The kinetics of bitumen (asphalt), oil, and residual fuel oil extraction from oil sands by ultrasonic treatment has been studied. The influence of the working temperature of the process, characteristics of the separated components, fineness of the solid phase, and additive concentration on the extraction rate has been investigated. A schematic diagram of the installation for oil sands processing using an ultrasonic reactor is given. It is shown that ultrasonic devices could be an alternative to the presently used industrial equipment for bitumen and oil products extraction from oil-bearing rocks and oil sludge.Modern technologies for processing oil-bearing soils and rocks (oil sands and soils contaminated as a result of technological mishaps) are based on integrated use of hydromechanical, heat and mass exchange, and chemical processes [1-4]. Powerful ultrasound markedly intensifies these processes upon combined use, causes cavitation and heating up of water-pulped inhomogeneous systems, to which reagents are added, activates chemical and accelerates mass exchange processes. Under the impact of pulsating cavitation bubbles and shock waves, the aggregates of the solid phase break up, erosion and cracks appear in the contaminant films sticking to the particles, and they separate in layers. Through the cracks the leaching solution containing surface active agents formed as a result of sonochemical reactions of the components of the oil products and reagents may infiltrate into the originally closed pores under the action of capillary forces intensified by ultrasonic effect [5][6][7].The efficiency of oil sand processing using ultrasonic effect was assessed in the course of laboratory experiments on specimens obtained from a field in Canada as well as on artificial model mixtures prepared from various fractions of river sand (average particle diameter d = 0.02-1 mm) with addition of 13-14 % (mass) of oil or residual fuel oil. Aqueous sodium silicate, carbonate, and hydroxide solutions with temperatures of 30-75°and a pH > 7 were used as the working dispersion medium.The experiments were performed in ultrasonic reactors or in baths. A schematic diagram of the experimental setup is shown in Fig. 1. Elastic vibrations were introduced into the working medium of the reactor 1 with the aid of a rod waveguide 2 whose working end diameter was 15 mm. The magnetostriction transducer 4 connected to a 1 kW generator 9 was used as the source of ultrasonic vibrations. The amplitude of radiator vibrations generated during ultrasonic processing was 5-10 µm at a frequency of 22 kHz.An electric heater 7 maintained the required temperature of the working medium. Upon completion of ultrasonic action, after brief settling, the separated products (oil products, clarified water, washed sand, etc.) were successively removed from the reactor. In the course of the study of the kinetics of oil products yield, the floated-up drops were collected periodically. To get data for balance calculations, the sand and oil products were dewatered and wei...