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A method and device for the reaction of a solid, in the shape of the particles present in the heat evaporable reaction participant with a gaseous reaktionsteilnemer
A method and device for the reaction of a solid, in the shape of the particles present in the heat evaporable reaction participant with a gaseous reaktionsteilnemer
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机译:用于以热蒸发反应参与物形式存在的颗粒形状的固体与气态重整反应器反应的方法和装置
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摘要
PICT:0819051/III/1 In an apparatus for reacting solids with gases, the solid in particulate form is carried as a suspension in an inert gas heated to a temperature below the softening point of the solid, through a cooling zone immediately after which it passes together with the reactant gas heated to a temperature above the softening point of the solid, to a vaporizer where the solid particles react with the gas and then flow into a reactor which may contain a dehydrating catalyst. For example, phthalonitrile is made by feeding iso-or terephthalic acid through a star valve into a tube 7, Fig. 1, where it forms a suspension in nitrogen heated at 60/400 DEG F. admitted in a pipe 9. Ammonia gas admitted through a pipe 10 and heated at 800/100 DEG F. carries the suspension into a vaporizer 14, any conducted heat being absorbed in a jacket condenser 11, which prevents the solid particles melting in advance of the ammonia treatment. The mixed product passes to a dehydration reactor, heated externally at 750 DEG to 850 DEG F., and containing a catalyst, e.g. alumina, silica, or thoria, whereby phthalonitrile is formed. This is recovered from the vapours issuing from a line 15, by solvent extraction or by crystallization.ALSO:Phthalonitriles are made by feeding powdered iso- or terephthalic acid into a tube 7, Fig. 1, where it forms a suspension in nitrogen heated below the melting-point of the acid, and injected through a pipe 9. Ammonia gas admitted through a pipe 10 and heated at 800/1000 DEG F. carries the suspension into a vaporizer 14, any PICT:0819051/IV (b)/1 conducted heat being absorbed in a jacket condenser 11, which prevents the acid particles melting in advance of the ammonia treatment. The mixed product passes to a dehydration reactor 15, heated externally to 750 DEG to 850 DEG F., and containing a catalyst, e.g. thoria, silica, or alumina, whereby phthalonitrile is formed, substantially free from side-reaction products. The product vapours issuing from a line 22 are submitted to solvent extraction, or crystallization to recover the phthalonitrile.
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