Abstract: The proposed method comprises passing the hydrodynamic flow of liquid hydrocarbons through a flow-through passage accomodating a baffle body providing for a local constriction of the flow; establishing the local flow constriction on at least one portion of the flow-through passage whose cross-sectional profile area is so selected as to maintain such a velocity of the flow on the portion of the passage that promotes the development of a hydrodynamic cavitation field past the baffle body having the degree of cavitation of at least one; processing the flow of a mixture of liquid hydrocarbons in the hydrodynamic cavitation field to initiate chemical transformations of liquid hydrocarbons resulting in a change in the qualitative and quantitative composition of the mixture of liquid hydrocarbons.

Abstract: A method and apparatus for conducting sonochemical reactions and processes using in large scales liquid medium volumes is disclosed which passes a hydrodynamic liquid flow at a velocity through a flow through channel internally containing at least one element to produce a local constriction of the hydrodynamic liquid flow. The velocity of the liquid flow in the local constriction is at least 16 m/sec. A hydrodynamic cavitation cavern is created down stream of the local constriction, thereby generating cavitation bubbles. The cavitation bubbles are shifted with the liquid flow to an outlet from the flow through channel and the static pressure of the liquid flow is increased to at least 0.85 kg/cm.sup.2. The cavitation bubbles are then collapsed in the elevated static pressure zone, thereby initiating the sonochemical reactions and processes.

Abstract: A method of and an apparatus for producing ultra-thin emulsions and dispersions is disclosed. The method includes the steps of passing a hydrodynamic liquid flow containing dispersed components through a flow-through channel having at least one nozzle and a buffer channel and directing a primary liquid jet from the nozzle into the buffer channel, thereby creating a secondary liquid jet in the buffer channel directed toward the nozzle. The primary liquid jet and the secondary liquid jet create a high intensity vortex contact layer that creates collapsing cavitation caverns and cavitation bubbles in the high intensity vortex contact layer. Ultra-thin emulsions and dispersions are formed under the influence of the collapsing cavitation caverns and cavitation bubbles. The apparatus includes a flow-through channel having an inlet and an outlet and a nozzle located inside the flow-through channel between the inlet and the outlet and having an orifice.