ElectronicError said:
Thanks for your help. This is what I have done so far, but it is still wrong.
ln[(PPH3)t / (PPH3)o] = -kt
This is only true for n=1, and is not the correct equation for n != 1. You need to figure out the order of the reaction rate; you can't assume it is 1.
For n not 1, you have:
[tex]dA/dt = -kA^n \implies A^{-n}dA = -kdt \implies A^{1-n} - A_0^{1-n} = -k(t - t_0)[/tex]
Ptotal = PPH3 + PP4 + PH2
PPH3 = Po - PP4
PH2 = 6PP4
Ptotal = (Po - PP4) + 6PP4 + PP4
Ptotal= Po + 6PP4
PP4 = (Ptotal - Po) / 6
PPH3 = Po -PP4 = Po - [(Ptotal-Po) / 6]
Not sure I follow what you're doing here. For every 4 moles of PH3 consumed there are 7 moles of products produced, resulting in a net change of +3 moles (for every 4 moles of PH3 consumed). So the decrease in partial pressure of PH3 is 4/3 of the increase in total pressure over any interval of time.
So, for instance, during the first 40s, since the p(tot) increases by 50 torr, p(PH3) must decrease by 50*4/3 torr. Using this method, you can translate the table for p(tot) into a similar table for p(PH3).
Write down the values in this new table and plug them into the general equation for the n'th order rate law (above) to find k and n.
Note that the above rate equation only applies if n is not 1. It is actually prudent to first check if n=1 works.
PS: I just checked. It
is first order; so you can indeed use the rate equation you used in post #3, only you need to use it on the new table of numbers.