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Membrane reactors volatile organic compounds

Pina MP, Menendez M, and Santamaria J. The Knudsen-diffusion catalytic membrane reactor an efficient contactor for the combustion of volatile organic compounds. Appl. Catal. B Environ. 1996 11(1) L19-L27. [Pg.179]

Pina, M., Menendez, M. and Santamaria, J. (1996). The Knudsen-DiffusionCatalytic Membrane Reactor An Efficient Contactor for the Combustion of Volatile Organic Compounds, Appl. Catal. B Environ., 11, pp. L19-L27. [Pg.936]

Santamaria and coworkers (Aguado cf a/.,2005) preparedPt/ZSM-5 membrane reactors for the combustion of n-hexane present at a low concentration in the air. Experimental results showed that n-hexane combustion was achieved at 210°C. A comparison of the conversion of the hexane obtained using the membrane reactor and the fixed bed reactor evidenced the better performance of the membrane reactor with a light-off temperature lower (about 70°C) than that obtained in the fixed bed reactor as illustrated in Fig. 6.5. Another example of the successful application of a Pt/ZSM-5 membrane in the catalytic combustion of volatile organic compounds (VOCs) (Bottino et al, 2001) showed that a high removal efficiency of toluene can be obtained and that the zeolite membrane with a relatively thick layer (40 pm) is clearly affected by mass transfer limitations. [Pg.259]


See other pages where Membrane reactors volatile organic compounds is mentioned: [Pg.157]    [Pg.242]    [Pg.304]    [Pg.66]    [Pg.330]    [Pg.970]    [Pg.932]    [Pg.287]   


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