The enthalpy for a mixture of H2SO4(1) and Water (2) at 313.15 K as a function of mass fraction is given by equation below where H is in units of kJ/mole and S is in units of J/mol K. (Careful of units) We are mixing a stream of 50 kg H2SO4 at 313.15 K with a stream of 100 kg water at 313.15 K. What is the enthalpy change on mixing for this mixture. If we desired that the outlet is 313.15 K, how much energy must be removed/added to the mixing tank to ensure that temperature remains constant. Determine the partial molar excess enthalpy for component 1 at infinite dilution. Determine gibbs free energy change on mixing for this process. Demonstrate if this system is not possible, reversible, irreversible?