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1
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Pressure drop in two-phase gas-liquid (Taylor) flow in microreactors

100%
Cygański P., Sobieszuk P., Pohorecki R.
Chemical and Process Engineering
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2012
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vol. 33
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issue 3
369-384
EN
The pressure drop in microreactors for the gas - liquid Taylor flow was measured for 4 different microreactor geometries and 3 different gas - liquid systems. The results have been compared with the existing literature correlations. A selection of the best correlations has been made.
2
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Investigations of mass transfer in annular gas-liquid flow in a microreactor

100%
Sobieszuk P., Napieralska K.
Chemical and Process Engineering
|
2016
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vol. 37
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issue 1
3
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Content available

Pressure drop in two-phase gas-liquid (Taylor) flow in microreactors

100%
Cygański P., Sobieszuk P., Pohorecki R.
Chemical and Process Engineering
|
2012
|
issue 3
4
Content available remote

Contribution of Liquid- and Gas-Side Mass Transfer Coefficients to Overall Mass Transfer Coefficient in Taylor Flow in a Microreactor

100%
Sobieszuk P., Ilnicki F., Pohorecki R.
Chemical and Process Engineering
|
2014
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vol. 35
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issue 1
35-45
EN
Gas-liquid microreactors find an increasing range of applications both in production, and for chemical analysis. The most often employed flow regime in these microreactors is Taylor flow. The rate of absorption of gases in liquids depends on gas-side and liquid-side resistances. There are several publications about liquid-side mass transfer coefficients in Taylor flow, but the data about gas-side mass transfer coefficients are practically non existent. We analysed the problem of gas-side mass transfer resistance in Taylor flow and determined conditions, in which it may influence the overall mass transfer rate. Investigations were performed using numerical simulations. The influence of the gas diffusivity, gas viscosity, channel diameter, bubble length and gas bubble velocity has been determined. It was found that in some case the mass transfer resistances in both phases are comparable and the gas-side resistance may be significant. In such cases, neglecting the gas-side coefficient may lead to errors in the experimental data interpretation.
5
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Numerical modelling of a microreactor for thermocatalytic decomposition of toxic compounds

100%
Jóźwik P., Karcz M., Badur J.
Chemical and Process Engineering
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2011
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vol. 32
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issue 3
215-227
EN
In this paper a three-dimensional model for determination of a microreactor's length is presented and discussed. The reaction of thermocatalytic decomposition has been implemented on the base of experimental data. Simplified Reynolds-Maxwell formula for the slip velocity boundary condition has been analysed and validated. The influence of the Knudsen diffusion on the microreactor's performance has also been verified. It was revealed that with a given operating conditions and a given geometry of the microreactor, there is no need for application of slip boundary conditions and the Knudsen diffusion in further analysis. It has also been shown that the microreactor's length could be practically estimated using standard models.
6
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Numerical modelling of a microreactor for thermocatalytic decomposition of toxic compounds

88%
Badur J., Jóźwik P., Karcz M.
Chemical and Process Engineering
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2011
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issue 3
7
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Contribution of Liquid- and Gas-Side Mass Transfer Coefficients to Overall Mass Transfer Coefficient in Taylor Flow in a Microreactor

88%
Pohorecki R., Sobieszuk P., Ilnicki F.
Chemical and Process Engineering
|
2014
|
issue 1
8
Content available remote

Absorption of Co2 into Perfluorinated Gas Carrier in the Taylor Gas–Liquid Flow in a Microchannel System

88%
Sobieszuk P., Pilarek M.
Chemical and Process Engineering
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2012
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vol. 33
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issue 4
595-602
EN
The aim of this study was to determine the solubility of CO2 in perfluorodecalin (PFD) which is frequently used as efficient liquid carrier of respiratory gases in bioprocess engineering. The application of perfluorinated liquid in a microsystem has been presented. Gas-liquid mass transfer during Taylor (slug) flow in a microchannel of circular cross section 0.4 mm in diameter has been investigated. A physicochemical system of the absorption of CO2 from the CO2/N2 mixture in perfluorodecalin has been applied. The Henry’s law constants have been found according to two theoretical approaches: physical (H = 1.22·10-3 mol/m3Pa) or chemical (H = 1.26·10-3 mol/m3Pa) absorption. We are hypothesising that the gas-liquid microchannel system is applicable to determine the solubility of respiratory gases in perfluorinated liquids.
9
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Absorption of Co2 into Perfluorinated Gas Carrier in the Taylor Gas–Liquid Flow in a Microchannel System

75%
Sobieszuk P., Pilarek M.
Chemical and Process Engineering
|
2012
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issue 4
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