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Boreskov Institute of Catalysis SB RAS, Novosibirsk, Russia

Boreskov Institute of Catalysis SB RAS, Novosibirsk, Russia

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COMPLEX WASTE-FREE TECHNOLOGY OF ANILINEAND N-MONOMETHYLANILINE PREPARATION WITH USEHETEROGENEOUS Cu-BASED CATALYST<strong>SB</strong>achurikhin A.L. 1 , Golosman E.Z. 2PP-41 N.D. Zelinsky <strong>Institute</strong> <strong>of</strong> Organic Chemistry <strong>of</strong> the <strong>Russia</strong>n Academy <strong>of</strong> Science,<strong>Russia</strong>, Moscow 119991, GSP - 1, the Leninscky av., 47,E-mail: SECRETARY@ioc.ac.ru2 LLC "NIAP-KATALIZATOR", Novomoskovsk, <strong>Russia</strong>Aniline and N-monomethylaniline are the major products <strong>of</strong> the chemical industry,world which total manufacture annually increases approximately for 5 % and now isat a level about 5 million tons one year. Aniline is strategic raw material inmanufacture <strong>of</strong> dyes, medical products, explosives, N-monomethylaniline anddiphenylmethanediisocyanate - a component for manufacture polyurethanes. N-monomethylaniline - an antidetonation additive for easy updating octane numbersautomobile fuels.Technological process <strong>of</strong> preparation <strong>of</strong> aniline and N-monomethylaniline isdeveloped and is at a stage <strong>of</strong> preparation <strong>of</strong> pilot tests on the basis <strong>of</strong> usenitrobenzene and methanol as initial products. Process is characterized by use <strong>of</strong>catalysts on the basis <strong>of</strong> Al 2 O 3 and Fe 2 O 3 , modified CuO (6÷60 weights <strong>of</strong> %) and Cr,Mn (III, IV)-oxide (0÷1 weights <strong>of</strong> %), tubular reactor systems with the multizonecontrol <strong>of</strong> temperature pr<strong>of</strong>ile. Process differs an opportunity <strong>of</strong> joint and separatepreparation <strong>of</strong> aniline and N-monomethylaniline, absence <strong>of</strong> necessity <strong>of</strong> use <strong>of</strong>hydrogen as separate initial component, high efficiency and absence <strong>of</strong> harmfulwaste products.The work cycle is characterized by presence <strong>of</strong> the following stages:1) Fluid-phased nitrobenzene hydrogenation at speeds up to 10 h –1 in fluidphasedcatalytic hydrogenation battery, consisting <strong>of</strong> the several, consistentlyconnected reactors, with consistently growing temperature <strong>of</strong> hydrogenation in aninterval 100-300°С2) Alkylation aniline with methanol and re-alkylation in system aniline - N,Ndimethylaniline,proceeding at speeds up to 10 h –1 in a temperature interval 250-300°С3) Sequence <strong>of</strong> transformations <strong>of</strong> the easy gaseous products including a)Decomposition residual <strong>of</strong> methanol; b) Disproportion reaction <strong>of</strong> mixes CO, Н 2 and91

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