Initially, a feed stream containing 0.1mol/L of pure A is fed into a CSTR at a rate of 100L/hr. The CSTR is followed by a series-connected PFR. If the volume of the CSTR is 2400L and the PFR is 1240L, calculate the interconversion (XA1) and output conversion rates (XA2) that can be achieved with the existing reactor system. The rate expression for the reaction is unknown. The graph containing the conversion rates (XA) determined under the operating conditions of the reactor system and the change of the inverses of the reaction rates [rA1( L.hr) /mol] is given below