Renewable Energy Integration: Economic Assessment of Solar Energy to Produce Biodiesel at Supercritical Conditions

Table 2

Operating conditions and mass compositions of simulation streams.

Stream	WVO	Methanol	6	B-diesel	MET-REC	11
Mass flow (kg/h)	100	39.59	139.5	109.64	17.09	12.86
T (°C)	25	25	350	95	75.5	178.4
P (bar)	1.01	1.01	100	1.01	1.01	1.01
Triolein	0.72	0	0.010	0.000	0.000	0.112
Trilinolein	0.18	0	0.003	0.000	0.001	0.027
Methanol	0	1	0.138	0.017	0.987	0.042
Oleic acid	0.06	0	0.001	0.001	0.000	0.000
Linoleic acid	0.03	0	0.000	0.001	0.000	0.000
Linolenic acid	0.01	0	0.000	0.000	0.000	0.000
M-oleate	0	0	0.552	0.703	0.000	0.000
M-linoleate	0	0	0.149	0.190	0.000	0.000
M-linolenate	0	0	0.007	0.009	0.000	0.000
G-M-E	0	0	0.096	0.076	0.000	0.396
H2O	0	0	0.043	0.003	0.012	0.423