Abstract

Propene is an important synthetic industrial product predominantly formed by a methanol-to-olefins (MTO) catalytic process. Propene is known to form oligomers on zeolite catalysts, and paramters to separate it from mixtures and its diffusion properties are difficult to measure. Herein, we explored the adsorption–chemisorption behavior of propene by choosing SAPO-34 zeolites with three different degrees of acidity at various adsorption temperatures in an ultra-high-vacuum adsorption system. H-SAPO-34 zeolites were prepared by a hydrothermal method, and their structural, morphological, and acidic properties were investigated by XRD, SEM, EDX, and temperature-programmed desorption of ammonia (NH3-TPD) analysis techniques. The XRD analysis revealed the highly crystalline structure which posses cubic morphology as confirmed by SEM images. The analysis of adsorption of propene on SAPO-34 revealed that a chemical reaction (chemisorption) was observed between zeolite and propene at room temperature (RT) when the concentration of acidic sites was high (0.158 mmol/g). The reaction was negligible when the concentration of the acidic sites was low (0.1 mmol/g) at RT. However, the propene showed no reactivity with the highly acidic SAPO-34 at low temperatures, i.e., −56 °C (using octane + dry ice), −20 °C (using NaCl + ice), and 0 °C (using ice + water). In general, low-temperature conditions were found to be helpful in inhibiting the chemisorption of propene on the highly acidic H-SAPO-34 catalysts, which can facilitate propene separation and allow for reliable monitoring of kinetic parameters.

Highlights

  • SAPO-34 zeolite plays a pivotal role in the chemical industry [1]

  • Results and Discussions order to examine propene–SAPO-34 interaction, different batches of SAPO-34 zeolites In In order to examine thethe propene–SAPO-34 interaction, different batches of SAPO-34 zeolites were were prepared with different strengths of acidity by controlling zeolite alumina and silica prepared with different strengths of acidity by controlling zeolite alumina and silica components

  • We have successfully developed three H-SAPO-34 zeolites with a similar morphology but different acid properties as evidenced by the X-ray powder diffraction (XRD), FESEM, EDX, and NH3 -TPD measurements

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Summary

Introduction

One of its important applications is in a methanol-to-olefins (MTO) process [2,3,4,5]. The Chinese government has passed an agreement to scale up MTO processes in tons per year and many operational units are expected in the coming years [6]. The most desirable product generated in this process is propene. Catalysts 2019, 9, x FOR PEER REVIEW issues related to this product, including separation of propene from its mixture [7,8,9] and design of new. There are certain issues related to this product, including separation of propene from its mixture [7–.

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