Article ID Journal Published Year Pages File Type
6630212 Fuel 2018 8 Pages PDF
Abstract
A lumped kinetic model for methanol to aromatics (MTA) process was investigated using modified ZSM-5 industrialized catalyst. The deactivation kinetic behavior of MTA was studied by developing a 5-lump kinetic model to describe the product distributions. The feedstock and products are divided into five lumps by simplifying reaction network, including oxygenates (methanol and dimethyl ether), C1 (CO, CO2, CH4 and H2), aliphatic hydrocarbons, light aromatics (C6-C8) and heavy aromatics (C9+). The catalytic activity was reflected by activity coefficient a. The deactivation model kinetic parameters were estimated using simplex and nonlinear least squares methods. This model can be used to predict key products and their compositions of MTA industrial process.
Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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