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 |
|
||
○ Outlet Port |
<none> |
Any Output Port |
○ Is Scaleable ? |
Yes |
Yes/No |
○ Consider Solids ? |
No |
Yes/No |
● Is Solid? |
No |
Yes/No |
○ Is Particulate Solid? |
No |
Yes/No |
○ Split % (or Retained %) |
0.0 |
0-100 |
○ Amount (kg) |
0.0 |
Positive |
◙ Total Solids in Output Stream (or Total Solids in Final Contents) (%) |
15.0 |
(0,100) |
◙ Particulate Solids in Output Stream (or Particulate Solids in Final Contents) (%) |
15.0 |
(0,100) |
○ Setup Time (min) |
15.0 |
Positive |
◙ Process Time (min) |
0.0 |
Positive |
◙ Mass Flowrate (kg/h) |
600.0 |
Positive |
◙ Vol. Flowrate (L/h) |
600.0 |
Positive |
○ Ignore Labor? |
Yes |
Yes/No |
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 Batch Component Splitting: Modeling Calculations.
•Outlet Port...
Select one of the available output streams for this operation as split stream. Note that multiple split operations can use the same split stream. In such a case, if you visit the dialog of that stream, you will see the sum of all materials transferred using that stream.
•Material Balance Options
Two options are available for specifying the component mass balances: you can either set the component splits from the selected component source to the output stream or the retained components of the selected source in the final contents. As component source, you may choose among three different options (total contents, liquid phase or vapor phase).
If you select the option to set the component splits to the output stream, then for each component you must specify either the split percentage or split amount from the selected component source to the output stream. If you select the option to set the retained components in the final contents, then for each component you must specify either the retained percentage or retained amount of the selected component source in the final contents. Based on the specified component data, the program will do the component mass balances to determine the component amounts that must be split to the output stream and the component amounts that must be retained in the final contents.
If you select total contents or liquid phase as component source, then you can also check the option to consider solids. If that option is checked, then the components table is used to specify component splitting/retention data only for particulate solid components (i.e., undissolved solids, suspended or precipitated). Only pure components that are set as solid through the Pure Component Properties dialog can be set as particulate solids in the components table. In addition to setting one or more solid components as particulate solids and specifying the splitting (or retention) data for those components, you must also specify either the total (particulate and dissolved) or particulate solids percentage of the output stream (or final contents). Based on this information, the program will calculate the component splitting/retention data for all other components besides particulate solids (i.e., dissolved solids, liquids and gases).
•Duration options...
You can set the process time (component splitting time), or have the process time calculated based on either on the volumetric or mass flowrate during transfer, or match the duration of this operation to the duration of another operation by introducing a master-slave relationship between the two operations. If you introduce a master-slave relationship, the program will match the setup time, the process time and the turnaround time of this operation (the ‘slave’) with the corresponding times of the reference operation (the ‘master’ operation). For more details on how to setup a master-slave relationship, see The Scheduling Tab.