| initial
FAME concentration (mol/m3) |
2509 |
| initial DEA concentration (mol/m3) |
2650 |
| initial nitrogen partial pressure (bar) |
1 |
| initial methanol partial pressure (bar) |
0 |
| initial volume of the gas (mL) |
900 |
| initial volume of the liquid mixture
(mL) |
100 |
|
M = total reactor volume/initial volume of liquid mixture |
10 |
| temperature (°C) |
80 |
| Parameters used
for the model |
|
Keq at 80 °C (obtained from Section 4.2) |
16.92 |
|
kf at 80 °C (m3/mol·min) (obtained
from Section 4.2) |
3.95 × 10–5
|
| γMeOH at 80 °C (obtained from Section 4.2) |
0.7 |
