Consider a cylindrical batch reactor that has one end fitted with a frictionless piston attached to a spring. The gas phase reaction is taking place in this type of reactor.

$A+B$

$6C$

The rate law for reaction is second order in A and first order in $B$ and overall third order

Write the rate law solely as a function of conversion, numerically evaluating all possible symbols.

What is the conversion and rate of reaction when $V=0\mathrm{.}3f{t}^3$

Additional information:

Equal moles of A and $B$ are present at $t=0$

Initial volume: $0\mathrm{.}19f{t}^3?$

Value of $k$:$2(f\frac{t^3}{\text{I}}$bmol${)}^2*s^{-1}$

The relationship between the volume of the reactor and pressure within the reactor is:

$P=12V,P_0=12V_0$

$($Vin $f{t}^3.P$ in atm$)$

Temperature of system $($considered constant$)$: $600R$

Gas constant: $0\mathrm{.}73f{t}^3.at\frac{m}{\text{I}}b$ mol $*R$

Question $2$:

$A+2$BlongrightarrowC

An elementary liquid phase reaction needs to be carried out in a CSTR reactor with a volume $5m^3$ and conversion desired is $70\%.$the molar feed is $30\%$A and $70\%B$ at a pressure $202$kpa and $333K$

Construct a complete stoichiometric table in terms of concentrations

What is the rate of reaction of $A$

Calculate $k$&$E$ and then specify the type of reaction energy

Additional information:

Total feed: $10$mol$\frac{e}{s}.$

Gas constant: $8\mathrm{.}314k\frac{J}{m}ol*K$

Frequency factor: $0\mathrm{.}00717\frac{m^3}{m}ol.$s