The following table shows a brief description of the variables appearing in this tab. The table also displays their default values and their generally acceptable range:
Variable |
Default Value |
Range |
|
||
○ % Absorption |
0.0 |
0 – 100 |
○ Perform Reaction Calculations in the Liquid Outlet Stream |
No |
Yes/No |
◙ Top Stream Temp. (oC) |
100.0 |
Positive |
◙ Bottom Stream Temp. (oC) |
40.0 |
Positive |
○ Design Component |
<none> |
Any Pure Component |
○ Diffusivity in Gas Phase (x 103) (cm2/s) |
150.0 |
Positive |
○ Diffusivity in Liquid Phase (x 106) (cm2/s) |
15.0 |
Positive |
○ Auto-Adjust Liquid Stream |
No |
Yes/No |
● Minimum (L/G) Ratio |
0.0 |
Positive |
◙ Operating Factor |
1.1 |
>1.0 |
● HTU (m) |
0.0 |
Positive |
● NTU |
0.0 |
Positive |
○ Liquid Surface Tension (dyn/cm) |
30.0 |
Positive |
○ Liquid Phase Viscosity (cP) |
1.0 |
Positive |
○ Gaseous Phase Viscosity (cP) |
0.018 |
Positive |
● Pressure Drop (Pa) |
0.0 |
Positive |
○ Pressure Drop/Length (Pa/m) |
400 |
Positive |
Symbol Key: ○ User-specified value (always input); ● Calculated value (always output); ◙ Sometimes input, sometimes output
The following list describes the available specification choices in this tab; for more details on how these are implemented, see Absorption: Modeling Calculations.
•Perform Reaction Calculations in the Liquid Outlet Stream...
Check this option if there are reactions taking place. This will make the ‘Stoichiometric Reactions’ tab appear on the operation’s dialog. Note that reactions are done after the separation calculations.
•Equilibrium Line Specification...
The user has the option to specify the equilibrium line, either in the form of Henry’s law or in the form of a quadratic polynomial.