III International Conference

PP-III-75three MCP’s. In the second microreactor we used special 0.5 mm flat microelectroheatersinstead of copper plates. We found that in both microreactors MSR is carried out moreeffectively. In the first microreactor the hydrogen production is two times more than that forthe microreactor without copper plates. Microreactor with internal flat microelectroheatersreaches hydrogen production equal to 140 l/h at the reaction volume 22 cm 3 .References1. Lykov A. Methods of heat counduction and thermal diffusivity meashuring. Moskow, Energia,1973.2. Liu Y, Hayakawa T, Suzuki K, Hamakawa S, Tsunoda T, Ishii T, Kumagai M. Highly activecopper/ceria catalysts for steam reforming of methanol. Appl Catal A 2002;223(1-2):137–145.3. L.L. Makarshin, D.V. Andreev, A.G.Gribovskiy, P.M.Dutov, R.M.Hantakov and V.N.Parmon.Influence of the microchannel plates’ design on the efficiency of the methanol steam reforming inmicroreactors. Kinetics and Catalysis, 2007, In Press.611