Not applicable
Not applicable
Not applicable
1. Field of the Invention
The present disclosure relates generally to nozzle assemblies for liquid dispensers and, more particularly, to nozzle assemblies capable of producing different liquid output patterns.
2. Description of the Background of the Invention
Liquid dispensers can take on various general forms, e.g., trigger sprayers, finger type pumps, aerosol dispensers, etc. Further, nozzle assemblies can be coupled to such liquid sprayers to project different liquid output patterns, e.g., a stream, a divergent or conical spray pattern, aerated foam, and the like. The design of such nozzle assemblies generally depends on the intended application and/or the characteristics of the liquid that is dispensed.
For example, if the liquid is intended to be suspended in the air, a nozzle assembly to project a divergent spray may be used, but if the liquid is intended to be applied to a surface, e.g., carpet, wood, a painted surface, etc., a nozzle assembly to project a stream or foam may be used.
Nozzle assemblies that are designed to project a divergent spray typically include a swirl chamber that is directly upstream from an exit orifice. In a typical swirl chamber, a vortex is created in the chamber by restricting the liquid to enter the chamber through one or more generally tangential paths before exiting through the exit orifice. Such tangential paths include obstructions that substantially block direct radial flow paths to the exit orifice. In contrast, if a stream pattern is desired, the fluid is allowed to flow through a substantially direct radial flow path to the exit orifice.
According to one embodiment, a nozzle assembly for a liquid dispenser includes an outlet member that defines a liquid supply conduit and a nozzle that includes an exit orifice extending therethrough, wherein the nozzle is disposed over an end of the outlet member. A liquid compression path is defined by the nozzle and the outlet member, wherein the liquid compression path includes a liquid compression chamber that supplies liquid from the liquid supply conduit to the exit orifice. The nozzle is adjustable between a first spray position for projecting a liquid spray having a first average droplet size and a second spray position for projecting a liquid spray having a second average droplet size greater than the first average droplet size. In the first spray position the liquid compression chamber has a first volume and in the second spray position the liquid compression chamber has a second volume larger than the first volume. The liquid spray is formed without a swirl chamber directly upstream from the exit orifice.
According to another embodiment, a method of using a single adjustable nozzle assembly for broadcasting a liquid as a first liquid spray output having a first average droplet diameter size into the air with minimal liquid droplet fallout and for applying the liquid as a second liquid spray output having a second average droplet diameter size onto a surface includes the step of providing a single adjustable nozzle assembly. The nozzle assembly defines a discrete first liquid compression path and a discrete second liquid compression path and does not provide a continuously variable adjustment between the first and second liquid compression paths. The method also includes the steps of adjusting the nozzle assembly to form the first liquid compression path, pumping a liquid through the first liquid compression path, generating a first liquid spray output from the nozzle assembly, wherein the first liquid spray has an average droplet diameter size selected to minimize droplet fallout onto surrounding surfaces by ensuring substantial evaporation into surrounding air, and directing the first liquid spray output into the surrounding air in a manner selected to allow substantially complete evaporation of the first liquid spray output before encountering the surrounding surfaces. Further, the method includes the steps of adjusting the nozzle assembly to form the second liquid compression path, pumping the liquid through the second liquid compression path, generating a second liquid spray output from the nozzle assembly that has an average droplet diameter size at least about double an average droplet size of the first liquid spay output, and directing the second liquid spray output against a surface.
According to yet another embodiment, a nozzle assembly for a liquid dispenser includes an outlet member that defines a liquid supply conduit and a nozzle that includes an exit orifice, wherein the nozzle is disposed over an end of the outlet member. A liquid compression path is defined between the nozzle and the outlet member, wherein the liquid compression path includes a liquid compression chamber that supplies liquid from the liquid supply conduit to the exit orifice. The liquid compression chamber is directly upstream of the exit orifice and provides a substantially unobstructed direct radial flow path to the exit orifice. The nozzle is adjustable between a first spray position for projecting a divergent liquid spray having a first average droplet size and a second spray position for projecting a divergent liquid spray having a second average droplet size greater than the first average droplet size. The first average droplet size is between about 40 micrometers and about 60 micrometers and the second average droplet size is between about 90 micrometers and about 120 micrometers.
