We will produce $47,000$ tons of $99\mathrm{.}5\%$ purity Phthalic Anhydride. I want you to calculate the relative volatility using Antoine coefficients and perform a mass balance calculation from bottom to top. The operating temperature for distillation $2$ is $145$ degrees Celsius, for distillation $1$ it is $150$ degrees Celsius, and both operate at $1$ ATM pressure. The reactor operates at $360$ degrees Celsius and $3$ ATM pressure. We assume that the column efficiencies are $100\%.$ We will produce $47,000$ tons of $99\mathrm{.}5\%$ purity Phthalic Anhydride. I want you to calculate the relative volatility using Antoine coefficients and perform a mass balance calculation from bottom to top. The operating temperature for distillation $2$ is $145$ degrees Celsius, for distillation $1$ it is $150$ degrees Celsius, and both operate at $1$ ATM pressure. The reactor operates at $360$ degrees Celsius and $3$ ATM pressure. We assume that the column efficiencies are $100\%.$ And we are assuming that o$-$xylene is entering the system at a rate of $100$ kmol$/$hour$.$ Based on this information, what are the mass balances along with the mole fractions?distillation $1$ fed total of $7904\mathrm{.}68$ kg$/$hour$,$ that is$,$ what comes out of the flash separator, install flash separator and reactor mass balance accordingly