The present invention relates to nozzle arrangements. More particularly, but not exclusively, the present invention relates to nozzle arrangements that are adapted to generate a spray of a fluid, which is forced to flow through the nozzle arrangement under pressure.
Nozzles are often used to provide a means of generating sprays of various fluids. In particular, nozzles are commonly fitted to the outlet valves of pressurised fluid-filled containers, such as so-called “aerosol canisters”, to provide a means by the fluid stored in the container can be dispensed in the form of a spray or mist. A large number of commercial products are presented to consumers in this form, including, for example, antiperspirant sprays, deodorant sprays, perfumes, air fresheners, antiseptics, paints, insecticides, polish, hair care products, pharmaceuticals, water and lubricants. In addition, pump or trigger-actuated nozzle arrangements, i.e. arrangements where the release of fluid from a non-pressurised container is actuated by the operation of a manually operable pump or trigger that forms an integral part of the arrangement, are also frequently used to generate a spray or mist of certain fluid products. Examples of products that typically incorporate pump or trigger nozzle devices include various lotions, insecticides, as well as various garden and household sprays.
A spray is generated when a fluid is caused to flow through a nozzle arrangement under pressure. To achieve this effect, the nozzle arrangement is configured to cause the fluid stream passing through the nozzle to break up or “atomise” into numerous droplets, which are then ejected through an outlet of the arrangement in the form of a spray or mist.
The optimum size of the droplets required in a particular spray depends primarily on the particular product concerned and the application for which it is intended. For example, a pharmaceutical spray that contains a drug intended to be inhaled by a patient (e.g. an asthmatic patient) usually requires very small droplets, which can penetrate deep into the lungs. In contrast, a polish spray preferably comprises spray droplets with larger diameters to promote the impaction of the aerosol droplets on the surface that is to be polished and, particularly if the spray is toxic, to reduce the extent of inhalation.
The size of the aerosol droplets produced by such conventional nozzle arrangements is dictated by a number of factors, including the dimensions of the outlet orifice and the pressure with which the fluid is forced through the nozzle. However, problems can arise if it is desired to produce a spray that comprises small droplets with narrow droplet size distributions, particularly at low pressures. The use of low pressures for generating sprays is becoming increasingly desirable because it enables low pressure nozzle devices, such as the manually-operable pump or trigger sprays, to be used instead of more expensive pressurised containers and, in the case of the pressurised fluid-filled containers, it enables the quantity of propellant present in the spray to be reduced, or alternative propellants which typically produce lower pressures (e.g. compressed gas) to be used. The desire to reduce the level of propellant used in aerosol canisters is a topical issue at the moment and is likely to become more important in the future due to legislation planned in certain countries, which proposes to impose restrictions on the amount of propellant that can be used in hand-held aerosol canisters. The reduction in the level of propellant causes a reduction in the pressure available to drive the fluid through the nozzle arrangement and also results in less propellant being present in the mixture to assist with the droplet break up. Therefore, there is a requirement for a nozzle arrangement that is capable of producing an aerosol spray composed of suitably small droplets at low pressures.
A further problem with known pressurised aerosol canisters fitted with conventional nozzle arrangements is that the size of the aerosol droplets generated tends to increase during the lifetime of the aerosol canister, particularly towards the end of the canisters life as the pressure within the canister reduces as the propellant becomes gradually depleted. This reduction in pressure causes an observable increase in the size of the aerosol droplets generated and thus, the quality of the spray produced is compromised.
Accordingly, it is an object of the present invention to provide a nozzle arrangement that is adapted to generally reduce the size of the droplets generated when compared with conventional nozzle devices, as well as reduce the droplet size distributions. In addition, it is an object of the present invention to provide a nozzle arrangement that is adapted to enable small droplets of fluid to be generated at low pressures, i.e. when fluids containing reduced or depleted levels of propellant, or a relatively low-pressure propellant such as compressed gas, is used, or a low-pressure system is used, such as a pump- or trigger-actuated nozzle arrangement.
The problem of providing a high quality spray at low pressures is further exacerbated if the fluid concerned has a high viscosity because it becomes harder to atomise the fluid into sufficiently small droplets.
Accordingly, it is a further object of the present invention to provide a nozzle arrangement that is capable of generating a spray from a viscous fluid at low pressures.
A further problem associated with known nozzle arrangements is that certain products have a tendency to block or clog the spray orifices provided in the nozzle arrangement International Patent Publication Numbers WO 01/89958 and WO 97/31841 both describe cleanable nozzle arrangements, which can be slit apart to expose the internal fluid flow passageway for cleaning. However, it is not practicable to clean the spray orifices after each individual use, which may be necessary with some products that are particularly prone to clogging the nozzle arrangement. As a consequence, the spray orifices present at the outlet of the nozzle arrangement or within the nozzle can become blocked or clogged with such products, which can adversely affect the performance of the nozzle arrangements and thus, the quality of the spray produced.
Hence, it is a further object of the present invention to provide a nozzle arrangement in which the occurrence of blockages at spray orifices is obviated or at least substantially minimised.
