Cold model of a vibrated-bed microreactor capable of varying Peclet number at fixed weight hourly space velocity providing a tool for simulating an important feature of the reaction kinetic scene in large catalytic fluid beds
A cold-flow model of a vibrated-bed microreactor has been designed and tested with capability for varying the level of gas dispersion (characterized by axial Peclet number) at a fixed weight hourly space velocity (WHSV). A tool has thus been provided whereby an important feature (viz., gas disper...
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ndltd-VTETD-oai-vtechworks.lib.vt.edu-10919-390832021-04-21T05:26:25Z Cold model of a vibrated-bed microreactor capable of varying Peclet number at fixed weight hourly space velocity providing a tool for simulating an important feature of the reaction kinetic scene in large catalytic fluid beds Benge, G. Gregory Chemical Engineering Squires, Arthur M. Avidan, Amos A. Beyer, Gerhard H. Conger, William L. Johnson, Lee W. Thomas, Benku LD5655.V856 1992.B397 Fluidized reactors -- Design A cold-flow model of a vibrated-bed microreactor has been designed and tested with capability for varying the level of gas dispersion (characterized by axial Peclet number) at a fixed weight hourly space velocity (WHSV). A tool has thus been provided whereby an important feature (viz., gas dispersion) of the reaction kinetic scene in large catalytic fluid beds can be simulated on a microscale, using approximately 5 grams of catalyst. Realization of a hot design of the microreactor (a task for another student) should permit the industrial chemist or chemical engineer, working at laboratory bench scale, quickly and inexpensively, to determine the sensitivity of a cataly1ic reaction to fluid-bed gas dispersion. The new microreactor exploits the coherent-expanded (C-E) vibrated-bed state, and is perhaps the first technical use of this state. The C-E state is achieved by subjecting a shallow layer of a fine powder to vertical sinusoidal vibration. The microreactor comprises a rectangular horizontal duct, 12.7 mm in height, 25.4 mm in width, variable in length, and with nonporous floor and walls. The microreactor is charged with a powder, such as fluid cataly1ic cracking (FCC) catalyst, at a compacted depth of I mm, and is vibrated at ~15 Hertz and amplitude of ~3 mm. Under influence of this vibration, the powder expands, displaying the C-E state. Between a phase angle of ~50° and an angle of ~150°, the powder assumes a depth of ~4 mm (i.e., expanded 4-fold from its compacted depth). Later, in each vibration cycle, the powder expands further. At ~300° phase angle, the powder reaches ~12.7 mm (i.e., collides with the roof of the microreactor duct). Ph. D. 2014-03-14T21:17:23Z 2014-03-14T21:17:23Z 1992-03-04 2007-08-08 2007-08-08 2007-08-08 Dissertation Text etd-08082007-115021 http://hdl.handle.net/10919/39083 http://scholar.lib.vt.edu/theses/available/etd-08082007-115021/ en OCLC# 26064294 LD5655.V856_1992.B397.pdf In Copyright http://rightsstatements.org/vocab/InC/1.0/ xxiii, 463 leaves BTD application/pdf application/pdf Virginia Tech |
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LD5655.V856 1992.B397 Fluidized reactors -- Design Benge, G. Gregory Cold model of a vibrated-bed microreactor capable of varying Peclet number at fixed weight hourly space velocity providing a tool for simulating an important feature of the reaction kinetic scene in large catalytic fluid beds |
description |
A cold-flow model of a vibrated-bed microreactor has been designed and tested with capability
for varying the level of gas dispersion (characterized by axial Peclet number) at a fixed weight hourly
space velocity (WHSV). A tool has thus been provided whereby an important feature (viz., gas
dispersion) of the reaction kinetic scene in large catalytic fluid beds can be simulated on a microscale,
using approximately 5 grams of catalyst.
Realization of a hot design of the microreactor (a task for another student) should permit the
industrial chemist or chemical engineer, working at laboratory bench scale, quickly and
inexpensively, to determine the sensitivity of a cataly1ic reaction to fluid-bed gas dispersion.
The new microreactor exploits the coherent-expanded (C-E) vibrated-bed state, and is perhaps
the first technical use of this state. The C-E state is achieved by subjecting a shallow layer of a fine
powder to vertical sinusoidal vibration. The microreactor comprises a rectangular horizontal duct,
12.7 mm in height, 25.4 mm in width, variable in length, and with nonporous floor and walls. The
microreactor is charged with a powder, such as fluid cataly1ic cracking (FCC) catalyst, at a compacted
depth of I mm, and is vibrated at ~15 Hertz and amplitude of ~3 mm. Under influence of this vibration, the powder expands, displaying the C-E state. Between a phase angle of ~50° and an angle of ~150°, the powder assumes a depth of ~4 mm (i.e., expanded 4-fold from its compacted
depth). Later, in each vibration cycle, the powder expands further. At ~300° phase angle, the
powder reaches ~12.7 mm (i.e., collides with the roof of the microreactor duct). === Ph. D. |
author2 |
Chemical Engineering |
author_facet |
Chemical Engineering Benge, G. Gregory |
author |
Benge, G. Gregory |
author_sort |
Benge, G. Gregory |
title |
Cold model of a vibrated-bed microreactor capable of varying Peclet number at fixed weight hourly space velocity providing a tool for simulating an important feature of the reaction kinetic scene in large catalytic fluid beds |
title_short |
Cold model of a vibrated-bed microreactor capable of varying Peclet number at fixed weight hourly space velocity providing a tool for simulating an important feature of the reaction kinetic scene in large catalytic fluid beds |
title_full |
Cold model of a vibrated-bed microreactor capable of varying Peclet number at fixed weight hourly space velocity providing a tool for simulating an important feature of the reaction kinetic scene in large catalytic fluid beds |
title_fullStr |
Cold model of a vibrated-bed microreactor capable of varying Peclet number at fixed weight hourly space velocity providing a tool for simulating an important feature of the reaction kinetic scene in large catalytic fluid beds |
title_full_unstemmed |
Cold model of a vibrated-bed microreactor capable of varying Peclet number at fixed weight hourly space velocity providing a tool for simulating an important feature of the reaction kinetic scene in large catalytic fluid beds |
title_sort |
cold model of a vibrated-bed microreactor capable of varying peclet number at fixed weight hourly space velocity providing a tool for simulating an important feature of the reaction kinetic scene in large catalytic fluid beds |
publisher |
Virginia Tech |
publishDate |
2014 |
url |
http://hdl.handle.net/10919/39083 http://scholar.lib.vt.edu/theses/available/etd-08082007-115021/ |
work_keys_str_mv |
AT bengeggregory coldmodelofavibratedbedmicroreactorcapableofvaryingpecletnumberatfixedweighthourlyspacevelocityprovidingatoolforsimulatinganimportantfeatureofthereactionkineticsceneinlargecatalyticfluidbeds |
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