This application is related to U.S. patent application Ser. No. 14/066,435, filed concurrently herewith, and entitled “METHODS AND SYSTEMS FOR CREATING AEROSOLS”.
Many manufacturing and industrial applications benefit from fluid atomization to create a fine vapor mist or aerosol, such as the fuel/air mixture used in combustion applications, atomized air-paint mixtures for spray painting, application of coatings to pharmaceuticals, adhesive applications, and the like. Once a component solution is made into an aerosol it can be readily processed to coat virtually any shaped surface. Alternatively, in the pharmaceutical industry, aerosols are commonly used in a process called “spray-drying” to create fine powders that serve as upstream component solutions to create active pharmaceutical ingredients.
In all known applications, creating the aerosol from a component solution is challenging. When the component solution behaves like a Newtonian fluid, the creation of a vapor or aerosol is accomplished by a number of conventional methods. One conventional method uses high velocity air flows to entrain air and liquid. A typical atomizer or aerosol involves the coaxial flow of air and component solution at large Reynolds and Weber numbers, i.e., the inertial forces dominate the viscous and surface tension forces in the fluid. Such flows are generally unstable and lead to fluid break-up by Kelvin-Helmholtz and Plateau-Rayleigh instabilities. In many instances, the flow is turbulent and chaotic, which strips and stretches the fluid parcels at high strain and strain rates, which leads to the entrainment of large amounts of air with the fluid and results in a fine mist of drops suspended in the air.
High velocity coaxial flows are effective when the component solution has Newtonian properties and behaves like a Newtonian fluid. However, many component solutions contain a variety of macromolecular and interacting solids components that lead to non-Newtonian properties, including shear-thinning and viscoelasticity. Conventional methods of atomization like high velocity coaxial flows and electrospray can be ineffective for component solutions that have non-Newtonian properties. For example, if a component solution is viscoelastic and strongly extensionally thickening, its extensional viscosity can increase by several orders of magnitude in the straining direction when the fluid is stretched, i.e., greater than 105 for some high molecular weight polymer component solutions.
During jetting, the extensional thickening of component solutions having non-Newtonian properties causes the viscous drag to overwhelm the inertial and surface tension forces, which allows the system to support large strain before breaking-up and preventing the formation of small drops. The jetting leads to the formation of long, sticky filaments, films, and tendrils that never break-up and become suspended in air. Essentially, the liquid stretches, but never breaks into droplets to form a mist or vapor.
The principal problem with coaxial flow systems to create aerosols is that the straining direction is coincident with the translation direction. The filament eventually breaks up into droplets to form a mist, but to achieve the large strain the filaments issuing from the jet must necessarily travel long distances. As the filaments travel, the filaments lose momentum and can recoil to reform large droplets. Alternatively, attempts to continually impel the filament during its trajectory require impractically long jetting to break the filaments and form droplets.
Therefore, methods and systems that create aerosols from fluids that show one or both of Newtonian and non-Newtonian properties would be beneficial in the art.
Systems and methods for creating aerosols are disclosed in which fluid filaments are stretched and break-up into droplets that create an aerosol, mist, or other vapor. Aerosols, mists, and vapors are interchangeable terms used to describe one or more droplets of fluid filaments that become suspended in air. The fluids are often liquids, having either Newtonian or non-Newtonian properties. Generally, fluids having non-Newtonian properties can have strong extensional thickening, which cause their extensional viscosity to increase significantly, sometimes several orders of magnitude, in the straining direction when strained. The extensional thickening of non-Newtonian fluids causes viscous drag that overwhelms the inertial and surface tension forces of the fluid and allows the system to support large strain before breaking-up and preventing the formation of small drops or droplets.
If strained and stretched enough along an appropriately long strain pathway, all fluids, including fluids having Newtonian and non-Newtonian properties, eventually break-up into small droplets and form a mist or aerosol. All fluids can be continually stretched to form fluid filaments (stretched fluid) until the fluid filaments break into several droplets thus forming a mist or aerosol.
The process of straining and stretching fluid filaments can be repeated with excess fluid remaining after the first round of droplets have been formed or with new fluid. Further, multiple fluid filaments can be stretched in parallel with the first fluid filament stretching and straining process thus increasing the volume of the formed droplets. The amount of time between stretching the first fluid filament and any additional excess fluid filaments can be defined by a time period that may be adjusted or controlled, as desired. The time periods between multiple stretching and breaking of fluid filaments can be variable or can be constant.