Other aspects and advantages of the present invention will become apparent upon consideration of the following detailed description.
The present disclosure is directed to a nozzle assembly that can be coupled to a dispensing end of a liquid dispenser, such as a trigger sprayer, finger type pump, aerosol dispenser, and the like. The nozzle assembly is adjustable between various functional positions or settings to project different liquid output patterns. Preferably, the nozzle assembly is adapted to project different divergent or conical spray outputs with a spray cone angle from between about 5 degrees to about 90 degrees and the spray outputs have average liquid droplet sizes that are less than about 120 microns. Such spray outputs are distinguishable from foaming output patterns, non-divergent stream patterns, and divergent stream patterns. Further, prior art nozzle assembles that generate a divergent spray commonly include a swirl chamber directly upstream of an exit orifice. The typical swirl chamber generally restricts the flow of a liquid to a tangential path directly upstream from the exit orifice in order to produce a vortex of fluid entering the exit orifice to subsequently create the divergent spray. In contrast, the present nozzle assembly, in some instances, generates divergent spray outputs without creating a vortex with a swirl chamber directly upstream of an exit orifice. Rather, such nozzle assemblies disclosed herein include a substantially unobstructed direct radial flow path to the exit orifice to produce a divergent spray without creating a vortex. Still further, the present nozzle assembly preferably can be adjusted between at least two different settings in order to generate divergent spray outputs having different average liquid droplet sizes by varying the size of a liquid compression chamber that is directly upstream from an exit orifice. In one example, the nozzle assembly is adjustable between first and second discrete spray positions to generate specific spray outputs with distinct average droplet sizes. The discrete spray positions prevent the nozzle assembly from providing a continuously variable adjustment between the first and second spray positions. However, in other examples, the nozzle assembly is adjustable between a plurality of spray positions that can be discrete or continuous or any combination of discrete and continuous. As used herein, a discrete spray position is a single position and is not continuously variable between an infinite number of intermediate spray positions.
In yet another example, the nozzle assemblies disclosed herein are adapted for use with a liquid, such as an air freshener, deodorizer, cleaning agent, and any combination of the like, that has intended uses when dispensed as a first divergent spray that suspends in the air and when dispensed as a second divergent spray that is applied to a surface. In such applications, the first and second divergent sprays should provide a generally even dispersion of the liquid and it may be useful to have divergent spray patterns with different average droplet sizes. For example, the first divergent spray can have a smaller average droplet size to suspend an aerosol-like spray into the air with minimal liquid droplet fallout. Droplet fallout describes the action of having, for example, aerosolized liquid particles fall from the surrounding air environment onto surrounding surfaces, such as a floor or furniture, before completely or substantially evaporating into the air, which can cause the surfaces to feel wet to the touch and may be undesirable to a user. The smaller average droplet size of the first divergent spray promotes the substantially complete evaporation of the liquid before encountering an object when directed into the air away from any obstructing objects. Thus, the first divergent spray is particularly suited for dispensing the liquid as an air freshener that substantially completely evaporates into the air to provide a longer lasting ambient effect. However, as would be understood by one of skill in the art, some components of the liquid may not completely evaporate into the air. Instead, such non-evaporating components generally break down into even smaller particle sizes as the other evaporating components of the liquid do evaporate. The smaller particle sizes of the non-evaporating components are normally sufficiently small so that they do not contribute to any noticeable undesirable effects to a user.
