The following table shows the meaning of the variables appearing in this tab, as well as their default values and their generally acceptable range. Note that due to the manner by which the variables are used by the sizing and costing equations, the range of acceptable values may be further reduced.
Variable |
Default Value |
Range |
|
||
◙ Actual Stages |
0 |
Positive |
◙ Max Diameter |
2.0 m |
Positive |
◙ Stage Height |
0.4 m |
Positive |
◙ Column Height |
0.0 m |
Positive |
◙ Column Diameter |
0.0 m |
Positive |
● Volume |
0.0 L |
Positive |
○ Design Pressure |
1.52 bar |
Positive |
○ Is ASME Vessel? |
Yes |
Yes/No |
Symbol Key: ○ User-specified value (always input); ● Calculated value (always output); ◙ Sometimes input, sometimes output
In Calculate (Design Mode), the user specifies the Maximum Diameter and Stage Height and the system computes the Number of Units, Number of Actual Stages, Column Height, and Column Diameter. For more information on sizing of the distillation column, see Continuous Distillation (Shortcut): Modeling Calculations.
In User-Defined (Rating Mode), the user specifies the Number of Units, Number of Actual Stages, Column Height, and Column Diameter.
The equipment purchase cost is based on the diameter and the height of the column. It is supplied by the built-in model assuming as material of construction CS. Other factors that affect the cost are:
Conforming to ASME Specification; if checked, then the vessel is assumed to have been constructed according to standards published by the American Society of Mechanical Engineers (ASME) and it is assumed to withstand pressure up to 35psig. Checking this option penalizes the cost by about 20% over the base cost.
For more information on this equipment, see Distillation Column.
For information on the left-hand side variables and options, see Equipment Data Dialog: Equipment tab.