Abstract
The structured cartridges with glass-fiber catalyst (GFC) with axial flow of gaseous reactants were studied in terms of pressure drop and mass transfer limitations. The universal equation for calculation of the pressure drop for cartridges of the various design was proposed. Mass transfer intensity in the GFC cartridges was studied on the base of model reaction of ethylbenzene deep oxidation in air. The obtained data on external mass transfer coefficient may be described by the common criterial equation Sh = 0.0695Re0.93Sc1/3. According to the quality of the compromise between mass transfer efficiency and unit pressure drop the structured cartridges with glass-fiber catalysts were found to be one of the most promising forms of catalysts from the reaction engineering point of view.
| Original language | English |
|---|---|
| Pages (from-to) | 58-65 |
| Number of pages | 8 |
| Journal | Chemical Engineering Journal |
| Volume | 282 |
| DOIs | |
| Publication status | Published - 15 Dec 2015 |
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Keywords
- Glass-fiber catalyst
- Mass transfer
- Pressure drop
- Structured cartridge
ASJC Scopus subject areas
- Chemical Engineering(all)
- Chemistry(all)
- Industrial and Manufacturing Engineering
- Environmental Chemistry
Cite this
Pressure drop and mass transfer in the structured cartridges with fiber-glass catalyst. / Lopatin, Sergey; Mikenin, Pavel; Pisarev, Danil; Baranov, Dmitry; Zazhigalov, Sergey; Zagoruiko, Andrey Nikolaevich.
In: Chemical Engineering Journal, Vol. 282, 15.12.2015, p. 58-65.Research output: Contribution to journal › Article
}
TY - JOUR
T1 - Pressure drop and mass transfer in the structured cartridges with fiber-glass catalyst
AU - Lopatin, Sergey
AU - Mikenin, Pavel
AU - Pisarev, Danil
AU - Baranov, Dmitry
AU - Zazhigalov, Sergey
AU - Zagoruiko, Andrey Nikolaevich
PY - 2015/12/15
Y1 - 2015/12/15
N2 - The structured cartridges with glass-fiber catalyst (GFC) with axial flow of gaseous reactants were studied in terms of pressure drop and mass transfer limitations. The universal equation for calculation of the pressure drop for cartridges of the various design was proposed. Mass transfer intensity in the GFC cartridges was studied on the base of model reaction of ethylbenzene deep oxidation in air. The obtained data on external mass transfer coefficient may be described by the common criterial equation Sh = 0.0695Re0.93Sc1/3. According to the quality of the compromise between mass transfer efficiency and unit pressure drop the structured cartridges with glass-fiber catalysts were found to be one of the most promising forms of catalysts from the reaction engineering point of view.
AB - The structured cartridges with glass-fiber catalyst (GFC) with axial flow of gaseous reactants were studied in terms of pressure drop and mass transfer limitations. The universal equation for calculation of the pressure drop for cartridges of the various design was proposed. Mass transfer intensity in the GFC cartridges was studied on the base of model reaction of ethylbenzene deep oxidation in air. The obtained data on external mass transfer coefficient may be described by the common criterial equation Sh = 0.0695Re0.93Sc1/3. According to the quality of the compromise between mass transfer efficiency and unit pressure drop the structured cartridges with glass-fiber catalysts were found to be one of the most promising forms of catalysts from the reaction engineering point of view.
KW - Glass-fiber catalyst
KW - Mass transfer
KW - Pressure drop
KW - Structured cartridge
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UR - http://www.scopus.com/inward/citedby.url?scp=84947869283&partnerID=8YFLogxK
U2 - 10.1016/j.cej.2015.02.026
DO - 10.1016/j.cej.2015.02.026
M3 - Article
AN - SCOPUS:84947869283
VL - 282
SP - 58
EP - 65
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
SN - 1385-8947
ER -