Q:$4$

For the isothermal, isobaric gas$-$phase pyrolysis

$C2H6$longrightarrowC$2H4+H2$

pure ethane enters a flow reactor at $6$atm and $1100K.$ Set up a stoichiometric table and then write $-rA=f(x).$ How would your equation for the concentration and reaction rate, i$.$e$.,-rA=f(x),$ change if the reaction were to be carried out in a constant$-$volume batch reactor?