WERKWIJZE VOOR DE BEREIDING VAN EEN KATALYSATOR EN WERKWIJZE VOOR HET KATALYTISCH DEHYDROGENEREN VAN ALIFATISCHE EN NAFTENISCHE KOOLWATERSTOFFEN ONDER TOEPASSING VAN DE ALDUS BEREIDE KATALYSATOR.

摘要

1328455 Dehydrogenation catalysts INSTITUT FRANCAIS DU PETROLE DES CARBURANTS ET LUBRIFIANTS 27 April 1971 [30 April 1970] 11677/71 Heading B1E [Also in Division C5] Catalyst for use in the dehydrogenation of saturated hydrocarbons comprises (a) from 0.05 to 2 weight per cent of molybdenum or tungsten, from 0.05 to 2 weight per cent of rhenium and (c) alumina. The catalyst may be prepared by a procedure which comprises depositing molybdenum or tungsten valves and rhenium valves, either separately or simultaneously, from solution on the alumina, the resulting material being dried, optionally calcined in an oxidising atmosphere at a temperature of from 300 to 600‹C, and reduced in a hydrogen stream at a temperature of from 350 to 700‹C. The alumina, which may be in the form of extrudates, pellets or spheres, may be treated, either before or after incorporation with the molybdenum or tungsten valves and the rhenium valves, with a basic compound or a compound decomposable thereto ladder dehydrogenation reaction conditions, for example an alkali metal or alkaline earth metal oxide, hydroxide, carbonate or other weak acid salt, for instance sodium hydroxide, potassium hydroxide, sodium carbonate potassium carbonate, sodium nitrate, magnesium acetate or calcium acetate, in an amount preferably of not more than 2 weight per cent of the alumina. The alumina (and the catalyst prepared therefrom) may have a heat of neutralization by ammonia absorption at 320‹C under a pressure of 300 mm Hg of below 10 calories per gram, a surface area of from 20 to 150 m2/g and a pore volume of from 0.4 to 0.8 cm3/g, preferably at least 75 per cent of the pore volume being constituted by pores having an average diameter of from 100 to 500 Angstrons. Examples relate to catalysts which comprise molybdenum, rhenium and gamma-alumina and tungsten, rhenium and alpha-alumina, gamma-alumina or (unspecified) transition alumina; deactivated catalyst which comprises tungsten, rhenium and gamma-alumina is regenerated by sequential contact, at specified elevated temperatures, with an air stream, a nitrogen stream and a hydrogen stream.