CHE 303 (Winter 2000)
4) Determine the exit conversion in the available 500 ft3 reactor if the DBP flow rate is 40 lbmol/hr (1 ft3 = 7.48 gal.) X = 0.691. 5) If the MBP feed rate is 60 lbmol/hr and the exit conversion in the CSTR is 0.4, what conversion would be achieved if a second 500 ft3 CSTR were placed in series with the first CSTR? X … ................
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