This invention relates to fluid cavitation processing methods, and more specifically, to cavitation processing of fluids having specific content of water or other liquid phase exceeding 30-35% of the total weight. Different fluid media placed in individual cells in a single processing bath may be exposed to simultaneous processing.
One known method and apparatus for simultaneous collagen processing is taught in CA2025833 dated 22 Mar. 1991. This reference requires placing collagen vials (syringes) in a fluid-filled bath with its bottom ultrasonically vibrated at the frequency ranged within −20 kHz to 3 MHz. Specific, well-developed acoustic cavitation is produced within every cell exposed to processing. A drawback of this method is that fluid cannot be equally processed at different frequencies, since a fluid level in the bath depends on cell volumes used for processing, but not on the length of ultrasonic waves in fluid. Besides, a few frequencies only can define specific elastic properties of the bath bottom under vibration due to rather effective ultrasonic wave excitation in bath fluid. Only the first two/three natural vibration harmonics are available. Thus, as applied to the cells placed in process fluid, cavitation processing efficiency is significantly reduced.
Another prior art describes a method for measuring biological tissue radiation parameters: patent JP 6207893 dated 26 Jul. 1994.
In this method, the cells, under measurement, are placed in a vessel filled with process fluid. The fluid is then processed by ultrasonic acoustic waves excited from below through ultrasonic vibration tools immersed in the process fluid.
The cells that processed tissues are placed in are made of materials having an acoustic resistance close to that of the process fluid. Thus, developed acoustic cavitation conditions are produced not only in the process fluid, but also inside the fluid cells where processed tissues are placed. Similar to CA 2025833, this invention is disadvantaged by its dependence of cavitation processing efficiency on the level of the process fluid.
Should a fluid level fail to be a multiple of one fourth of the acoustic wave length, a complex superposition of incident and reflected waves will be formed under surface reflection. As a result, optimal conditions of cavitation bubbling dynamics is inevitably changed cavitation effect is reduced.
Cosmetic emulsion production method (Pat RU 2427362 dated 8 Sep. 2010) also teaches a cavitation process. The acoustic cavitation conditions described in this method are formed under a double resonance effect and configured to occur inside the flowing mechanical vibratory system—a channel on opposite sides of which in-phase sound vibration and a standing wave are generated at fundamental harmonic frequency. This in turn forms a quasi-plane standing wave in moving processed medium at a gap between the channel walls, wherein width of the channel gap is a multiple of one fourth of the wavelength excited by the channel walls. As a result, a specific high-intensity acoustic wave is formed in the processed fluid at the same resonance frequency. Drawbacks of this method are that several cells having different contents cannot be processed simultaneously.
Further, it is known that cavitation processes performed simultaneously at two different frequencies have a much larger synergetic effect than that produced serially at the both frequencies.
It is an object of this invention to provide a technique for simultaneous processing of several fluid-filled cells that may have several and single low-volume ingredient contents. Another object of this invention is to provide a method and system for processing these contents under the simultaneous effect of several resonant acoustic waves.
This object is achieved by using a square or rectangular bath filled with a process fluid where a standing acoustic wave is produced and reflected from the bath walls and bottom. These walls are designed as elastic membranes to have self-resonant first-harmonic resonance frequency where the opposite square bath walls may have either equal or different first-harmonic frequencies. Length “a” and width “b” of the bath are selected as multiples of one fourth of the wavelength excited within process fluid by the lateral bath walls:
a=(k/4)*(c/fi),
b=(k/4)*(c/fi),
where “c” is acoustic speed rated within process fluid, m/s;
The height of process fluid level “h” is specified as a multiple of one fourth of the bath bottom-excited wavelength, wherein vibration frequencies “fi” are rated by a cross-multiple factor “k”.
This invention relates to fluid cavitation processing methods, and more specifically, to cavitation processing of fluids that have specific content of water or other liquid phase exceeding 30-35% of the total weight. Different fluid media placed in individual cells may be exposed to simultaneous processing.
This method is intended for effective and simultaneous processing of various or identical compositions of fluid media. Particularly, this method may be successfully applied for preparation of individual submicron-sized disperse-phase cosmetic products.
The method for ultrasonically and simultaneously induced cavitation processing of fluid media-filled cells contemplated herein requires placing of cells in a bath filled with process fluid. The fluid cell material exhibits specific acoustic resistance to be equal or close to that of the process fluid. Sufficient acoustic wave amplitude is produced for specific process fluid such that well-developed acoustic cavitation occurs in the process fluid and every cell placed within the bath exposed to processing. The process fluid bath vessel has a rectangular or square form where an acoustic standing wave is produced in the process fluid and is reflected from the bath walls and bottom. The walls and bottom are designed as elastic membranes to have self-resonant first harmonic frequency. The bath vessel's opposite walls may exhibit both equal and different first harmonic frequencies.
Turning now to
The rate of polyethylene acoustic resistance (density: 0.92-0.94 g/cm3, longitudinal wave speed: ˜1900-1950 m/s) is approximately equal to the resistance of water selected for process fluid. As such, polyethylene is a good option for cell material. However, it should be understood that any similar material may be used without straying from the scope of this invention.
Concerning the opposite bath walls generating different frequencies, it is a matter of a problematic nature. In one embodiment, a membrane wall may be reinforced with ribs and have an area less than that of the bath wall—for the technique of implementation, refer to
To achieve the highest cavitation and collateral resonance effects, a standing acoustic wave with selected frequencies “fi” must be produced in a cell 3 filled with the fluid media for processing. For these effects, internal bath dimensions must be multiples of one fourth of the wavelength excited in the fluid 2 between lateral walls of the bath. Matching of standing wave nodes and loops is secondly conditioned by cross-multiplicity of frequencies “fi”. Height of process fluid level “h” is specified as a multiple of one fourth of the bath vessel bottom-excited wavelength.
The total fluid double resonant effect produced by processing of fluid cells may be specifically utilized for preparation of small amounts of cosmetic emulsions intended for individual types of a customer skin. Specific cream structure and phospholipid-based (liquid crystals) microphotography obtained by means of polarizing microscope using Maruzen Pharm's formulation is demonstrated in
Similar results have been obtained using this method on processing suspensions, in particular chalk dental pastes, using SPLAT's formulation.
Hence, accomplishment of the object and commercial capabilites of this invention are duly acknowledged.
Number | Date | Country | Kind |
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2012120584 | May 2012 | RU | national |
This application is a continuation utility patent application which claims the benefit to and priority from International Patent Application number PCT/RU2012/000552 filed on Jul. 9, 2012, which in turn claims priority to Russian Patent Application number RU2012/120584 filed on May 21, 2012.
Number | Date | Country | |
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Parent | PCT/RU2012/000552 | Jul 2012 | US |
Child | 14454066 | US |