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Esercitazione 7 Soluzione

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time [s] sigma [‐]r a t e riduzione 00 . 8 29.4 0.7 71.1 0.6 rate ossidazione 137.8 0.5 227.7 0.4 dati kox [s^‐1*atm^‐0.5] 0.0091 pNO [ppm] 500 0.0005 yO2 [%mol/mol] 10 p [atm] 1 T [°C] 200 R red k P NO s‐oh ^m k' 0.006766292 k 13.53258432 m 2.033773142 s‐oh 0.477377761 s ‐r 0.522622 Es 7 ‐ chimica industriale 𝑟௥௜ௗൌ𝑘௥௜ௗ𝑝ேை𝜎ௌିைு ௠ 𝑟௥௜ௗൌ𝑘௢௫𝑝ைమ ଴.ହ𝜎ௌ CINETICA POWER LAW r*1e‐2 [mol/m3/h] C A [mol/m3] CB [mol/m3] 0.2095 972.9 9729.2 1.294 1945.8 9728.7 3.754 2918.7 9729.5 7.993 3891.6 9728.3 3.756 2921.4 4864.5 3.753 2919.3 14593.4 calcoli reattore tabella portate [kmol/h] inlet A 1 B 5 E 0 H2O 0 V 0.5 m3/h conversione target 0.32 r = k Ca ^ alfa Ca in kmol/m3 T [K] 373.15 ka l f a 22.51774 2.626819 V CSTR 6.33639894 m3 V PFR 3.87625097 m3 Es 7 ‐ chimica industriale

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