6,948,30,Orientation/ MOLE BALANCE: definition of the rate of reaction, general mole balance equation, types of reactors, industrial reactors,,,,,CONVERSION & REACTOR SIZING: definition of conversion, design equations, application of design equations, reactor in series,,,,,RATE LAWS & STOICHIOMETRY 1: reaction rate constant, reaction order and rate law, elementary rate law and molecularity, reversible reactions, elementary rate laws and reactions,,,,,RATE LAWS & STOICHIOMETRY 2:
stoichiometry table (batch system, constant volume reaction system, flow system, volume change with reaction), expressing concentration in terms other than conversion.,,,,,ISOTHERMAL REACTOR DESIGN: design structure for isothermal reactors, batch operation, design of CSTRs, tubular reactor.,,,,,COLLECTION & ANALYSIS OF RATE DATA 1: batch reactor data (differential method of rate analysis, integral method).,,,,,COLLECTION & ANALYSIS OF RATE DATA 2: method of initial rates, method of half-lives, differential reactors, evaluation of laboratory reactors.,,,,,NONELEMENTARY REACTION KINETICS: Active intermediate, PSSH, chain reaction, reaction pathway.,,,,,MULTIPLE REACTIONS: definitions, parallel reactions, maximizing the desired product in series reactions.,,,,,NONELEMENTARY REACTION KINETICS: Enzymetic reaction, Michaelis-Menten equation, batch reactor calculation, inhibition of enzymetic reaction.,,,,,STEADY-STATE NONISOTHERMAL REACTOR DESIGN: rationale, energy balance.,,,,,NONISOTHERMAL CONTINUOUS-FLOW REACTORS: application to CSTR, adiabatic tubular reactor, steady-state tubular reactor with heat exchanger.,,,,,EQUILIBRIUM CONVERSION: adiabatic temperature and equilibrium conversion, optimum feed temperature.,,,,,CATALYSIS & CATALYTIC REACTORS: catalysts, steps in a catalytic reaction.,,,,,CATALYSIS & CATALYTIC REACTORS: design of reactors in gas-solid reactions, heterogeneous data analysis for reactor design.,,,,,Wrap-up and general discussion.,,,,,,,,,,,,,,,,,,,,/////3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,,,,,,,,,,,,,,,,/////3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,3,,,,,,,,,,,,,,,,,,,,/////,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,/////,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,/////,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,/////1,,,,,1,,,,,1,,,,,1,,,,,1/////,,,,,,,,,,,,,,,,,,,,,,2024-05-29 11:19:24,2024-05-29 11:19:24