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2C2H6+O22C2H4O An unde-ifed compiting reaction is the combusticn of etholine. C2H4=3O2+2CO2+3H2O calcidule ehe collowirs quabivin Ethylene oxide is produced by the catalytic oxidation of ethylene: 2C2H4+O22C2H4O An undesired competing reaction is the combustion of ethylene: C2H4+3O2+2CO2+2H2O The feed to the reactor (not the fresh feed to the process) consists of 3.00 moles of ethylene permole of oxygen. Thesingle-pass conversion of ethylene to either ethylene oxide or carbon dioxide is 30.0%, and for every 100.0 moles of ethylene consumed in the reactor, 80.0 moles of ethylene oxide emerges in the reactor products. A multiple-unit process is used to separate the products; ethylene and oxygen are recycled to the reacton ethylene oxide is sold as a product, and carbon dioxide and water are discarded. Assume a quantity (100.0mol/h) of the reactor feed stream as a basis of calculation, draw and label the flowchart, perform a degreeof-freedom analysis, and write the equations you would use to calculate (i) the molar flow rates of ethylene and oxygen in the fresh feed, (ii) the production rate of ethylene oxide, and (iii) the overall conversion of ethyiene. a. Calculate the following quantities. Molar flow rate of ethylene in the fresh feed:- Molar flow rate of oxygen in the fresh feed: molhi2H4 Production rate of ethylene cxide: molhil2 Overall conversion of ethylene: b. Calculate the molar flow rates of ethylene and axyzen in the fresh feed needed to produce 1 ton per hour of ethviene owidel Molar flowrate of ethylene: lbmol/hC2H4 Molar now rate of axysen- lbmolhO2 2C2H6+O22C2H4O An unde-ifed compiting reaction is the combusticn of etholine. C2H4=3O2+2CO2+3H2O calcidule ehe collowirs quabivin Ethylene oxide is produced by the catalytic oxidation of ethylene: 2C2H4+O22C2H4O An undesired competing reaction is the combustion of ethylene: C2H4+3O2+2CO2+2H2O The feed to the reactor (not the fresh feed to the process) consists of 3.00 moles of ethylene permole of oxygen. Thesingle-pass conversion of ethylene to either ethylene oxide or carbon dioxide is 30.0%, and for every 100.0 moles of ethylene consumed in the reactor, 80.0 moles of ethylene oxide emerges in the reactor products. A multiple-unit process is used to separate the products; ethylene and oxygen are recycled to the reacton ethylene oxide is sold as a product, and carbon dioxide and water are discarded. Assume a quantity (100.0mol/h) of the reactor feed stream as a basis of calculation, draw and label the flowchart, perform a degreeof-freedom analysis, and write the equations you would use to calculate (i) the molar flow rates of ethylene and oxygen in the fresh feed, (ii) the production rate of ethylene oxide, and (iii) the overall conversion of ethyiene. a. Calculate the following quantities. Molar flow rate of ethylene in the fresh feed:- Molar flow rate of oxygen in the fresh feed: molhi2H4 Production rate of ethylene cxide: molhil2 Overall conversion of ethylene: b. Calculate the molar flow rates of ethylene and axyzen in the fresh feed needed to produce 1 ton per hour of ethviene owidel Molar flowrate of ethylene: lbmol/hC2H4 Molar now rate of axysen- lbmolhO2