Exergy analysis of a lignocellulosic-based biorefinery annexed to a sugarcane mill for simultaneous lactic acid and electricity production

• Published in: Energy (Oxford) Vol. 149; pp. 623 - 638
• Main Authors: Aghbashlo, Mortaza, Mandegari, Mohsen, Tabatabaei, Meisam, Farzad, Somayeh, Mojarab Soufiyan, Mohamad, Görgens, Johann F.
• Format: Journal Article
• Language: English
• Published: Oxford Elsevier Ltd 15.04.2018; Elsevier BV
• Subjects: Acid production; Bagasse; Bagasse and trash; Biorefineries; Destruction; Electric power generation; Electricity; Electricity generation; Exergy; Exergy analysis; Lactic acid; Lignocellulose; Mathematical models; Organic chemistry; Parameters; Polylactic acid; Refineries; Refining; Second generation biorefinery; Steam electric power generation; Steam generation; Sugar; Sugarcane; Thermodynamics; Second generation biorefinery; Lactic acid; Electricity; Exergy analysis; Bagasse and trash
• ISSN: 0360-5442; 1873-6785
• DOI: 10.1016/j.energy.2018.02.063

This study was aimed at exergetically analyzing a lignocellulosic biorefinery annexed to a sugar mill for simultaneous lactic acid and electricity production using sugarcane bagasse and brown leaves as feedstock. The main goal was to reveal the reasons and sources of thermodynamic inefficiencies associated with the biorefinery under investigation. After presenting the exergy balance equations for all the subunits of the biorefinery, their exergetic performance parameters were computed and consequently exergetic performance parameters were measured for the whole system. The exergetic values of the net electricity and steam were found to be 20.66 MW and 50.41 MW, respectively, while the chemical exergy content of the produced lactic acid was determined at 112.84 MW. The overall exergy destruction of the system stood at 207.69 MW. The contribution of the steam generation, as the main subunit wasting exergy, to the overall exergy destruction of the system was found to be 63.31%. Furthermore, lactic acid production subunit stood in the next rank in terms of exergy destruction, contributing 16.30% of the overall exergy destruction of the biorefinery. The universal and functional exergetic efficiencies of the system were determined as 52.71% and 44.73%, respectively, while the normalized exergy destruction was calculated as 1.13. •Exergy analysis was applied to a lignocellulosic biorefinery annexed to a sugar mill.•The steam generation subunit delivered the highest exergy destruction rate.•Lactic acid production subunit stood in the second rank in terms of exergy destruction.•The functional exergetic efficiency of the system was determined as 44.73%.•The normalized exergy destruction of the plant was found to be 1.13.