Patent Application
20110168804
The invention relates to fluid feed systems for spray devices; in particular, to fluid feed systems utilising a porous medium to enable an electronic spray head to deliver consistent spray performance, regardless of the spray device orientation and the quantity of fluid remaining within the device's fluid reservoir.
As a result of both the increasing demand from consumers for additional ‘smart’ functionality in spray products, and the ever-growing pressure to eliminate the greenhouse gas propellants inherent to traditional aerosol can technology, alternatives to traditional spray technologies are being sought. This has led to rapid growth in the field of electronic spray technologies such as that disclosed in PCT/G B92/02262. These devices bring environmental benefits as they do not require propellants and, because the spray is electronically generated, they provide repeatable, controllable performance.
For many applications such electronic spray products can be required to deliver high flow rates, operate in multiple or all orientations, and operate with the spray head above the bulk of the fluid in the primary operating orientation. Further, such fluid feeds should ensure that almost all of the fluid initially contained within the product's fluid reservoir can be sprayed, i.e. minimise residual fluid when the product stops functioning at an acceptable level. The move towards more compact products drives the fluid feed system to be space-efficient and, finally, a requirement on the user to prime the spray product manually should be avoided as this reduces the product's consumer appeal and the repeatability of the spray.
Thus there is a requirement for fluid feed designs which can deliver high flow rates in many or all orientations to such electronic spray heads that do not require a priming operation and that minimise un-sprayable residual fluid.
Many examples of fluid feed systems for spray devices are known in the art. For example, dip tubes are commonly used in manually pumped spray heads, for example U.S. Pat. No. 5,518,150 and U.S. Pat. No. 6,202,943. Dip tubes are also used in highly pressurised reservoirs for aerosol type applications as disclosed in U.S. Pat. No. 4,966,313. However such systems are not in general suitable for feeding electronic spray heads. Electronic spray heads generally will not pump air: if air gets into the dip tube then the device may fail.
To counter this problem porous media, generally in the form of wicks, have been used to deliver air-freshener formulations to electronic spray heads for example EP1159078 and PCT/GB92/02262. An advantage of these systems is that they can be self-priming, but a related drawback of these systems is that they can deliver only relatively low flow-rates and are generally restricted in the range of orientations in which they operate effectively.
A mechanically operated suction pump has been used to draw fluid against gravity to deliver it to an electronic spray head, as described in WO9729851. This approach enables the fluid to be drawn up to the electronic spray head in bulk, thereby enabling the desired high flow-rates to be achieved; however a drawback related to these systems is that they require a manual priming operation.
The prior art has attempted to overcome some of the drawbacks of these systems by the use of sponge-filled reservoirs for fluid delivery to an electronic spray head in WO06066671 and PCT/GB92/02262. Such systems can help to increase the range of orientations in which the spray can operate, but suffer from a degradation of spray delivery with time as the amount of fluid in the reservoir reduces, and these systems tend to result in a high level of residual fluid remaining in the sponge which cannot be dispensed.
The present invention is concerned typically with the field of fluid feed systems for electronic spray heads that consist of a reservoir containing fluid, together with a fluid transport element composed of a porous medium. When the reservoir is full, the porous medium is saturated with fluid and free fluid fills at least some of the space in the reservoir outside of the porous medium. As the reservoir empties, the free fluid may be replaced by air, or the reservoir volume may reduce, while the porous medium remains largely saturated with fluid. Finally, once all free fluid is exhausted, fluid is drawn out of the porous medium and air is ingested into the porous medium to replace it.
It is well known in the art to use a porous medium to transport fluid from a reservoir to an electronic spray head and a basic system suited to this is shown in
When the fluid reservoir 10 is not able to collapse as fluid is expelled from it, the fluid that is sprayed out must be replaced by the same volume of air, or some other immiscible fluid. A separate air inlet path 11 may be provided for this air to enter the reservoir but, for cost reduction or technical reasons, it may alternatively enter the reservoir through holes in the electronic spray head 16 itself. Further, when delivering fluid at high flow rates, nozzle-based spray heads may pump air back into the reservoir regardless of whether a separate air inlet path exists. This pumping of air into the reservoir can also occur even when the reservoir is collapsible and there is no differential pressure across the spray head. Any air that enters the reservoir through the spray head in this way has the potential to block the supply of fluid to the spray head. A fluid feed and reservoir system according to the present invention seeks to manage the flow of such incoming air to avoid blocking of the fluid feed to the spray head by air ingested through the spray head.
