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European Congress of Chemical Engineering - 6
Copenhagen 16-21 September 2007

Abstract 417 - Catalytic Wet Air Oxidation of Aqueous Solution of Phenol over Pt/CNF Catalysts

Catalytic Wet Air Oxidation of Aqueous Solution of Phenol over Pt/CNF Catalysts

Advancing the chemical engineering fundamentals

Catalysis - III (T2-13c)

Mrs Carmen Diaz
Universidad Complutense de Madrid
Departamento de Ingenieria Química
Avda. Complutense s/n
28040 Madrid
Spain

Dr Juan Garcia
Complutense University of Madrid
CyPS, Department of Chemical Engineering
Dpto. Ingenieria Quimica. Fac. C.C. Quimicas. Avda. Complutense s/n
28040 Madrid
Spain

Mr Gabriel Ovejero
Universidad Complutense de madrid
Departamento de Ingenieria Quimica
Avda. Complutense s/n
28040 Madrid
Spain

Mr Araceli Rodriguez
Universidad Complutense de Madrid
Ingenieria Química
Avda. Complutense s/n
28040 Madrid
Spain

Keywords: carbon nanofibers, catalytic wet oxidation, kinetic

During the past two decades, carbon nanofibres (CNFs), including multi-walled carbon nanotubes (MWNTs), have attracted extensive interest and attention from both academia and industry. Due to their novel physico-chemical and mechanical properties, CNFs exhibit growing perspectives in a number of potential applications, especially in heterogeneous catalysis (G. Ovejero, 2006).
One of the advantages of CNFs used as catalysts and catalyst supports is the possibility of tailoring their microstructures by proper selection of preparation method and controlling their surface chemistry via surface modification (P. Serp, 2003). The mesoporous macrostructure with relatively high specific surface area and almost completely exposed external surface of these materials can be expected to reduce the inner pore diffusion resistance dramatically during the reaction (J. Garcia, 2006).
Therefore, the aim of this work is the study of the catalytic wet air oxidation (CWAO) of phenol, as model organic compound of many industrial wastewaters, using 2 wt. % platinum supported in commercial CNF as catalyst in a continuous trickled bed reactor.
Samples were taken periodically to measure the phenol conversion and analyze the Total Organic Carbon (TOC).
The effect of process parameter like temperature, pressure, catalyst load, air flow, liquid flow and pollutant concentration, has been studied. The experimental dates were satisfactory fitted to a Langmuir-Hinshelwood kinetic model. The conversion of phenol increases with the temperature, pressure and catalyst load.
It was demonstrated that Pt/CNF is an efficient catalyst for the CWAO of phenol. High phenol conversion and TOC removal can be reached over this catalyst at mild reaction temperature (433 K) and moderate pressure (2.0 MPa).


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Presented Thursday 20, 15:00 to 15:20, in session Catalysis - III (T2-13c).

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