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Boreskov Institute of Catalysis SB RAS, Novosibirsk, Russia

Boreskov Institute of Catalysis SB RAS, Novosibirsk, Russia

Boreskov Institute of Catalysis SB RAS, Novosibirsk, Russia

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PP-62CERAMIC MEMBRANES IN THE PROCESSES OF VAPORCONVERSION OF ETHANOL AND ACETIC ACID AS THE MAINPRODUCTS OF BIOMASS FERMENTATIONUvarov V.I., Borovinskaya I.P., Malevannaya I.G.<strong>Institute</strong> <strong>of</strong> Structural Macrokinetics and Materials Science <strong>RAS</strong>, Chernogolovka,Moscow region, 142432 <strong>Russia</strong>. E-mail: uvar@ism.ac.ruThe paper is dedicated to obtaining high-temperature, corrosion-resistant,mechanically strong nano-porous structures by self-propagating high-temperaturesynthesis and producing efficient membranes based on the structures for vaporconversion <strong>of</strong> ethanol and acetic acid as the main products <strong>of</strong> biomass fermentation.At first the «gas-kinetic model» <strong>of</strong> porous structure formation during SHS wasconsidered and Laplace’s equation was used for determining the pore size. Themetal melts in the combustion wave and spreads with a liquid layer formation. If inthis case the pressure <strong>of</strong> the liquid vapor and impuritive gases in the liquid is higherthan the external pressure, the open porosity <strong>of</strong> the final product (membrane) isformed at fast cooling.The conditions <strong>of</strong> the open and closed porosity formation were defined; the zone<strong>of</strong> conversion <strong>of</strong> the closed porosity <strong>of</strong> the synthesized material to its open value wasalso found. It allows controlling the structure and pore size in the obtained gradednano-porous SHS materials, i.e. membranes.Using the «gas-kinetic model», we developed the modes for synthesizingcatalytically active high-porous ceramic carriers <strong>of</strong> membrane-catalytic systemsbased on refractory inorganic compounds Ni-Al-Co; Ni-Al-Co/NiO, Ni-Al-Mn, Ni-Al-Ti,Ni-Al/NiO with the following characteristics:Open porosity, % 40 – 58Pore size, μm 10 – 0.01Bending strength, MPa 50 – 60Specific surface, m 2 /g 3 – 10The structure <strong>of</strong> the samples was studied with an electronic microscope, thestructural analysis was carried out using an X-ray microanalyser. A membranecatalyticmodule with gas consumption <strong>of</strong> up to 25 m 3 /h was made.The catalytic layer <strong>of</strong> metal oxides was formed inside the membrane channels bythe sol-gel method using organic solutions <strong>of</strong> metal-complex precursors in toluene153

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