2021
DOI: 10.1016/j.energy.2021.121028
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Comparative analysis of different CHP systems using biogas for the cassava starch plants

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Cited by 22 publications
(8 citation statements)
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“…For the case of methane and considering the average scenario, the CH 4 flow rate of 91.04 m 3 /minute would involve a total power generation capacity of 5925.32 kW and net energy production of 35,018 GWh/year. This energy potential is consistent with reported projects that used similar technologies (Coskuner et al, 2020; Yin et al, 2021). By contrast, the waste incineration would produce 537.71 GWh/year.…”
Section: Resultssupporting
confidence: 91%
“…For the case of methane and considering the average scenario, the CH 4 flow rate of 91.04 m 3 /minute would involve a total power generation capacity of 5925.32 kW and net energy production of 35,018 GWh/year. This energy potential is consistent with reported projects that used similar technologies (Coskuner et al, 2020; Yin et al, 2021). By contrast, the waste incineration would produce 537.71 GWh/year.…”
Section: Resultssupporting
confidence: 91%
“…The CHP unit for biogas utilization provides the most carbon offset (226.0 kgCO 2 -eq/t). The energy utilization efficiency in the CHP unit of biogas is generally above 60%, earning considerable heating and electricity credits. It is generally believed that land use of fiber digestate and liquid digestate earns the best environmental benefits, and its contribution to carbon reduction is comparable to that of biogas utilization .…”
Section: Resultsmentioning
confidence: 99%
“…The amount of biogas is about 100 m 3 per tonne of FW, where the methane content is 63% (v/v) . Biogas generated from the fermentation process is combusted in a CHP unit, with a power efficiency of 33% and heat efficiency of 30% . After the digestate is dewatered, the liquid digestate is treated by an “Anaerobic Sludge Blanket Reactor + Membrane Bioreactor + Nanofiltration + Reverse Osmosis” (UASB + MBR + NF + RO) process before being discharged into surface water, consuming 30 kWh per tonne of liquid .…”
Section: Methodsmentioning
confidence: 99%
“…Each pretreatment has merits and demerits and should be chosen carefully to improve methane yield and avoid downstream processing (Periyasamy et al 2022 ). After the anaerobic digestion process, biogas can be combusted directly as a cooking fuel (Rajendran et al 2013 ), combusted in a combined heat and power unit for heat and power generation (Yin et al 2021 ), combusted in a boiler for heat generation (Kim et al 2020 ), reformed for hydrogen production (Guerrero et al 2020 ), or upgraded into pure biomethane (Ardolino et al 2021 ). Another important process after anaerobic digestion is managing the digestate generated after biogas production (Alengebawy et al 2022b ).…”
Section: Bioenergymentioning
confidence: 99%