As the fluid in the reservoir is expelled and replaced by air, the pressure behind the spray head may change. The feed system needs to support this change. In particular, the feed system needs to continue to deliver fluid to the head when the fluid level in the reservoir is gravitationally below the level of the head. This is commonly achieved through the use of a homogeneous (but not necessarily isotropic) porous medium 15 that has pores small enough to support the required fluid rise height. By “homogeneous”, we mean that the medium has uniform properties throughout its bulk when considered on a macroscopic scale (as distinguished from the microscopic pore-size scale). By “isotropic”, we mean that the medium has the same physical structure and properties in all directions. For example, a fibre wick is usually homogeneous, but not isotropic and open cell reticulated foam is usually homogeneous and isotropic.
Different arrangements of the reservoir 10 and spray head 16 may give rise to different required rise heights required of porous medium 15. The relationship between maximum rise height and effective pore size is described by Equation 1 later in this specification. It shows that, for a fluid of given density and surface tension, as the required maximum rise height as measured from the bottom of reservoir 10 to the spray head 16 increases, the effective pore size in the entire medium must be reduced. However, as the effective pore size is reduced, the permeability of the medium generally also reduces, resistance to flow increases and this leads to a limit on the flow rate that can be achieved. Further, a spray head must work harder to draw fluid through a low-permeability medium. For portable electronic spray applications in particular, this can increase the cost of drive electronics and reduce battery and spray head life.
The present invention therefore seeks to provide a fluid feed and reservoir system capable of generating a sufficient fluid rise height, in combination with an improved permeability of the porous medium, which combination of properties allows higher flow rates to be achieved by the spray head being fed. The present invention further seeks to improve the performance of the fluid feed system by providing improved means of encouraging the displacement of air ingested into the porous medium such that fluidic pathways are less at risk from being broken down by air ingested into the porous medium.
In any dispensing system using porous media fluid feeds, air may be ingested into the porous medium either from the free space in the reservoir, via the spray head, or via both of these routes.
Air may be ingested into the porous medium via the spray head regardless of the fluid level in the reservoir, and can cause the fluidic pathways in the medium to break down. This can cause a reduction in the flow rate achieved, as increasing numbers of pathways within the medium break down as more air is ingested. It is therefore advantageous to encourage any air ingested via the spray head to move away from the vicinity of the spray head, leaving fluidic pathways to the spray head intact, yet none of the prior art makes specific provision for the removal of air from the porous medium.
Providing a pore size gradient in the porous medium can encourage ingested air to move away from the spray head. Providing ingested air with the shortest possible route to the edge of the medium and on to any free space in the reservoir can also reduce the amount of air residing in the porous medium. The provision of pathways through the medium from adjacent to the spray head to the edge of the medium can help to encourage air away from the spray head and on to the edge of the medium and any free space in the reservoir. These methods assist in the removal of air from the medium and thus reduce the risk of breaking down fluidic pathways.
To aid the understanding of the present invention and the terms used in the claims, it will be beneficial to understand the following theory and definitions of terms:
Effective pore size can also be described as the equivalent capillary tube radius required to provide the same rise-height in a simple capillary tube as is achieved in the porous medium for a given fluid.
The required tube radius for a simple capillary tube achieving a given rise-height can be calculated from the following equation, which gives the maximum achievable rise-height as:
where ρ is the fluid density, σ is the fluid surface tension, g is the acceleration due to gravity, R is the capillary tube radius, hmax is the maximum rise height and α is the contact angle made between the fluid and the capillary wall.
