External mass transfer in a laser sintered structured reactor for continuous hydrogenation of alkynes
External mass transfer in a laser sintered structured reactor for continuous hydrogenation of alkynes
This work presents a study on the continuous operation of a structured reactor for alkyne hydrogenation in the field of Process Intensification. The reactor consists of a laser sintered metal structure characterized by a regular geometry, coated with a layer of ZnO/Al2O3 and impregnated with palladium nanoparticles. The partial hydrogenation of 2-methyl-3-butyn-2-ol with co-current gas-liquid upward flow was used as the test reaction system. A plug flow reactor model was applied to study the mass transfer phenomena under the reacting conditions. The reaction kinetics with the Pd/ZnO-based catalyst were simplified using a power rate law expression. The results in terms of the overall mass transfer coefficient Kov were modelled with a predictive Sherwood number correlation whose parameters were estimated by means of an optimization procedure. The structured reactor shows an overall mass transfer coefficient ranging between 0.2 and 1.2 s−1 depending on the operating conditions. The model is able to predict the impact of temperature (333–363 K), pressure (3.0–7.0 bar), gas velocity (0.005–0.024 m s−1) and liquid velocity (0.025–0.085 m s−1) on the overall mass transfer coefficient with a maximum deviation of 15%.
74-80
Vernuccio, Sergio
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Dempfle, David
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Goy, Roman
ccec5251-33fc-49b7-ba6e-883d5beb866a
Medlock, Jonathan
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von Rohr, Philipp Rudolf
733c7f0c-8b65-45fa-a5ed-e378f18f131b
Vernuccio, Sergio
4bafd7f3-0943-4f6c-bc78-b4026516ccdb
Dempfle, David
d6522b2f-b9df-4953-a380-5e55bf11e793
Goy, Roman
ccec5251-33fc-49b7-ba6e-883d5beb866a
Medlock, Jonathan
cd7bdd75-d3f2-4478-8f59-aa728d64126b
von Rohr, Philipp Rudolf
733c7f0c-8b65-45fa-a5ed-e378f18f131b
Vernuccio, Sergio, Dempfle, David, Goy, Roman, Medlock, Jonathan and von Rohr, Philipp Rudolf
(2018)
External mass transfer in a laser sintered structured reactor for continuous hydrogenation of alkynes.
Chemical Engineering and Processing - Process Intensification, 126, .
(doi:10.1016/j.cep.2018.02.005).
Abstract
This work presents a study on the continuous operation of a structured reactor for alkyne hydrogenation in the field of Process Intensification. The reactor consists of a laser sintered metal structure characterized by a regular geometry, coated with a layer of ZnO/Al2O3 and impregnated with palladium nanoparticles. The partial hydrogenation of 2-methyl-3-butyn-2-ol with co-current gas-liquid upward flow was used as the test reaction system. A plug flow reactor model was applied to study the mass transfer phenomena under the reacting conditions. The reaction kinetics with the Pd/ZnO-based catalyst were simplified using a power rate law expression. The results in terms of the overall mass transfer coefficient Kov were modelled with a predictive Sherwood number correlation whose parameters were estimated by means of an optimization procedure. The structured reactor shows an overall mass transfer coefficient ranging between 0.2 and 1.2 s−1 depending on the operating conditions. The model is able to predict the impact of temperature (333–363 K), pressure (3.0–7.0 bar), gas velocity (0.005–0.024 m s−1) and liquid velocity (0.025–0.085 m s−1) on the overall mass transfer coefficient with a maximum deviation of 15%.
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Accepted/In Press date: 6 February 2018
e-pub ahead of print date: 9 February 2018
Identifiers
Local EPrints ID: 495792
URI: http://eprints.soton.ac.uk/id/eprint/495792
ISSN: 0255-2701
PURE UUID: 75fe82ae-c2b6-4843-94fd-e242a9de68a9
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Date deposited: 22 Nov 2024 17:45
Last modified: 23 Nov 2024 03:13
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Author:
Sergio Vernuccio
Author:
David Dempfle
Author:
Roman Goy
Author:
Jonathan Medlock
Author:
Philipp Rudolf von Rohr
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