Table 5: Exergy associated with the exchange of work and heat at the equipment level.

Equipment	Power Consumed or Delivered	Associated Exergy
Sugar Extractor (P-5/Extract) Agitation Rme =90%	W=11.07 kW
Fermentor (P-9 /Ferment) Agitation Rme =90% Cooling	W=1.20 kW Q =11.96 kW (-)
Pumps (P-10/PM-1) Rme=70% (P-10/PM-2) Rme=70% (P-10/PM-3) Rme=70%	W=0.03 kW W=0.03 kW W= 0.003 kW
Evaporator (P-11/HXF)Rth =90%	Q=63.63 kW
Condensation (P-12/HX-2) Rth =90%	Q=3.38 kW (-)
Distillation (dist-1) Condenser Boiler	Qc=1058.22 kW (-) Qb=1094.59 kW
Distillation (dist-2) Condenser Boiler	Qc=119.90 kW (-) Qb=120.78 kW
Distillation (dist-3) Condenser Boiler	Qc=226.07 kW (-) Qb=249.30 kW