Further, the second divergent spray can have a larger average droplet size to provide a targeted application of the liquid to a surface for a specific purpose, e.g., as a deodorizer or cleaning agent. In one non-limiting example, the second average droplet spray can be applied to a stain on a fabric, wherein the larger average droplet size allows the liquid to be applied directly to the surface without substantial evaporation of the liquid and to penetrate the stain to provide a more effective deodorizing or cleaning function. In one example, the second divergent spray applied to a surface preferably has a generally conical spray geometry with a diameter at a surface between about 6 inches (about 15 cm) and about 14 inches (about 36 cm) when generated between about 10 inches (about 25 cm) and about 18 inches (about 46 cm) from the surface to which it is being applied. In another example, the second divergent spray has a generally conical spray geometry with a diameter at a surface of about 10 inches (about 25 cm) when generated at about 14 inches (about 36 cm) from the surface to which it is being applied. Such spray geometries in terms of shape, size, and distance from a surface have been found to apply the liquid to the surface in an optimal and even manner.
In one preferred example, the larger and smaller average droplet diameter sizes are generally less than about 120 microns and the larger average droplet diameter size is approximately double the smaller average droplet diameter size. Preferably, the larger average droplet size is generally between about 90 microns to about 120 microns and the smaller average droplet size is generally between about 40 microns to about 60 microns. In yet a further example, the larger average droplet size is about 100 microns and the smaller average droplet size is about 40 microns. Such average droplet sizes can be measured using any suitable particle analyzer, such as a Mastersizer particle analyzer manufactured by Malvern Instruments Ltd., of Worcestershire, UK.
At normal environmental conditions, e.g., room temperature and 50% relative humidity, and when the spray is projected from a typical trigger sprayer, droplet sizes between about 40 microns and about 60 microns will usually result in substantially complete evaporation of the liquid before encountering an object when directed into the air away from any obstructing objects. However, even at diameter sizes between about 40 microns and about 60 microns, some components of the liquid may not completely evaporate into the air. Instead, such non-evaporating components, such as surfactants, often shrink or break down into even smaller particle sizes as the other evaporating components of the liquid do evaporate. In one example, at normal environmental conditions, the non-evaporating components often may shrink or break down into particles of about 10-20 microns or smaller in average diameter within about 2-3 feet (about 0.5-1.0 meters) from the nozzle assembly. Such small particle sizes of the non-evaporating components generally do not contribute to any noticeable undesirable effects to a user.
Referring to
With additional reference to
The first and second exit orifices 56, 58 can be any size and shape but are generally cylindrical in the present non-limiting example. Further, the first and second exit orifices 56, 58 can be the same or different sizes and shapes. In the present example, the second exit orifice 58 is larger than the first exit orifice 56. More specifically, the second exit orifice 58 has a larger diameter than the first exit orifice 56. In one example, the second exit orifice 58 has a diameter that is between about 0.017 inches (about 0.44 mm) to about 0.021 inches (about 0.53 mm) and the first exit orifice 56 has a diameter that is about 0.013 inches (about 0.33 mm) to about 0.017 inches (about 0.44 mm). In another example, the second exit orifice 58 has a diameter that is about 0.019 inches (about 0.48 mm) and the first exit orifice 56 has a diameter that is about 0.015 inches (about 0.38 mm). Alternatively or in conjunction, the lengths of the first and second exit orifices 56, 58 can be varied. In one example, the lengths of the first and second exit orifices 56, 58 are between about 0.055 inches (about 1.40 mm) to about 0.035 inches (about 0.89 mm). In another example, the lengths of the first and second exit orifices 56, 58 are about 0.045 inches (about 1.14 mm).
Referring now to FIGS. 2 and 6-8, the preference valve 44 is a generally cylindrical member with an inlet end 80 and a discharge end 82. A planar, generally rectangular end wall 84 is disposed at the inlet end 80 and an outer tubular wall 86 extends from the end wall 84 to the discharge end 82. An inner tubular wall 88 is radially spaced within the outer tubular wall 86 and is connected thereto by an end wall 90 that extends therebetween. The end wall 90 is spaced from the discharge end 82 of the preference valve 44 to define a recessed channel 92. Radially opposed openings 94 are disposed through the inner tubular wall 88 proximate the discharge end 82. In other examples, the inner tubular wall 88 may include fewer or additional openings therethrough. Further, a hump or step 96 is disposed in the recessed channel 92 between a first side of the opposed openings 94. In the present example, the hump 96 is spaced generally half-way between the opposed openings 94. The hump 96 includes a planar top and there is a smooth, generally parabolic transition from the end wall 50 to a base and a top of the hump 96. However, in other examples, modifications can be made to the hump 96 without departing from the spirit of the present disclosure, such as modifying the hump 96 to include channels and/or cavities disposed therein (not shown).
