| 摘要 |
FIELD: technological processes. ^ SUBSTANCE: method is intended for realisation of reactions of olefins, dienes, styrene, aromatic compounds hydrogenation, and also in reactions of oxidation, nitration, amination, sulfonation, cyanidation, chlorination, fluoridation. Bulk catalyst is installed in reactor in single or several tiers. Gas and liquid are supplied into capillary channels, and gas is additionally supplied between tiers. Gas and liquid flows are set so that capillary number does not exceed critical capillary number that depends on Bond number, with account of angle gamma cosine between vector of two-phase mixture speed in capillary Us and vector of free fall acceleration g. ^ EFFECT: higher efficiency of mass exchanged and reaction processes and facilitation of technological process control and control of its parameters. ^ 6 dwg, 4 ex, 1 tbl |