The nip 306 has an upstream side 310 and a downstream side 312. Fluid coating the roller(s) pools on the upstream side 310 of the nip 306. The fluid is drawn through the nip 306 to the downstream side 312 and stretched to form a fluid filament 308. The fluid filament 308 has a continuous and increasing strain applied to it on the downstream side, which causes the fluid filament 308 to grow longer and thinner as the strain is increased and the surfaces of the rollers 302, 304 are pulled farther apart. In the example shown in
In
Between the pair of counter-rotating rollers 402, 404 is a nip 406. In this example, the nip squeezes the fluid layers 412, 414 between the two rollers 402, 404 at a controlled fluid thickness. The controlled fluid thickness can be adjustable in some examples or can be fixed in other examples. Controlling the fluid thickness controls the volume of and manner in which the droplets 418 of the mist are formed on the downstream side of the nip 406. As discussed above regarding
As discussed above, when the rollers counter-rotate with respect to each other, the fluid coating one or both of the rollers is drawn into a nip defined between the rollers. The fluid filament stretches on a downstream side of the nip and breaks into droplets to form the mist on the downstream side of the nip. The fluid filament breaking into droplets flows in a direction that is away from the rollers themselves. A harvesting element can be positioned to collect mist that is formed by the fluid coating being drawn through the nip of the rollers. The mist is a collection of the droplets that are formed by the fluid filaments breaking.
The counter-rotation of the rollers 604, 610 draws fluid through a nip 608 formed between the top roller 604 and the bottom roller 610. The bottom roller 610 rotates in a clockwise motion, which thereby draws the fluid film through an upstream end of the nip 608. Air flow pathways 612, 614 on the downstream side of the nip 608 have a pathway that is parallel to the rotating motion of each respective roller, e.g., for the top, counter-clockwise rotating roller 604, the airflow pathway 612 is parallel to the counter-clockwise rotation of the top roller 604 and for the bottom, clockwise rotating roller 610, the airflow pathway 614 is parallel to the clockwise rotation of the bottom roller 610.
The nip 608 shown in the
Any suitable coating technique(s) can be used to apply fluid to the surface of a roller and the above discussed coating techniques are not designed to limit the disclosure in any way. For example, the fluid can be applied at any suitable angle and in any suitable location with respect to the roller(s). The fluid can be dripped on to one or both rollers or can be directly applied to the roller's surface. The fluid can be applied on the upstream or downstream side of the nip, although in the above examples, the rollers are round and any application of fluid on the downstream side of the nip coats the roller on the downstream side and the roller's rotation causes the fluid to enter the nip on the upstream side of the nip.
In
The texture and/or the treatment applied to the rollers can be selected based on the characteristics of the fluid that is aerosolized to customize the aerosol creation process to each fluid and provide the most efficient manner for aerosolizing the fluid among other reasons. In some examples, the textured surface of one or both of the rollers varies the thickness of the fluid coating that adheres to the surface of the roller. Such a textured surface can help vary the thickness of the fluid film in a manner that increases the efficiency of the fluid filament breaking into droplets by varying the concentration of the fluid in target regions.
The rollers can include any suitable materials such as steel or other metal(s), plastics, rubbers, or the like. The rollers or any portions thereof also can be a single material or may be any number of multiple materials. For example, a roller can have a core material that is coated with or includes a surface layer of a material that is softer than the core material. In some examples, the surface layer material encourages the fluid to adhere to the roller or may encourage the fluid to adhere to the roller at a different angle or in a different way than would occur without the surface layer material.
The orientation of the fluid source with respect to the rollers can be any desirable position. Some of the above examples discuss an air flow source that directs the droplets forming the mist or aerosol in a particular direction. The air flow source can be any gas source and is not limited to air. For example, the gas source can be positioned to cause gas to flow on either side of, above, or below the nip to encourage or cause the formation of droplets from breaking of the fluid filaments. Alternatively, the gas source can be positioned to cause gas to run through one or both rollers so the gas is expelled radially from the roller(s).
The formed mist can be directed to form an aerosol of various geometries. Any desirable geometrical shape can be formed, depending on how the mist is directed. The geometry can be any shape, such as a rectangle, cone, or conical shape and the size and contour of such shapes can be controlled by altering the volume and concentration of the aerosolized fluids.
It will be appreciated that variations of the above-disclosed systems and methods for creating aerosols and other features and functions, or alternatives thereof, may be desirably combined into many other different systems, methods, or applications. Also various presently unforeseen or unanticipated alternatives, modifications, variations, or improvements therein may be subsequently made by those skilled in the art.
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