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...

Full description

Bibliographic Details
Main Author: Benge, G. Gregory
Other Authors: Chemical Engineering
Format: Others
Language:en
Published: Virginia Tech 2014
Subjects:
Online Access:http://hdl.handle.net/10919/39083
http://scholar.lib.vt.edu/theses/available/etd-08082007-115021/
id ndltd-VTETD-oai-vtechworks.lib.vt.edu-10919-39083
record_format oai_dc
spelling 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
collection NDLTD
language en
format Others
sources NDLTD
topic LD5655.V856 1992.B397
Fluidized reactors -- Design
spellingShingle 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
_version_ 1719397706268409856