Determination of fast gas-liquid reaction kinetics in flow

We present a flow concept to measure fast gas-liquid reaction kinetics. A tube-in-tube reactor design with semipermeable Teflon AF-2400 tubes is adopted to achieve fast gas-liquid mass transfer without direct contact of gas and liquid. By performing a steady-state flux balance of both gas and liquid...

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Bibliographic Details
Main Authors: Zhang, Jisong (Author), Teixeira, Andrew (Author), Zhang, Haomiao (Author), Jensen, Klavs F (Author)
Other Authors: Massachusetts Institute of Technology. Department of Chemical Engineering (Contributor)
Format: Article
Language:English
Published: Royal Society of Chemistry (RSC), 2020-02-28T18:32:26Z.
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Online Access:Get fulltext
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100 1 0 |a Zhang, Jisong  |e author 
100 1 0 |a Massachusetts Institute of Technology. Department of Chemical Engineering  |e contributor 
700 1 0 |a Teixeira, Andrew  |e author 
700 1 0 |a Zhang, Haomiao  |e author 
700 1 0 |a Jensen, Klavs F  |e author 
245 0 0 |a Determination of fast gas-liquid reaction kinetics in flow 
260 |b Royal Society of Chemistry (RSC),   |c 2020-02-28T18:32:26Z. 
856 |z Get fulltext  |u https://hdl.handle.net/1721.1/123889 
520 |a We present a flow concept to measure fast gas-liquid reaction kinetics. A tube-in-tube reactor design with semipermeable Teflon AF-2400 tubes is adopted to achieve fast gas-liquid mass transfer without direct contact of gas and liquid. By performing a steady-state flux balance of both gas and liquid flowing into the reactor and developing a mathematical model based on the film theory, the reaction kinetic parameters can be determined with excellent precision with the use of only a single gas flow meter. Reactions of CO2 with alkanolamines and ozonolysis of organics serve as case studies to assess the ability of the technique to resolve reaction kinetics in situ. The proposed strategy presents a new opportunity for the study of fundamental aspects of gas-liquid reactions in a simple, safe, automated and high-throughput manner. 
655 7 |a Article 
773 |t Reaction Chemistry and Engineering