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5a Conversion rate as a function of the degree of conversion
Isothermal reactor calculations
12 other sections not shown
adiabatic assumed autothermal average residence batch reactor cascade of tank catalyst chemical reaction chlorination complex reactions component concentration consecutive reactions constant continuous tank reactor continuously operated conversion rate cooling costs cross-flow reactor curve degree of conversion density desired product diffusion equal equation equilibrium reaction ethyl acetate example exothermic exothermic reaction fluidized bed function given heat effect heat exchange heat of reaction heat transfer ideal tubular reactor Illustration increase influence inlet interface isothermal liquid longitudinal dispersion material balance maximum yield mixed tank reactor molar obtained optimization optimum temperature order reaction outlet packed bed parallel reactions parameters particle possible production rate ratio reac reactant reaction mixture reaction path reaction phase reaction temperature reaction volume reactor system reactor types relative degree residence time distribution respect result second order reaction shown in Fig solution surface tion tube unit mass variable