To calculate an effective pore size, the same equation can be applied to porous media, with contact angle α tending to zero at hmax, to find an effective radius of the pores in a sample. However, due to the complex microscopic structure of porous media, these media generally consist of a range of actual pore sizes within a given volume of medium. Therefore the value of R must be considered as an effective pore size as calculated for a finite section of a medium, based upon the rise height achieved by a sample having the properties of that section.
Further, porous media generally exhibit hysteresis and so the values of R and hmax may be different for the same media depending on whether it starts being saturated and surrounded by fluid which is then drained, or it starts being dry and is brought into contact with the same fluid.
In the present description and claims, when we refer to effective pore size, we mean that derived from the rise height measured from a fully-saturated starting condition and calculated according to Equation 1 above.
Experiments to determine the effective pore size in a sample can be conducted as follows:
When using equation 1 to determine effective pore size, it is necessary to pump fluid out of a full reservoir through the medium in order to find the maximum rise-height achieved and thus calculate an effective pore size, R.
For a homogeneous media this approach is actually measuring the effective pore size at the top of the sample, furthest away from the reservoir fluid level, as this is the point at which the fluidic pathways will break down first.
For a non homogeneous medium or a compressed homogeneous medium, the fluidic path may not fail at the top of the sample. This is because, in an ideal embodiment of this invention, the effective pore size gradient through the sample brings about a situation in which the medium is transporting fluid close to its maximum achievable rise-height at numerous points along the fluidic path. Therefore, in this case the value of R obtained from equation 1 can be called an effective pore size for the whole sample of the medium, in the orientation in which it is being operated.
One way of detecting a gradient in effective pore size within a sample of medium is to perform the same rise-height experiment with the sample under different orientations; a homogeneous medium will exhibit the same maximum rise height, a non-homogeneous medium will exhibit differing rise heights with the maximum rise height achieved when the smaller effective pore size is at the maximum height.
Using fluids of reduced surface tension and/or increased density for the above experiments will reduce the rise height achieved. This can help ensure that the maximum rise height is less than the overall sample length so that breakdown of the fluidic pathways can be observed.
It is also important to note that two media may exhibit equal rise heights when a sample of each dry medium is brought into contact with a fluid, but that these same two media may support different rise heights when starting from a fully-saturated condition. At least two effective pore sizes may therefore be defined for a given medium. In the following description and claims, when we refer to effective pore size, we mean that derived from the rise height measured from a fully-saturated starting condition and calculated according to Equation 1 above.
Considering the flow of fluid along a saturated, inclined porous medium of length L, the flow rate per unit area, q is a function of several variables;
K is commonly referred to as the hydraulic conductivity and is proportional to the permeability, k, and fluid density, ρ, and inversely proportional to the fluid viscosity, μ. φ is a measure of the potential and is a function of the vertical height, z and the fluidic pressure, pi. From this it can be seen that for a positive flow rate the change in potential must be negative. For cases where the fluid exit height is gravitationally above the fluid entry height this requires that the fluidic pressure at the exit location be lower than the fluidic pressure at the entry location. This fluidic pressure reduction at the fluid exit location is, in this case, created by the spray head pumping the fluid out of the reservoir. From this it can be understood that the lower the permeability k of the medium, the higher the required pressure differential, and the harder the spray head must work, provided that the other variables are kept constant.
Permeability is a well known term in the art and there are many known ways of measuring the permeability of a sample of porous medium.
Differences in the permeability of a sample of porous medium from one point to another may be detected by measuring pressure-drops across those points for a given flow-rate of fluid through the medium. It will be appreciated that pressure drops should be measured over the same distance at each point to get an accurate comparison of the permeability at each point.
The permeability of a porous medium is, in general, approximately proportional to the square of its pore radius. Therefore, reducing the effective pore size so as to increase the rise height results in a large reduction in permeability. Since the spray head can generally only provide a limited pressure differential, this reduction in permeability k results in a reduction in the achievable flow rate q.
