Synthetic Rubber from Acetylene. III. The Preparation of Butadiene by Catalytic Hydrogenation Of Monovinylacetylene in the Gaseous Phase
Abstract Of the various technical methods for the preparation of butadiene from monovinylacetylene, the present authors chose to make first of all a thorough investigation of the continuous hydrogenation process, utilizing gaseous monovinylacetylene with various catalysts. As a result of this work the following conclusions were reached. The chief fault of this continuous hydrogenation process lies in the fact that, in addition to butadiene, large quantities of butene and oily polymerization products of monovinylacetylene are formed, as a result of which the yield of butadiene is small. This disadvantageous course of the reaction is attributable to the great heat of reaction which is evolved locally on the surface of the catalyst. In the experiments carried out by the present authors, the chief efforts were directed toward overcoming this drawback. As may be seen in Table II, a series of experiments were carried out with palladium as catalyst, which was used with excess carrier having a low heat conductivity, e. g., diatomaceous earth and Japanese acidic earth. This catalyst was expected to have a weakening effect on the activity, for this effect is very pronounced in the hydrogenation of acetylene to ethylene. In the present case, however, the results were unsatisfactory; dilution of the reaction gas with water vapor, a change in the gas current, and a change in the proportion of hydrogen to monovinylacetylene, were all tried. The maximum yield of butadiene at 80° C was 33.7 per cent, based on the monovinylacetylene.