| 摘要 |
Sulphur trioxide is produced by contacting a mixture of sulphur dioxide and a gas containing free oxygen with a catalyst comprising oxides of vanadium, potassium, and silicon, the molar ratio of K2O : V2O5 being from 4.5 : 1 to 6 : 1 and the reaction being initiated at a temperature within the range of 380 DEG to 400 DEG C. At temperatures of 380 DEG , 390 DEG , and 400 DEG , the optimum K2O : V2O5 ratios are 5.4 : 1, 5 : 1, and 4.5 : respectively. The oxides of vanadium, potassium, and silicon may be present in combination, e.g. as potassium silicate or potassium vanadate. The catalyst is prepared by adding potassium silicate solution to dilute sulphuric acid, at a pH not greater than 4, to form a silica sol, mixing the sol with a soluble vanadium compound and coprecipitating silica and an insoluble vanadium compound by the addition of ammonia. Suitable soluble vanadium compounds are vanadyl sulphate, vanadyl chloride, vanadyl oxalate, and ammonium vanadate. The reactant concentrations are preferably controlled to give a gel product free from supernatant liquid. A preferred vanadium content is 6-7.5 per cent by weight, as V2O5. The catalyst may contain an inert filler, such as kieselguhr, in an amount of up to 50 per cent by weight. The oxidation process may be carried out in three successive reaction zones, the inlet temperature to each zone being, for example, 380 DEG C. and the outlet temperature from the third zone 410 DEG C. The composition of the catalyst may vary throughout each bed, but especially the third bed, so as to give maximum conversion at all parts of the bed. Specification 705,615 is referred to. |
