CDP5-CC The ethane hydrogenolysis over a commercial nickel catalyst was studied in a stirred tank solids reactor H₂ + C₂
Posted: Wed Jun 08, 2022 9:37 am
CDP5-CC The ethane hydrogenolysis over a commercial nickel catalyst was studied in a stirred tank solids reactor H₂ + C₂H6→ 2CH4 (a) Determine the rate law parameters from the data in the table below. There are four spnning baskets, each with 10 g of catalyst. Only hydrogen and ethane are fed to the reactor at 300 °C Partial Pressure (atm) in Feed Total Molar Feed Mole Fraction CHain Rate to Reactor Ethane, Hydrogen, (g mol/h) PAO Рво Ext Stream 1.7 0.5 0.5 0.5 1.2 0.5 0.5 0.7 0.6 0.5 0.5 0.16 0.3 0.4 0.6 0.16 0.75 0.6 0.6 0.1 2.75 0.6 0.4 0.06 (b) What experimental conditions would you suggest if you were to obtain more data?