the biological process within an anaerobic digester. Such models can then be further developed on a process and biological level to improve their ability to mimic the function of the reactor. This chapter will provide background into modelling and reactor configuration in order to obtain a digital twin of an anaerobic digester.


2015 ◽  
Vol 62 (4) ◽  
pp. 476-482 ◽  
Author(s):  
Xiaofen Li ◽  
Janis E. Swan ◽  
Giridhar R. Nair ◽  
Alan G. Langdon

2002 ◽  
Vol 46 (11-12) ◽  
pp. 153-157 ◽  
Author(s):  
H.Q. Yu ◽  
H.H.P. Fang

Experiments were conducted to study the acidogenesis of a dairy wastewater in batch reactors at pH 5.5 and 55°C. There was a biased fermentation sequence for carbohydrate and protein, and the protein fermentation was delayed by carbohydrate. The production of hydrogen was exclusively from the fermentation of carbohydrate. Acetate and butyrate concentrations both increased rapidly at the beginning and peaked at some points, then declined in the reactors fed with 8 g-COD (chemical oxygen demand)/l, or higher concentrations. Butanol and propanol fractions increased with the substrate concentration. The metabolism shifted from the volatile fatty acid-producing pathways to the alcohol-producing pathways when the substrate concentration increased beyond 8 g-COD/l. The acidogenic biomass yield was in the range 0.19-0.25 mg-VSS/mg-COD.


Sign in / Sign up

Export Citation Format

Share Document