The preference valve 44 further includes a wall 98 that is disposed between a second side of the opposed openings 94 diametrically opposite the recessed channel 92. In the present example, the wall 98 extends substantially between the opposed openings 94 and projects past ends of the outer and inner tubular walls 86, 88. The wall 98 functions to block an exit orifice that is not in use, as will be described in more detail hereinafter. Consequently, modifications to the wall 98 are contemplated that still allow the wall 98 to perform such function.
Referring more specifically to
In the present disclosure, the outlet member 46 generally defines a conduit that supplies liquid from the dispensing end of a liquid dispenser to a nozzle and out one or more exit orifices. By way of non-limiting example, FIGS. 2 and 9-12 illustrate the outlet member 46 with a discharge valve 130 disposed within a valve body 132 to define a liquid supply conduit. The discharge valve 130 includes a circular end wall 134, a rectangular column 136 extending from the end wall 134, and a generally cylindrical member 138 projecting axially from the rectangular column 136. Referring more particularly to
Referring to
In one non-limiting example of the nozzle assembly 40 in use, liquid flows through the aperture 166 in the base wall 160 of the valve body 132 and past a periphery of the end wall 134 of the discharge valve 130. The end wall 134 resiliently flexes toward the cylindrical member 138 to allow the liquid to pass and resiliently closes when there is no forward pressure on the end wall 134. In the present example, the discharge valve 130 and the end wall 134 function as a check valve that only allows liquid to flow in one direction through the nozzle assembly 40 and out an exit orifice. Referring to
The nozzle 42 is axially rotatable about the outer tubular wall 86 of the preference valve 44 between four successive functional positions: a first spray position, a first off position, a second spray position, and a second off position. In both off positions, as shown in
With the liquid passageways 104 opened, liquid flows therethrough into the recessed channel 92, over the hump 96, and out an exit orifice. In the first spray position shown in FIG. 13, for example, the first exit orifice 56 is aligned over the hump 96 and the second exit orifice 58 is aligned over the wall 98. Liquid flows only through the first exit orifice 56 while the second exit orifice 58 is blocked by the wall 98. In the second spray position shown in
More specifically, in the first spray position, a first liquid compression path is defined between the nozzle 42 and the preference valve 44. The first liquid compression path includes a first compression volume defined between the first exit orifice 56 and the hump 96. Similarly, in the second spray position, a second liquid compression path is defined between the nozzle 42 and the preference valve 44. The second liquid compression path includes a second compression volume defined between the second exit orifice 58 and the hump 96. The second compression volume is larger than the first compression volume because of the recess 68 in the end wall 50 of the nozzle 42 around the second exit orifice 58. Consequently, the second spray position projects a divergent spray pattern with droplets that have an average droplet size greater than in the first spray position.
In one example, the first and second spray positions produce sprays with an average droplet size generally less than about 120 microns and the average droplet size in the second spray position is approximately double the average droplet size in the first position. In another example, the second spray position produces a spray with an average droplet size generally between about 90 microns to about 120 microns and the first spray position produces a spray with an average droplet size generally between about 40 microns to about 60 microns. In yet a further example, the second spray position produces a spray with an average droplet size of about 100 microns and the first spray position produces a spray with an average droplet size of about 40 microns.
