Suppose from kinetic mass balance I get the following differential equation of the molarity substances $A$,$B$, and $C$ in a reactor, with molar in- or outflow rate $\phi$, and rate constant $k$:
$$ \frac{\mathrm{d}}{\mathrm{d}t}[C] = k[A]^2[B]^3 + \phi{C_{\mathrm{in}}} - \phi{C_{\mathrm{out}}} $$
Where the dimensions convert to:
$$ [\pu{mol L-1 s-1}] = [\pu{s-1}] [\pu{mol5 L-5}] + [\pu{mol s-1}] - [\pu{mol s-1}] $$
Which can be simplified by adding the flow rate terms to:
$$ [\pu{mol L-1 s-1}] = [\pu{s-1}] [\pu{mol5 L-5}] \pm [\pu{mol s-1}] $$
By cancelling similar terms mole,seconds on both sides to:
$$[\pu{L-1}] = [\pu{mol4 L-5}] \pm 1$$
This seems that something is off about the rate constant, but also that there is no $\pu{L-1}$ term in the molar flow rate.
I don't expect exact answers to this, but could someone point me the right way, or send some clear explanation on either reaction rate constants or on kinetic mass balances? It seems I cannot find clear explanations, not even in textbooks.
$\ce{H2SO4}$
or$\ce{a A <=> p P}$
or$\pu{6.022E23 mol-1}$
to get $\ce{H2SO4}$ or $\ce{a A <=> p P}$ or $\pu{6.022E23 mol-1}$ (all eventually with double dollars in the display mode like $$\ce{H2SO4}$$. // E.g. typographic rules say unit symbols are never in italic. $\endgroup$