Kinetic Modelling at the Basis of Process Simulation for Heterogeneous Catalytic Process Design

Abstract

Process simulation represents an important tool for plant design and optimisation, either applied to well established or to newly developed processes. Suitable thermodynamic packages should be selected in order to properly describe the behaviour of reactors and unit operations and to precisely define phase equilibria. Moreover, a detailed and representative kinetic scheme should be available to predict correctly the dependence of the process on its main variables. This review points out some models and methods for kinetic analysis specifically applied to the simulation of catalytic processes, as a basis for process design and optimisation. Attention is paid also to microkinetic modelling and to the methods based on first principles, to elucidate mechanisms and calculate thermodynamic and kinetic parameters. Different case histories support the discussion. At first, we have selected two basic examples from the industrial chemistry practice, e.g. ammonia and methanol synthesis, which may be described through a relatively simple reaction pathway. Then, a more complex reaction network is deeply discussed to define the conversion of bioethanol into syngas/hydrogen or into building blocks, such as ethylene.

ASPEN-HYSYS Simulation of AREW's Multi-Stage Adiabatic Reactor with Inter-Stage Quenching for Methanol Synthesis

“…The Langmuir-Hinshelwood-Hougen-Watson (LHHW) type integral equation, obtained from the kinetics and parameters developed by Bussche and Forment (1996), is employed by ASPEN-HYSYS to describe the methanol production kinetics (Tripodi et al 2017 ). This model accurately depicts the characteristics of both methanol production reactions.…”