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ProcDev - Process Development
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Activated MDEA. | |
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Ammonia. | |
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Carbon monoxide. | |
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Hydrogen. | |
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Rectisol. | |
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Sasol Fischer-Tropsch process. | |
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Stretford. | |
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Sulfolin. | |
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SuperClaus | |
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And many more. |
For example, to use the generalized material balance spreadsheet
to design a simple formaldehyde plant as shown (drawing using the "flow-sheet
drawing" module of course) below:-

open up the ProcDev module to show the following view:-

Type in "balance and press "enter". You should
see the material balance record. Now tap on the spreadsheet icon and copy it to
the clipboard with Ctrl-C. You should view the following:-

Next, paste the spreadsheet into your project files as below:-

Open the spreadsheet and enter data into the "Feed
table" below:-

Up to 8 components and 3 feed streams may be entered, along with their formula,
name, molecular weight, mole fractions and total molar flow-rates. The feed
steams must be given names to be included in the material balance.
Next enter data into the Equipment Specification Table, as
below:-

This table can take up to a total of 7 unit operations, of 4 types reactors,
adders, separators and distillation columns. As many as 4 parameters must be
entered for the distillation unit, and up to 8 (dependent on the number of
components) coefficients characterizing the equipment.
Having done that, enter the connections between the flow streams
and the equipment. Up to 3 feed streams per equipment (numbered 1, 2 & 3)
and 2 output streams (numbered 6 & 7 for top and bottom respectively) for
the separator and distillation units only, as below:-

Now recalculate using by selecting the entire spreadsheet and
copying and pasting it into itself, or use the "macro" provided. (The
Psion spreadsheet algorithm is unable to cope):-

Then pan to the bottom of the spreadsheet for your stream
flows:-

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Last updated 2001-09-15 - Created using FrontPage by Jeff
Harmed |