Abstract
Light olefins such as ethylene and propylene are high value-added gases usually derived from petroleum refining. The methanol to olefins (MTO) process offers an attractive alternative route to produce olefins, as methanol can be prepared from a relatively cheap and widely available source of energy, i.e., coal or natural gas. In the present work, a comprehensive single particle model was developed to characterize detailed chemical and physical phenomena occurring within a SAPO-34 catalyst particle during the MTO process. This model allows prediction of the species mass fraction, temperature, reaction rate, and pressure distributions within the particle as a function of particle diameter, operating temperature, mean intraparticle pore diameter, and thermal conductivity. A thorough parametric study based on the validated model demonstrated that intraparticle phenomena have a great impact on the MTO process and thus cannot be neglected in MTO process modeling, especially for the cases where fast or strong exothermal reactions occurred in large catalytic particles.
Published Version
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