Abstract
The results of investigating the porous structure of oxide, reduced and sulphided forms of alumina-supported nickel molybdena catalysts are presented. Microdistribution of the pores was determined by low-temperature nitrogen adsorption, and macrodistribution was determined by mercury porosimetry. The changes in pore-size distribution of different forms of NiMo-Al 2O 3 catalyst are discussed in relation to the conditions of its activation.
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