It is therefore advantageous to reduce the effective pore size, and resulting permeability, only as much as is necessary to achieve the rise-height required at each point along the fluidic pathway in the medium.
The effective pore size in a porous medium can be influenced by a number of factors. These include: the uniformity of the pore size in a medium, how pores of a different size are distributed in the medium, how pores interconnect in the medium and the mean pore size in the medium.
To calculate these or other statistical properties of the medium the concept of a ‘representative elementary volume’ is useful. This volume is large enough so as to contain enough pores such that the statistical properties within it represent the average properties of the medium at the location in question, but is not so big that non-homogeneity of the overall medium is seen.
To determine the representative elementary volume and calculate the statistical properties at a location in the medium, first calculate the properties of the medium over a specified volume or area where this volume or area is of the order of the pore size. Then increase this volume or area by small amounts and recalculate the statistical properties until any significant fluctuations in the calculated properties from one increment to the next are removed.
According to the present invention there is provided a fluid spray dispenser comprising:
a fluid reservoir for, in use, holding fluid to be dispensed;
a spray head for dispensing the fluid; and
a porous medium through which, in use, fluid passes from the reservoir to the spray head, the porous medium having a pathway located substantially adjacent the spray head for the removal of air ingested into the porous medium.
The pathway acts to remove the air to reduce the risk of air ingested by the spray head blocking the supply path of fluid to the spray head.
The pathway may be formed from one or more connected pores whose size is greater than that of the pores in the surrounding region. Creating the channel from larger pores within the medium itself removes the need for separate components or channels to remove the air.
The pathway may be a void formed in the porous medium. Forming a void in the porous medium to remove the ingested air also removes the need for separate components and enables ingested air to enter the channel at multiple locations along its length.
The channel may be supported by an insert in order to maintain the shape of the channel. Supporting the channel can help to avoid collapse of the channel, in particular if the porous medium is held under any stress.
The insert may be made from the same material as the surrounding porous medium. Making the insert from the same porous medium can reduce manufacturing costs incurred by the use of different materials.
The insert may be made from a different porous or non-porous material to the surrounding porous medium. This can allow the insert to have different physical properties to the surrounding porous medium, which may help to maintain its form and/or aid the movement of air or fluid through the medium.
The insert may be a hollow tube. This allows the air to be separated from the fluid in the porous medium as it moves along the channel.
The channel may be conic in shape, with the narrow end adjacent the head. This arrangement is advantageous because a slug of air trapped within the tube will try to minimise its surface area. A small movement of the slug towards the larger radius end will reduce the overall surface area and therefore air will tend to move from the smaller radius end towards the larger radius end.
The pathway may be formed substantially at the centre of the spray head. Forming the channel at the centre of the spray head is advantageous because the maximum distance that air ingested anywhere on the spray head has to travel through the non-modified porous medium before reaching the edge of the porous medium is minimised.
The spray head may include a piezoelectric actuator and a perforate membrane.
The porous medium may also have an effective pore size that decreases towards the spray head. The decreasing effective pore size of the medium facilitates an improved permeability of the medium for a given rise height and therefore an improved flow rate for a given rise height and spray head power.
The porous medium may also have a permeability when saturated that decreases towards the spray head. Reducing the permeability towards the spray head allows the permeability to be maximised and related pressure drop to be minimised in regions away from the spray head.
A plurality of pathways may be located substantially adjacent the spray head for the removal of air ingested into the porous medium. The provision of a plurality of pathways can further reduce the maximum distance that air ingested anywhere on the spray head has to travel through the non-modified porous medium before reaching the edge of the porous medium.
One example of the present invention will now be described with reference to the following drawings in which:
Firstly, while the effective pore size needs to be small enough to support the required fluid rise height, it should also be as large as possible to give maximum flow rate. The permeability, which affects flow rate, is linked to the pore sizes along the entire fluidic path from the free liquid in the reservoir to the spray head. The maximum rise height is only required at the location of the spray head, with reduced rise height required away from the spray head. Therefore increasing the effective pore size at each point away from the spray head, whilst still supporting the required rise height at that point, will increase permeability and lead to a lower overall fluid feed resistance and improved spray performance. This is illustrated by
Non-planar spray heads with either of one or two dimensional curvature are often used to give particular plume characteristics. However, compressing a planar section of porous media against such a head will lead to the effective pore size increasing towards the head. This would encourage the trapping of any ingested air next to the head and thus block the fluidic pathways through the medium.
