P100 - Chemical Engineering Process Design ... - Discovery Press
P100 - Chemical Engineering Process Design ... - Discovery Press
P100 - Chemical Engineering Process Design ... - Discovery Press
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EngrI 1120 - Introduction to <strong>Chemical</strong> <strong>Engineering</strong><br />
<strong>Design</strong> Competition - Annual Investment and Operation Plan - 2012<br />
Company<br />
Year<br />
Equipment Purchases:<br />
Reactor: Type: (1 or 2)<br />
Size: (capacity in mol/day or cost in $)<br />
Liquid-Solid Separator: Type: (1 or 2)<br />
Size: (capacity in mol/day or cost in $)<br />
(optional) Gas-Liquid Separator:<br />
Size: (capacity in mol/day or cost in $)<br />
Operating Parameters:<br />
Reactant A+I Purity: Grade: (1 or 2)<br />
Reactant A+I flow rate:<br />
(mol of A+I per day, or write MAXIMUM*)<br />
Fraction of Liquid-Solid Separator bottoms to purge:<br />
Fraction of Liquid-Solid Separator bottoms to bypass Gas-Liquid Separator**:<br />
Company Representative:<br />
*You need not calculate the exact flow rate of A+I. If you write “MAXIMUM,” we will process as much<br />
A+I as possible, limited by your equipment capacity or your cash remaining after buying equipment.<br />
** The sum of fraction purged plus fraction bypassed must be less than or equal to 1. If you do not<br />
purchase a gas-liquid separator (and therefore sell no by-product X), you must set the sum of fraction<br />
purged plus fraction bypassed to exactly 1.
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