PRODUCTION OF DIPHENYLAMINE COMPOUND
PURPOSE:To produce the titled compound, in high yield, under a low temperature condition, with elongated catalyst life, by the vapor-phase catalytic reaction of an aniline compound using a weak acid-type silica-alumina solid acid catalyst composed mainly of gamma-alumina and containing large-sized p...
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Main Authors | , , |
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Format | Patent |
Language | English |
Published |
22.03.1985
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Subjects | |
Online Access | Get full text |
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Summary: | PURPOSE:To produce the titled compound, in high yield, under a low temperature condition, with elongated catalyst life, by the vapor-phase catalytic reaction of an aniline compound using a weak acid-type silica-alumina solid acid catalyst composed mainly of gamma-alumina and containing large-sized pores at high ratio. CONSTITUTION:The objective compound is produced by using a silica-alumina solid acid catalyst composed mainly of gamma-alumina, exhibiting weak acidity represented by a Hammett's acidity function HO, max (showing the maximum acid strength of a catalyst) of >4.0, having an average pore diameter of 40-100Angstrom , the total volume of the <=100Angstrom phi pores of <=50% (especially <=30%) of the whole pore volume, and having a specific surface area of >=150m /g, and contacting the catalyst with the vapor of an aniline compound at 300-400 deg.C, preferably 330- 390 deg.C and 1-25atm for 300-1,000sec. The catalyst has high activity at a low temperature, and long life, and keeps the initial productivity comparable to the conventional catalyst even at a temperature lower than that of the conventional process by 100 deg.C. |
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Bibliography: | Application Number: JP19830159470 |