Abstract:Anaerobic co-digestion requires the digestion of two or more homogenous substrates to produce biogas. The superlative participated condition is when principal amount of most important substrate (example manure or sewage sludge) is combined and fermented with each other with lesser quantities of single, or a variety of additional substrate. The co-digestion of one or more substrates commonly improves the biogas output from anaerobic digesters owing to positive improvement brought about in the digestion medium a… Show more
“…The respective industrial process is implemented using one-step or two-step reactors in singe-phase or double-phase as a specific batch or applying continuous operation, with or without liquid phase recirculation [13]. Depending on the feedstock and system design, biogas typically consists of 55-70% CH 4 , 25-40% CO 2 , <2% N 2 , <0.5 O 2 , <0.5% H 2 S, 1-5% H 2 O, <0.5% NH 3 , 0-50 mg/m 3 SiO, 6-7.5 kWh/m 3 Hs [38,39]. Generally, raw biogas provides a methane concentration of 50-70% and its HHV is approximately 37.78 MJ/mn 3 .…”
Section: Ad Process/technologymentioning
confidence: 99%
“…), could produce satisfying yields of energy. On that account, techniques that increase the lignocellulosic biomass accessibility towards the achievement of anaerobic microbial decomposition are highly demanded [38].…”
Section: Progress On Ad Process Improvementmentioning
Nowadays, the climate mitigation policies of EU promote the energy production based on renewable resources. Anaerobic digestion (AD) constitutes a biochemical process that can convert lignocellulosic materials into biogas, used for chemical products isolation or energy production, in the form of electricity, heat or fuels. Such practices are accompanied by several economic, environmental and climatic benefits. The method of AD is an effective method of utilization of several different low-value and negative-cost highly available materials of residual character, such as the lignocellulosic wastes coming from forest, agricultural or marine biomass utilization processes, in order to convert them into directly usable energy. Lignin depolymerization remains a great challenge for the establishment of a full scale process for AD of lignin waste. This review analyzes the method of anaerobic digestion (biomethanation), summarizes the technology and standards involved, the progress achieved so far on the depolymerization/pre-treatment methods of lignocellulosic bio-wastes and the respective residual byproducts coming from industrial processes, aiming to their conversion into energy and the current attempts concerning the utilization of the produced biogas. Substrates’ mechanical, physical, thermal, chemical, and biological pretreatments or a combination of those before biogas production enhance the hydrolysis stage efficiency and, therefore, biogas generation. AD systems are immensely expanding globally, especially in Europe, meeting the high demands of humans for clean energy.
“…The respective industrial process is implemented using one-step or two-step reactors in singe-phase or double-phase as a specific batch or applying continuous operation, with or without liquid phase recirculation [13]. Depending on the feedstock and system design, biogas typically consists of 55-70% CH 4 , 25-40% CO 2 , <2% N 2 , <0.5 O 2 , <0.5% H 2 S, 1-5% H 2 O, <0.5% NH 3 , 0-50 mg/m 3 SiO, 6-7.5 kWh/m 3 Hs [38,39]. Generally, raw biogas provides a methane concentration of 50-70% and its HHV is approximately 37.78 MJ/mn 3 .…”
Section: Ad Process/technologymentioning
confidence: 99%
“…), could produce satisfying yields of energy. On that account, techniques that increase the lignocellulosic biomass accessibility towards the achievement of anaerobic microbial decomposition are highly demanded [38].…”
Section: Progress On Ad Process Improvementmentioning
Nowadays, the climate mitigation policies of EU promote the energy production based on renewable resources. Anaerobic digestion (AD) constitutes a biochemical process that can convert lignocellulosic materials into biogas, used for chemical products isolation or energy production, in the form of electricity, heat or fuels. Such practices are accompanied by several economic, environmental and climatic benefits. The method of AD is an effective method of utilization of several different low-value and negative-cost highly available materials of residual character, such as the lignocellulosic wastes coming from forest, agricultural or marine biomass utilization processes, in order to convert them into directly usable energy. Lignin depolymerization remains a great challenge for the establishment of a full scale process for AD of lignin waste. This review analyzes the method of anaerobic digestion (biomethanation), summarizes the technology and standards involved, the progress achieved so far on the depolymerization/pre-treatment methods of lignocellulosic bio-wastes and the respective residual byproducts coming from industrial processes, aiming to their conversion into energy and the current attempts concerning the utilization of the produced biogas. Substrates’ mechanical, physical, thermal, chemical, and biological pretreatments or a combination of those before biogas production enhance the hydrolysis stage efficiency and, therefore, biogas generation. AD systems are immensely expanding globally, especially in Europe, meeting the high demands of humans for clean energy.
“…The non-edible parts of agricultural residues that can be used as feedstock for biogas production include leaves, corn stover, groundnut shell, cocoa pod, cassava peel, straw, etc. They are available in abundance globally and are cost-effective, with a vast capacity for biotransformation into biofuels and other ancillary products [11,12]. Hydrolysis, acidogenesis, acetogenesis, and methanogenesis are the four vital biological and chemical stages of anaerobic digestion.…”
Enzymatic hydrolysis of lignocellulose materials has been identified as the rate-limiting step during anaerobic digestion. The application of pretreatment techniques can influence the biodegradability of lignocellulose substrate. This study combined Fe3O4 nanoparticles, which serve as a heterogeneous catalyst during anaerobic digestion, with different particle sizes of Arachis hypogea shells. Batch anaerobic digestion was set up at mesophilic temperature for 35 days. The results showed that 20 mg/L Fe3O4 additives, as a single pretreatment, significantly influence biogas and methane yields with an 80.59 and 106.66% increase, respectively. The combination of 20 mg/L Fe3O4 with a 6 mm particle size of Arachis hypogea shells produced the highest cumulative biogas yield of 130.85 mL/gVSadded and a cumulative methane yield of 100.86 mL/gVSadded. This study shows that 20 mg/L of Fe3O4 additive, combined with the particle size pretreatment, improved the biogas and methane yields of Arachis hypogea shells. This result can be replicated on the industrial scale to improve the energy recovery from Arachis hypogea shells.
“…), activated sludge, waste from the food industry, landfill gas, stillage from ethanol production, etc. ( Cesaro and Belgiorno, 2015 ; Ogunkunle et al, 2019 ). Biomass is the fourth largest global primary energy source contributing about 14%, and it can be as higher as 35% in developing countries ( Khanal et al, 2019 ).…”
A smart energy recovery process can achieve maximum energy recovery from organic wastes. Pretreatment of feedstock is essential to biogas and methane yields during the anaerobic digestion process. This work combined particle size reduction with Fe3O4 nanoparticles to investigate their influence on biogas and methane yields from anaerobic digestion of Arachis hypogea shells. Twenty milligrams per litre of Fe3O4 nanoparticles was implemented with 2, 4, 6 and 8 mm particle sizes and a single treatment of Fe3O4 for 35 days. The treatments were compared with each other and were discovered to significantly ( p < 0.05) enhance biogas yield by 37.40%, 50.10%, 54.40%, 51.40% and 35.50% compared with control, respectively. Specific biogas yield recorded was 966.2, 1406, 1552.7, 1317.4, 766.2 and 413 mL g−1 volatile solid. This study showed the combination of Fe3O4 with 6 mm particle size of Arachis hypogea shells produced the optimum biogas and methane yields. The addition of Fe3O4 to particle sizes below 6 mm resulted in over-accumulation of volatile fatty acids and lowered the gas yield. This can be applied on an industrial scale.
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