2010
DOI: 10.1139/a10-011
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Anaerobic digestion from the viewpoint of microbiological, chemical, and operational aspects — a review

Abstract: Anaerobic digestion (AD) is intrinsically a sequential complex chemical and biochemical process, and many factors (microbiological, operational, and chemical) can affect its performance. The great complexity of AD may lead to many serious problems (such as instability, long retention times, low efficiency, and high polluted supernatant) that prevent this technique from being widely used and commercialized. The aim of this paper is to review the present knowledge of the AD process in view of its microbiological… Show more

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Cited by 300 publications
(171 citation statements)
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“…The EL interaction energy was calculated as follows [16]: (6) where is the zeta potential of M. barkeri and the support material surfaces and assumed to be the same as the surface potential, is the electrical permittivity of the medium (8.854 x 10 -12 C 2 J -1 m -1 ) [22,27], His the separation distance and is the double layer thickness, calculated as [16]:…”
Section: Xdlvo Energy Profilesmentioning
confidence: 99%
“…The EL interaction energy was calculated as follows [16]: (6) where is the zeta potential of M. barkeri and the support material surfaces and assumed to be the same as the surface potential, is the electrical permittivity of the medium (8.854 x 10 -12 C 2 J -1 m -1 ) [22,27], His the separation distance and is the double layer thickness, calculated as [16]:…”
Section: Xdlvo Energy Profilesmentioning
confidence: 99%
“…The most popular method of sludge stabilization is methane fermentation, which is a multi-track process that transforms organic compounds into biogas and digested sludge. Methane fermentation has become an alternative energy source because methane from biogas can be used to produce heat during combustion and energy cogeneration (Pokój et al 2014, Amani et al 2010.…”
Section: Introductionmentioning
confidence: 99%
“…Based on these observations as well as the increased gas production that followed, it is reasonable to assume that the straw degradation in the pilot-scale digester was occurring by Day 14 of the digestion cycle. Following VFA accumulation, concentrations settled around 400 mgHAc/L which is within the optimum range of 50 to 500 mgHAc/L for anaerobic digestion [27], signifying stable digester performance.…”
Section: Discussionmentioning
confidence: 80%
“…The primary reason for this difference is the lack of mixing capacity in the pilot-scale reactor. Lack of mixing typically results in less methane production and incomplete digestion since there is no uniform distribution of substrate, inocula and enzymes [27]. Internal mixing components for dry digestion systems require lots of energy and maintenance since the material is heavy and immobile.…”
Section: Discussionmentioning
confidence: 99%
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