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Virginia Tech

Sensitivity of methanol-to-olefin reaction to axial gas dispersion: determination in a vibrated-bed microreactor

Abstract

dc:description.abstract

A microreactor has been developed to study the sensitivity of Methanol-To-Olefin (MTO) reaction to axial gas dispersion. It comprises a rectangular horizontal duct, 12.7 mm in height, 25.4 mm in width, variable in length, charged with a 1-mm-deep layer of HZSM-5 catalyst. The microreactor is constructed of aluminum alloy and heated with cartridge heaters. A glass reference duct with the same catalyst loading is mounted directly above the microreactor to provide visual check of the coherent-expanded vibration state achieved by vibrating the setup at 24 hertz and 4.3-mm vertical displacement. In this. state, catalyst powder expands to full duct height during a portion of each vibration cycle, with intense vertical mixing of powder and little horizontal. Axial gas dispersion coefficient varies linearly with superficial gas velocity, and axial Peclet Number (Pe<sub>ax</sub>) can be studied over a wide range of values simply by varying duct length while holding weight hourly space velocity constant. Conducting the MTO reaction in microreactors of 7.62-, 15.24-, and 22.86-cm length (Pe<sub>ax</sub> = ca. 2, 9, and 19 respectively) revealed the reaction to be sensitive to axial gas mixing. Trend in light olefin yield versus Pe<sub>ax</sub> agrees with earlier turbulent fluid-bed data. Loss in olefins with increase in axial gas dispersion (decrease in Pe<sub>ax</sub>) suggests that a circulating fluid bed may be the preferred reactor for this reaction. Researchers can use the microreactor to determine, quickly and inexpensively, how reaction outcomes vary with axial gas dispersion. The microreactor could help R&D managers to avoid expense of a fluid bed R&D effort where an economically significant outcome of a reaction is acutely sensitive to axial gas dispersion, and where a fixed bed is an acceptable alternative.

Degree

thesis:*
Name thesis:degree_name
Ph. D.
Level thesis:degree_level
doctoral
Discipline thesis:degree_discipline
Chemical Engineering
Department dc:contributor.department
Chemical Engineering
Grantor dc:publisher
Virginia Tech
Year dc:date.issued
1995

Author and committee

dc:creator, dc:contributor.*
Author dc:creator
  • Tshabalala, Samuel Nhlanganiso
Chair dc:contributor.committeechair
  • Squires, Arthur M.
Committee members dc:contributor.committeemember
  • Conger, William L.
  • McNair, Harold M.
  • Oyama, Ted S.
  • Benge, G. Gregory
  • Thomas, Benku

Rights

dc:rights
Statement dc:rights
  • In Copyright
Language dc:language.iso
en

Identifiers

dc:identifier.*
Dc Identifier Other
etd-10192006-115614
OAI identifier oai:identifier
oai:vtechworks.lib.vt.edu:10919/40005

Chain of custody

source
Harvested from
Virginia Tech
Base URL
vtechworks.lib.vt.edu/oai/request
Last updated
2026-07-22
Source record
OAI-PMH GetRecord
related terms
citation

Tshabalala, Samuel Nhlanganiso. Sensitivity of methanol-to-olefin reaction to axial gas dispersion: determination in a vibrated-bed microreactor. doctoral thesis, Virginia Tech, 1995. http://hdl.handle.net/10919/40005