A device for generating foam by the Venturi effect mixes liquid and gaseous phases. The device has a liquid insertion nozzle on the same axis as a Venturi stage having a converging portion disposed facing the nozzle, a throat of diameter "D", and a gas inlet coaxial with the nozzle and in communication with the converging portion. In operation, the gas is sucked in by the Venturi effect and directed towards a mixing chamber connected to a foam outlet. Mixing between the two phases takes place in a free jet, and the diverging portion of the Venturi has at least three zones of progressive cone angles, with discontinuities between the zones giving rise to a cavitation phenomenon, and opening out into a turbulent chamber.
A method for sanitizing a food processing environment includes preparing an ozonated foam sanitizing medium and applying the sanitizing medium to either objects in the food processing environment, such as food processing equipment, food contact surfaces, interior surfaces of the food processing facility, or the ambient environment within the food processing facility, or both the objects within the food processing facility and the ambient environment of the food processing facility. An ozonated foam sanitizing medium includes a foaming agent dissolved in an aqueous solution and an ozone concentration of at least about 0.1 ppm and is prepared by either injecting gaseous ozone or introducing an aqueous ozone solution into an aqueous solution containing a foaming agent. In a system for generating the ozonated foam medium, the gaseous ozone can be injected with a feed gas, such as oxygen, air, an inert gas, and mixtures thereof. Additionally, an inert gas, such as nitrogen, carbon dioxide, argon, krypton, xenon, neon, and mixtures thereof can be injected separately into the aqueous foam solution. Once prepared, the ozonated foam is applied to a surface within the food-processing environment to a thickness of about 0.25 inches to about 7 inches or more, and allowed to stand for a predetermined period of time. The ozonated foam is then washed away with an aqueous solution.
A liquid sprayer includes a casing (1) having a flow-through channel composed of sequentially joined inlet portion (2) formed as a converging tube, a cylindrical portion (3) and an outlet portion (4) formed as a conical diffuser. A length of cylindrical portion (3) is not less than a radius thereof. A cone angle of the diffuser forming the outlet portion (4) of the flow-through channel is greater than a cone angle of the converging tube forming the inlet portion (2) of the same channel. Alternatively, the converging tube forming the inlet portion of the flow-through channel is made conoid-shaped. Implementation of the liquid sprayer allows steady-state fine-dispersed liquid flow to be generated at the minimal energy consumption.
A low pressure foaming nozzle assembly having a modular construction for permitting the ready interchange of nozzle tips. The foaming nozzle assembly may be constructed of two pieces, with a first configuration employing a flow body and an engaging nozzle tip and a second configuration employing a pair of mating halves, wherein each mating half includes a portion of a venturi, a throat and a nozzle tip. The assembly cooperatively engages a foaming liquid source such as a wand, and upon pressure on the foaming liquid source, a foam is generated.
A liquid feed line includes a stepped internal nozzle and an exit diameter smaller than the diameter of the liquid feed line. The stepped internal nozzle desirably introduces hydrodynamics or hydraulic waves for the fluid, with the number of steps selected based on the pressure of the motive flow. By limiting the length of the stepped internal nozzle cylinder, a desirable splayed liquid stream is formed within a mixing chamber in fluid communication with a vent line. An exit cylinder in fluid communication with the mixing chamber includes a channel through which an aerated liquid stream of fluid passes. The entrance and exit faces forming the channel are substantially perpendicular to the fluid flow with the channel having a generally uniform dimension, neither converging nor diverging, and a diameter 1 to 10 times greater, depending on the pressure of the motive flow, than the exit to the internal nozzle.
Air is mixed with water passing through a liquid feed line. An internal nozzle carried within the feed line includes an exit diameter smaller than the diameter of the feed line for creating a liquid stream for mixing with air from a vent line directed into a mixing chamber within the feed line. Through the force of the nozzle, the aerated water is focused into an exit channel having a flat entrance face and an exit bore diameter greater than that of the internal nozzle.