The trimerization, 3A(g) --> A3(g,l) is carried out isothermally and without pressure drop in a PFR at 298 K and 2 atm. As the concentration of A3 increases down the reactor and A3 begins to condense....


The trimerization, 3A(g) --> A3(g,l)<br>is carried out isothermally and<br>without pressure drop in a PFR at<br>298 K and 2 atm. As the<br>concentration of A3 increases<br>down the reactor and A3 begins to<br>condense. The vapor pressure of<br>A3 at 298 K is 0.5 atm. If an equal<br>molar mixture of A and inert, I, is<br>fed to the reactor at what<br>conversion of A will A3 begin to<br>condense?<br>A(g) --> (1/3)A3(g,l)<br>Condensation begins at y = Py/PT<br>= 0.5 atm /2 atm = 0.25<br>

Extracted text: The trimerization, 3A(g) --> A3(g,l) is carried out isothermally and without pressure drop in a PFR at 298 K and 2 atm. As the concentration of A3 increases down the reactor and A3 begins to condense. The vapor pressure of A3 at 298 K is 0.5 atm. If an equal molar mixture of A and inert, I, is fed to the reactor at what conversion of A will A3 begin to condense? A(g) --> (1/3)A3(g,l) Condensation begins at y = Py/PT = 0.5 atm /2 atm = 0.25

Jun 07, 2022
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