The synthesis of methanol from carbon monoxide and hydrogen [CO(g) 2H2(g)->CH3OH(g)] is carried out in a continuous vapor-phase reactor at 5.0 atm absolute. The feed contains CO and H2in stoichiometric proportion and enters the reactor at 250C and 5.00 atm at a rate of 21.1 m3/h. The product stream emerges from the reactor at 1270C. The rate of heat transfer from the reactor is 21.0 kW. Calculate the fractional conversion achieved and the volumetric flow rate (m3/h) of the product stream.