(a) Carbon emissions (%) as a function of temperature for the integrated and control systems. (b) Output mass of biochar (g) at various temperatures for the integrated and control groups. (c) Output mass of biogas (g) across the temperature range for both systems. (d) Output mass of liquid effluent (g) for the integrated and control systems.

<p>(a) Carbon emissions (%) as a function of temperature for the integrated and control systems. (b) Output mass of biochar (g) at various temperatures for the integrated and control groups. (c) Output mass of biogas (g) across the temperature range for both systems. (d) Output mass of liquid...

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محفوظ في:

التفاصيل البيبلوغرافية
المؤلف الرئيسي:	Ning Zuo (17295415) (author)
مؤلفون آخرون:	JinChao He (21253189) (author), XueMei Tan (21253192) (author)
منشور في:	2025
الموضوعات:	Biochemistry Ecology Inorganic Chemistry Environmental Sciences not elsewhere classified Biological Sciences not elsewhere classified Chemical Sciences not elsewhere classified r version 4 methanosarcina barkeri </ methanosaeta concilii </ impregnating commercial alumina 800 ° c wastewater could provide 400 ° c mass balance showed div >< p digestion </ p 500 ml sample 500 ml fixed maximum methane yield significantly higher across cobalt nitrate solution anaerobic digestion stage enhanced biogas yield experimental group decreased biogas production kinetics biogas energy derived methanogenic archaea co gompertz model increased catalysed pyrolysis integrated al₂o₃ biochar showed experimental group biogas production co₂ yield wastewater algae pyrolysis stage modified gompertz methanogenic co methane generation catalysed pyrolysis anaerobic fermentation al₂o₃ catalyst activation energy 400 m² control group improve biogas biogas increased 71 ml 525 ml 300 ml 250 ml 20 ml 05 ml 026 ml volatile matter thermogravimetric analysis thermal degradation temperature increased sustainable pathway surface area statistical analyses scenedesmus obliquus results demonstrated research investigates renewable future rate constant multiple locations modelled using microbial cultures chemical mechanisms chemical details char yields carbon source calorific value bed reactor ash content arrhenius equations 966 mj 552 mj 145 kj 125 kj
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