An alternative method of ensuring contact between the porous medium and the spray head is to take a piece of medium of the form shown by the square 55 in
A porous medium of non-planar profile may be manufactured according to the process shown in
Both continuous gradients in pore size and discrete changes in pore size are beneficial and can be achieved in several ways in addition to those shown in
An alternative method of creating changes in effective pore size is by placing multiple homogenous porous media in contact with each other, each section having a different effective pore size.
A section of porous medium which, in its relaxed state is homogenous, may be compressed, stretched and/or twisted so as to induce preferable gradients in pore size. Such deformations may be achieved by a supporting structure, which may itself be made of a porous medium or of a non-porous medium. This supporting structure may be, for example, the fluid reservoir housing, or the spray head itself.
Examples of such deformation methods are shown in
An alternative method of creating the desired pore size gradient is illustrated in
As the dispenser is used and liquid is ejected from the reservoir by the spray head, any free liquid in the reservoir will eventually be used up, and air will start to replace the liquid in the porous media. The smaller the effective pore size, the more energy is required to displace the liquid, therefore keeping pore sizes as large as possible is beneficial. Further, providing a gradient in effective pore size by any of the means described above through the provision of a continuous gradient, or a series of discrete changes, will lead to liquid furthest away from the spray head being preferentially displaced first. With the smallest effective pore sizes located adjacent to the spray head, displacement of the liquid furthest away from the spray head in the larger pores will act to maintain the fluidic pathways from the spray head to the remaining fluid for longer than if the effective pore size were homogenous. This results in more of the stored liquid being sprayable.
Any air that is ingested through the spray head can block fluidic pathways in the porous medium and cause a reduction in flow rate. It is therefore important that such air should be encouraged to move away from the spray head. Providing a pore size gradient in the vicinity of the spray head can encourage air to move away from the spray head.
Most porous media has a distribution of pore sizes, meaning that air can also become trapped in larger pores if surrounding smaller pores are filled with liquid. In general therefore, it is desirable that any ingested air has only a short path to the edge of the porous medium, or to larger pores leading directly to the edge of the medium. This reduces the likelihood of ingested air becoming trapped and blocking the path of fluid to the spray head. To provide any ingested air with the desirable shortest possible route to the edge of the porous medium it is possible to provide one or more pathways in the medium specifically for the removal of air.
Alternative methods of creating air channels for the removal of air from the vicinity of the spray head are shown in
In example A, the pathways may be created as one or more voids in the porous medium, each connecting the spray head to an edge of the porous medium. A drawback of this embodiment is that the air removal pathways may collapse if no structural supporting element is provided.
In example B, the pathways are provided as one or more voids in the porous medium, each pathway connecting a point close behind the spray head to an edge of the porous medium.
Example C illustrates how the pathway may consist of a region of pores having an effective size larger than the pores in the surrounding medium. Such a pathway could be formed during manufacture, or through the use of an insert of alternative porous medium. This insert may also help to provide structural support to the pathway to ensure that it is kept open. This avoids the potential drawback of embodiment A.
Example D shows an alternative means of keeping the pathway open by supporting it with a structural component(s).
Example E shows the use of structural components which may be conical in shape. This can further encourage the movement of air away from the spray head when the free liquid in the reservoir is at a level which fully immerses the spray head and adjacent porous medium in liquid.
Example F shows a way in which multiple separate paths may be employed to assist in the removal of air from the vicinity of the spray head.
| Number | Date | Country | Kind |
|---|---|---|---|
| 0810667.6 | Jun 2008 | GB | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/GB2009/050652 | 6/10/2009 | WO | 00 | 2/11/2011 |