In the case of nozzles fitted to pressurised aerosol canisters, there is also a tendency for the fluid flow through the nozzle to reduce as the contents present in the canister become depleted. As previously indicated, this is primarily due to the depletion of the propellant present in the canister and can be particularly undesirable because it results in the quality of the spray produced by the nozzle arrangement being compromised as the canister approaches the end of its operational lifetime.
For this reason, it is a further object of the present invention to means by which the level of fluid flow through a nozzle arrangement can be maintained at a constant or substantially constant level.
According to the present invention there is provided a nozzle arrangement adapted to be fitted to .an outlet of a fluid supply and generate a spray of fluid dispensed from said fluid supply during use, said nozzle arrangement having a body which comprises:
wherein said fluid flow passageway further comprises an internal chamber, said chamber having two or more inlet orifices, and an outlet orifice through which fluid may exit the chamber.
The inlet orifices are preferably not directed towards the outlet orifice, so that the fluid will impinge on an internal wall of the chamber. The paths of the fluid from the orifices can be directed either on mutually divergent or mutually convergent paths.
The orifices are preferably outlets from ducts or passages aligned in the direction of the paths, and may lead from a space or chamber downstream of the said internal chamber to the orifices in the latter.
The internal chamber may be configured as a vestibule to the outlet orifice of the nozzle arrangement and have outlet means leading to a plurality of outlet orifices of the nozzle arrangement. Alternatively the outlet from the internal chamber may comprise a single outlet orifice, or a swirl chamber may be provided between the internal chamber and the outlet orifice.
A by-pass passage may be provided which leads from the downstream space or chamber to the internal chamber, and the by-pass passage may feed a plurality of tangential or otherwise aligned inlet orifices into the internal chamber. The flow paths from the by-pass inlet orifices may be arranged to intersect the flow paths from the first mentioned inlet orifices.
A further feed passage may be provided for gaseous medium such as air to be mixed with a liquor phase fluid, direct to the internal chamber. The gaseous medium may be introduced into the internal chamber via a plurality of orifices as a tangential or otherwise directed stream, and the streams may be directed to intersect the paths of fluid entering the internal chamber through the first mentioned inlet orifices.
In another embodiment, liquid phase fluid is fed tangentially to the downstream space and gaseous medium fed direct to the downstream space where they are mixed and then fed to the internal chamber by the ducts or passages from the space to the chamber.
The internal chamber may comprise an expansion chamber and have two or more inlet orifices and two or more outlet orifices, the inlet orifices being arranged in a divergent relationship to one another so that the fluid passing through the internal passageway accesses the chamber through the inlet orifices along independent and divergent paths, and the divergent inlet orifices preferably direct fluid towards the internal walls and/or to corners of the chamber.
The fluid entering the chamber is preferably directed towards an opposing wall of the expansion chamber or a corner between an opposing wall and an opposing wall and an adjacent wall of the expansion chamber.
One or more posts or protrusions may be positioned within the chamber to provide internal wall surfaces towards which the fluid may be directed.
Alternatively, the fluid may be directed towards one or more nodules formed on the internal walls and/or corners of the chamber said nodules being configured to cause further agitation or disturbance to the fluid stream within the chamber.
The outlet orifices may direct fluid exiting the chamber into a continuation of the passageway, and the chamber may be disposed next to the outlet and the outlet orifices of the expansion chamber may constitute outlet orifices of the nozzle arrangement.
The two or more inlet orifices of the internal chamber may be disposed in a convergent relationship to one another so that the fluid stream flowing through the inlet orifices into the chamber are directed toward one another and mix within the chamber.
The nozzle arrangement may, in addition to the said chamber, be configured to provide one or more expansion chambers with aligned inlet and outlet orifices or with a tangential feed, one or more swirl chambers, a chamber having constricted inlet and outlet orifices of lesser diameter from the fluid flow passageway, the latter preferably located between two expansion chambers, a venturi means, and/or a flap valve operative to variably constrict an orifice in response to variation in the pressure of fluid within the passageway, the said further arrangement being provided in any suitable combination.
The fluid supply may be any suitable fluid supply to which a nozzle arrangement is usually attached. In most cases the fluid supply will be container, such as pressurised hand-held aerosol canister.
The nozzle arrangements of the present invention are preferably formed from plastic.
It is also preferable that the body of the nozzle arrangements of the present invention is composed of at least two interconnected parts. Each part preferably has an abutment surface, which may be brought into contact with one another to form the final nozzle arrangement assembly. One or more of the abutment surfaces preferably comprise grooves and recesses formed thereon which, when the surfaces are brought into contact, define the fluid flow passageway (including any chambers positioned along its length), as well as the outlet and, optionally, the inlet. Preferably, a seal is provided between the abutment surfaces, which prevents fluid passing through the nozzle arrangement from leaking out between the abutment surfaces during use. This construction is preferred because it can be manufactured very cheaply and with a high degree of precision. In addition, the constituent parts of the body may be permanently fixed together to form the final, assembled nozzle arrangement or, alternatively, the parts may remain separable so that fluid flow passageway may be opened and exposed for cleaning. Most preferably, the nozzle arrangement is formed of two parts interconnected by a hinge so as to enable the respective parts to be moved towards or away from each other to enable cleaning to be effected.
