A new combination packing, which consists of bundles of structured packing and spacers, and which itself is conjoined to the elements of packed film and film-drop assemblies, is examined. The heat-and mass-exchange efficiency, and the dependence of the hydraulic resistance of the new packing on the velocity of the air flow are cited for various irrigation densities.Efficiency of heat and mass exchange with direct contact between the liquid and gaseous phases is ensured, above all, by the developed surface of their contact, which can be created by a packed assembly. Interaction between the phases may be film, film-drop, drop, or jet-drop in nature depending on the type of packed assembly [1][2][3]. A multitude of new types of packings, among which structured packings classed with the family of packed film assemblies, have come into the most widespread use in the past 15 years.Structured packings (SP) are regular packings represented as bundles assembled from flat or crimped sheets, which form a three-dimensional multichannel structure. The sheet components of the packing, which are fashioned from metallic foil, meshes, and polymeric, ceramic, and other materials, may be arranged in a vessel as a set of plates, spirals, cylinders, and may also be assembled into a honeycomb or cellular structure. Coaxial channels, which are formed by the packing elements, may assume different configurations -from simple (a circular or polygonal section) to complex three-dimensional [4].The term structured packings has also been expanded to include film heat-exchange contact assemblies for cooling towers (sprinklers) [5].Despite their high heat-and mass-exchange efficiency, SP have a number of deficiencies, primary among which is nonuniform distribution of the gaseous and liquid flows throughout the cross section of the vessel [1], since the geometric structure of the packing excludes communication between the free channels formed by neighboring sheets. To improve the operating efficiency of SP, it is necessary to ensure uniformity of gas and liquid throughout all channels, even at the inlet to a layer of packing. It is possible to organize sufficiently uniform distribution of flows, however, only on relatively small mock-up installations with a column vessel and in the presence of a liquid distributor, which ensures uniform irrigation over its entire cross section. In practice, it is virtually impossible to provide ideal irrigation of the entire surface of SP in industrial vessels, especially such large-scale vessels as cooling towers.Packings that organize the drop surface of phase contact are distinguished by an appreciably smaller specific surface as compared with packed film assemblies, and, consequently, also by low efficiency [1], although they provide free commu-