Photocatalytic degradation of some VOCs in the gas phase using an annular flow reactor - Determination of the contribution of mass transfer and chemical reaction steps in the photodegradation process
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Bouzaza, A
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Ecole Natl Super Chim Rennes, Lab Rennais Chim & Ingn Procedes, F-35700 Rennes, FranceEcole Natl Super Chim Rennes, Lab Rennais Chim & Ingn Procedes, F-35700 Rennes, France
Bouzaza, A
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Vallet, C
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Ecole Natl Super Chim Rennes, Lab Rennais Chim & Ingn Procedes, F-35700 Rennes, FranceEcole Natl Super Chim Rennes, Lab Rennais Chim & Ingn Procedes, F-35700 Rennes, France
Vallet, C
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Laplanche, A
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Ecole Natl Super Chim Rennes, Lab Rennais Chim & Ingn Procedes, F-35700 Rennes, FranceEcole Natl Super Chim Rennes, Lab Rennais Chim & Ingn Procedes, F-35700 Rennes, France
Laplanche, A
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[1] Ecole Natl Super Chim Rennes, Lab Rennais Chim & Ingn Procedes, F-35700 Rennes, France
The photodegradation of some VOCs in an annular reactor is chemical step controlled. The limitation due to mass transfer is negligible. The use of a combined plug-flow model shows that the apparent rate constant (k*) is equal to W representing the Lanumuir-Hinshelwood rate constants. So the design of an annular reactor using the L-H model can be considered. The photodegradability of the tested VOCs is strongly dependent on the product W. Trichloroethylene is the best degraded while toluene is the worst. The study of the mineralization rate, defined as the ultimate degradation phase of the compounds, shows that this last is firstly dependent on the contact time and not on the nature of the VOC. Moreover increasing the inlet VOC concentration leads to a decrease in the mineralization rate. (c) 2005 Elsevier B.V. All rights reserved.