Preferably, the nozzle arrangement includes one or more internal chambers which are configured to have a width extending transversely of the flow passage and in the plane of the abutment surface of the two parts of the nozzle arrangement, and a depth perpendicular to said plane, which is greater than said width.
The internal chamber preferably has curved interior surfaces defining an elliptical cross-section to said chamber, the major axis of which constitutes the depth. Alternatively, the internal chamber may have planar internal surfaces defining a rectangular or other polygonal cross-section to said chamber.
Advantageously, two or more of the chambers extend in parallel and are provided in independent multiple flow paths of said flow passage.
Nozzle arrangements of this construction are described further in WO 01/89958 and WO 97/31841, the entire contents of which are incorporated herein by reference.
The actuator means may be any suitable actuator means that is capable of initiating the flow of fluid through the nozzle arrangement. Various means are well known in the art. For example, nozzle arrangements fitted to pressurised fluid-filled canisters typically comprise and actuator that can be depressed so as to engage and open the outlet valve of the canister and thereby permit the fluid stored therein to be dispensed through the nozzle arrangement. In addition, pump and trigger nozzle arrangements are widely available as a means for dispensing fluids from non-pressurised containers. In these cases, the operation of the pump or trigger generates the pressure, which causes the fluid from the container to be dispensed through the nozzle arrangement.
How the invention may be put into practice will now be described in more detail in reference to the following Figures, in which:
During use, the fluid flow passageway 101 feeds fluid into a first chamber 201 through a constricted inlet 202. This causes the fluid to be introduced into the first expansion chamber. Fluid passing through the first expansion chamber travels along a series of divergent orifices 203, which form divergent inlet orifices to a second expansion chamber 204. The second expansion chamber is provided with three outlet orifices 102, through which fluid is ejected from the second chamber and the nozzle arrangement. An important feature of this embodiment resides in the divergent inlet orifices being arranged so that fluid entering the second chamber is directed against the opposing wall 206, or a corner between an opposing wall 206 and an adjacent wall 207, rather than directly towards the outlet orifices 102. The consequence of this arrangement is that fluid is caused to impact on the opposing wall and/or the corner between an opposing wall and the adjacent wall and thereby causes the disruption of the fluid stream and further atomises the droplets contained therein.
To the
Finally,
It will be appreciated that the flow passageways shown in
Turning now to the
The expansion chambers 129, 130, 131 are remarkable in that they have an elliptical cross-section, with the major axis extending perpendicularly to the plane defined by the interface 123. The expansion chambers could be provided with plane internal surfaces forming rectangular or polygonal chambers. As shown the chambers have considerable elongation on the major axis, e.g. about 5:1 which enable a substantial chamber volume to be attained whilst enabling parallel chambers to be used, which is not possible with conventionally formed chambers because of lack of space.
The chamber design may also be applied to other features such as swirl chambers, and the expansion chambers may be varied from that shown e.g. with tangential inlet feed rather than axial, and be formed with single or multiple throttles.
The chambers may be set in divergent paths or have divergent inlet and outlet orifices, or be offset with respect to each other to create more space for e.g. larger chambers.
The chamber arrangement of
The multiple orifices may lead from a chamber with a tangential feed, which causes the fluid to rotate and spin within the orifice channels, or each orifice could be provided with a respective swirl chamber. The chamber to which they lead may be accessed from the rear, straight from the side, tangentially from the side or any combination thereof. Inlets may face each other across the chamber so that their streams strike each other tangentially, from the same directions or in opposite directions, and in any combinations of single or multiple orifices at different locations.
Additional feeds for air or other gaseous medium may be provided in any embodiment, and this may be fed via a single orifice or multiple orifices and from any surface of the chamber, and in the same or in an opposed direction to the liquid phase medium.
The gas may be fed from parallel, divergent or convergent apertures, and the routes of gas and liquid feeds in
The orifices will tend to be from 0.15-0.4 mm in diameter and 0.2-2 mm in length. Smaller diameters such as 0.05 mm diameter may risk blocking. The orifices and passages may be of different diameter.
There may usually be from 2 to 4 orifices but would be as many as 10, and similarly for the air or gas orifices which could however be smaller and in the 0.05-0.2 mm diameter range.
Two separate liquid phase fluids may be introduced in place of the gaseous medium, and the fluid used in singe phase applications may be either liquid or gas.
Whilst the input streams may not impact each other directly if the chamber is flooded, or a tangential feed may result in a vortex around the walls of the chamber so that the stream does not impinge the other feed streams, nevertheless greater turbulence is created inside the chamber which causes greater droplet control in the final sprays.
Number | Date | Country | Kind |
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0315664.3 | Jul 2003 | GB | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/GB2004/002848 | 7/2/2004 | WO | 00 | 4/10/2008 |