Radial-Flow Reactor Packed with a Catalytic Cloth: Nitrate Reduction in Hydrogen-Saturated Water
A novel flow reactor packed with a fibrous catalytic cloth is proposed to carry out a gas−liquid reaction. Radial flow and separation of the transport of the gaseous reactant and the reaction are the main features of the new design. An activated carbon cloth supported 2 wt % Pd−0.6 wt % Cu bimetalli...
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Published in | Industrial & engineering chemistry research Vol. 44; no. 25; pp. 9575 - 9580 |
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Main Author | |
Format | Journal Article |
Language | English |
Published |
Washington, DC
American Chemical Society
07.12.2005
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Subjects | |
Online Access | Get full text |
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Summary: | A novel flow reactor packed with a fibrous catalytic cloth is proposed to carry out a gas−liquid reaction. Radial flow and separation of the transport of the gaseous reactant and the reaction are the main features of the new design. An activated carbon cloth supported 2 wt % Pd−0.6 wt % Cu bimetallic catalyst installed in the reactor was applied for the water-phase nitrate hydrogenation, showing selectivity up to 84% toward nitrogen at a nitrate conversion of up to 93%. The reactor performance has been evaluated using the diagnostic criteria associated with varying the hydrogen pressure, liquid flow rate, and catalyst loading in the reactor; it was described by a simplistic model, assuming one-dimensional, plug-flow, and steady-state operation. The significance of mass-transfer effects on the reactor performance has been analyzed. The results obtained indicate that the reactor investigated has a high potential for further development and scale-up. |
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Bibliography: | ark:/67375/TPS-HP7QT7SV-V istex:0ED4BA535281E640B3116AEB3F4553C09B03A0BD |
ISSN: | 0888-5885 1520-5045 |
DOI: | 10.1021/ie050260v |