Another way to analyze the different spray positions of the nozzle assembly 40 is in terms of pressure drops and/or peak velocities associated with fluid flow through the nozzle assembly 40 in each of the spray positions. In one analysis, a steady flow of water at a flow rate between about 1-2 ml/sec, more specifically about 1.8 ml/sec, is simulated. Such a flow rate can be generated from a typical trigger sprayer, wherein a trigger pump stroke generates a flow of liquid having a volume of about 0.9 ml with a stroke time of about 0.5 seconds and an output of liquid between about 0.8 and 1.8 grams per trigger pump stroke. In the first spray position, the simulated flow of water is associated with a pressure drop between about 39-40 psi (about 269-276 kPa), more specifically about 39.1 psi (about 270 kPa), and has a peak velocity between about 22-23 m/s, more specifically about 22.8 m/s. In the second spray position, the simulated flow of water is associated with a pressure drop between about 15-16 psi (about 103-110 kPa), more specifically about 15.8 psi (about 109 kPa), and has a peak velocity between about 14-15 n/s, more specifically about 14.3 m/s. In this example, known computational fluid dynamics (“CFD”) methods can be applied to these different pressure drops and peak velocities to estimate average droplet sizes in the first and second spray positions. According to one CFD method, the first spray position generates an output with a sauter mean diameter of about 44 microns and a most probable droplet diameter of about 51 microns, and the second spray position generates an output with a sauter mean diameter of about 94 microns and a most probable droplet diameter of about 108 microns. The sauter mean diameter is the diameter of a drop whose ratio of volume to the surface area is the same as that of the entire spray.
In use, liquid flows through the aperture 166 in the base wall 160 of the valve body 132 and past an outer periphery of the discharge valve 130. Thereafter, the liquid flows through the channels 106 disposed in the inner tubular wall 88 and into the cavity 170. The nozzle assembly 200 of
With the liquid passageways 104 opened, liquid flows therethrough into the recessed channel 92 over the first or second humps 208, 210 and out the exit orifice 206. In the first spray position shown in
In one example, the first and second spray positions produce sprays with an average droplet size generally less than about 120 microns and the average droplet size in the second spray position is greater than the average droplet size in the first spray position.
In use, the nozzle 242 is axially disposed over and around the valve body 132 so that the first screw thread 256 engages the second screw thread 258 and the sleeve 252 is disposed over and around the generally cylindrical member 138 of the discharge valve 130. Fluid flows through the aperture 166 in the base wall 160 of the valve body 132 and past an outer periphery of the discharge valve 130. The nozzle assembly 240 is rotatable between at least three functional positions: a first spray position, a first off position, and a second spray position. Additional successive off and spray positions may be possible depending, in part, on the lengths of the screw threads 256, 258 and the lengths of the nozzle 242 and the sleeve 252. In the off position, the axial channels(s) 254 in the sleeve 252 are not aligned with the axial channel(s) 148 in the cylindrical member 138 to prevent liquid from flowing to the exit orifices 250. However, in the first and second spray positions the axial channel(s) 254 in the sleeve 252 are aligned with the axial channel(s) 148 in the cylindrical member 138 to allow liquid to flow past the central protrusion 248 and out the exit orifices 250.
By way of non-limiting example,
In one example, the first and second spray positions produce sprays with an average droplet size generally less than about 120 microns and the average droplet size in the second spray position is greater than the average droplet size in the first position.
In all of the embodiments disclosed herein, a swirl chamber is preferably not formed in both the first and second spray positions. However, in some embodiments a swirl chamber could be formed, if desired. Thus, nozzle assemblies that include a swirl chamber or other vortex inducing structure can fall within the scope of this disclosure.
Other embodiments that include all of the possible different and various combinations of the individual features of each of the foregoing described examples are specifically included herein.
Nozzle assemblies disclosed herein are adapted to generate different divergent liquid spray outputs that have average droplet sizes less than about 120 microns. The different divergent liquid spray outputs are suited for applications where a liquid is being suspended in the air and/or applied to a surface.
Numerous modifications to the present invention will be apparent to those skilled in the art in view of the foregoing description. Accordingly, this description is to be construed as illustrative only and is presented for the purpose of enabling those skilled in the art to make and use the invention and to teach the best mode of carrying out same. The exclusive rights to all modifications that come within the scope of the appended claims are reserved.