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Effect of steam during catalytic cracking of n-hexane using P-ZSM-5 catalyst

Paper ID Volume ID Publish Year Pages File Format Full-Text
49343 46740 2015 5 PDF Available
Title
Effect of steam during catalytic cracking of n-hexane using P-ZSM-5 catalyst
Abstract

•The catalyst deactivated because of both dealumination and coke deposition.•The deactivation reasons were influenced by the steam to n-hexane ratio.•The amount of coke deposition increased with decreasing steam to n-hexane ratio.•The excess steam deactivated the ZSM-5 catalysts irreversibly via dealumination.

Phosphorus-modified ZSM-5 (P-ZSM-5) catalyst was active for steam cracking of n-hexane to produce propylene and ethylene; however, the P-ZSM-5 catalyst deactivated because of both dealumination and coke deposition, which were strongly influenced by the steam to n-hexane ratio in the reactant flow. The amount of coke deposition increased with decreasing the steam to n-hexane ratio from the TG-DTA measurement. The steam could reduce the reactions of the light olefins to BTX and coke and enhance the yield of the light olefins; however, the excess steam deactivated the ZSM-5 catalysts irreversibly via dealumination.

Graphical abstractThe P-ZSM-5 catalyst deactivated because of both dealumination and coke deposition, which were strongly influenced by the steam to n-hexane ratio in the reactant flow.Figure optionsDownload full-size imageDownload as PowerPoint slide

Keywords
Phosphorus-modified ZSM-5; n-Hexane steam cracking; Steam–hexane ratio; Propylene
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Effect of steam during catalytic cracking of n-hexane using P-ZSM-5 catalyst
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Publisher
Database: Elsevier - ScienceDirect
Journal: Catalysis Communications - Volume 69, 5 September 2015, Pages 20–24
Authors
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Subjects
Physical Sciences and Engineering Chemical Engineering Catalysis
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Price was $35.95
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