This reaction is always kept below 45°C, because above that temperature di- and tri-chlorinated benzene are products. In a particular reactor that produces chlorobenzene, chlorine gas and liquid benzene are fed into a reactor by two separate streams, each at T1 = 25°C. The chlorine gas stream is fed into the reactor at m1 = 3.85 kg/s. The molar flow rate of benzene, n2, enters the reactor in a stoichiometric amount. The reaction is carried out at T2 = 35.0 °C, and 1 atm. The fractional conversion of benzene is 0.750. The product streams exit at the same temperature at which the reactor is running. The products consist of chemicals in the gas state (chlorine gas and hydrogen chloride) and chemicals in the liquid state (benzene and chlorobenzene). Assume that no benzene or chlorobenzene is in the gas phase. Find the moles of each species leaving the reactor and the rate of heat that is removed or added to keep the product at 35.0°C. The heat capacity of liquid chlorobenzene is 0.15504 kJ/(mol·K). The heat of this reaction is