[0001] This invention relates to pressurised dispensers, in particular to the kind of small
hand-held dispenser often colloquially known as an 'aerosol can'. However it is not
limited to dispensers which are hand-held, nor to those in which the container is
a can.
[0002] The aim of such dispensers is usually to produce a spray of fine particles of the
product to be dispensed, the cone angle of the spray and the fineness of particles
or droplets being dependent on the requirement of the particular purpose and product
involved.
[0003] The spray head or button of such a dispenser generally employs a nozzle with a swirl
chamber to which the mixture of product and propellant is admitted tangentially so
that a swirl is imparted to the mixture before it emerges into the atmosphere at a
high speed from an orifice on the axis of the chamber and breaks up into a fine spray
of predictable particle size.
[0004] This is a so-called 'mechanical break-up' system, and examples of nozzles designed
for such use are shown in British Patent Specification Nos. 826527 and 845810 of Precision
Valve Corporation, 1 018 902 and 1 032 065 of E.H. Green and 1 161 865 of Risdon.
[0005] However in practice, using conventional propellants, the break-up into droplets is
not caused by any means solely by the swirling action but also by the sudden explosive
drop in pressure as the mixture emerges into the atmosphere and, even more important,
by the instantaneous evaporation of the propellant, which is a liquid at the pressures
prevailing in the can but a gas at atmospheric pressure. Its sudden evaporation blows
apart the droplets of the mixture of which it forms part, ensuring the production
of a fine spray of particles of relatively consistent size.
[0006] The above is true, however, only where the propellant is one of those conventionally
used to a wide extent in the past and generally one of the so-called chloro-fluorocarbons
(CFC's) or their equivalent, or one of the lower hydrocarbons such as butane or propane
which, like CFC's, are liquid at the pressure prevailing in a pressurised dispenser
at normal temperatures but gaseous liquid at atmospheric pressures. For environmental
reasons there is now a strong move away from CFC's, and the use of hydrocarbons has
its drawbacks in many situations as they are flammable.
[0007] The great advantage of these non-permanent gases in pressurised dispensers has been
that the pressure in the container remains constant throughout its useful life; there
is liquid propellant mixed with the product filling the greater part of the can when
it is new, with an atmosphere of gaseous propellant above it. As the product and propellant
are used up the liquid level falls but more propellant evaporates into the gas space
above and the pressure remains unchanged, governed only by the temperature at which
the can is stored.
[0008] For the environmental reasons mentioned above strenuous efforts have been made for
a number of years to get away from the CFC's and hydrocarbons, and a lot of work has
been put into substituting other materials, mainly the permanent gases such as carbon
dioxide, nitrous oxide, nitrogen and even air. Carbon dioxide has its own problems
in that it is now environmentally suspect, and although its slight solubility (with
difficulty) in some products does give it the advantage that it does to some degree
try to maintain pressure by evaporation into the gas space as the liquid level falls,
this effect is strictly limited. Nitrous oxide is expensive. Air is unsatisfactory
with most products because the oxygen in the air may, over the long period which an
aerosol can may be on the shelf before use, attack components in the product. Nitrogen
is ideal from this aspect, being almost totally inert, but like air and other permanent
gases it suffers from the very serious drawback that the pressure in the container
falls continuously and exponentially throughout the useful life of the dispenser.
[0009] The amount of the fall will depend on the proportions of gas and of product initially
in the container. If there is to a reasonable and useful amount of product present
to be dispensed then in a typical case the pressure might fall from 9 bar when the
dispenser is new to 3 bar or even less by the time 95% of the product has been dispensed.
[0010] The position is further aggravated if the user inadvertently, or through not realising
the problem, tilts the container and tries to dispense in a position in which the
lower end of the dip tube is momentarily uncovered by liquid. Where the propellant
is a permanent gas this can result in a direct and rapid loss of pressure, in contrast
to a dispenser of the earlier kind, where there is a margin of surplus propellant
and where, unless the uncovering is prolonged, the pressure is restored by additional
evaporation of propellant from the liquid.
[0011] However the main drawback of the fall in pressure using permanent gases is the behaviour
of the spray nozzle. Such nozzles are designed for spraying at a given pressure, or
at least at pressures within a certain limited range. As the pressure falls not only
does the rate of delivery fall but also the spray pattern changes and the droplet
size becomes much coarser so that, for example in the case of body sprays, there is
an increase in the perceived wetness of the product in contact with the skin.
[0012] Manufacturers of pressurised dispensers and of valves for them are well aware of
this problem and many attempts have been made in recent years to overcome it by the
use of some kind of compensator. These attempts have mainly have directed to the provision
of spring-loaded pressure-reducing valves mounted somewhere in the path of the product
from the interior of the container to the dispensing orifice, usually in the spray
tip or button itself. In one known arrangement, there is initially a substantial pressure
drop in the reducing valve but as the pressure in the container falls a spring moves
a piston-like valve member back and the reduction is less, so that the pressure at
the nozzle orifice is kept approximately constant. In another, instead of a piston
and spring, a resilient disc acts as a combined valve member and spring.
[0013] In a third known proposal the reducing valve is made of rubber and again acts as
a combined valve member and spring; it is mounted not in the nozzle but in the valve
housing, at an earlier point in the flow path, but again the purpose is to introduce
a pressure drop which itself falls as the pressure in the container falls.
[0014] It will be evident that these solutions, especially those involving sliding spring-backed
pistons, are not only expensive to produce but are moreover likely to be uncertain
in operation after a substantial shelf life. Other solutions have involved a capillary
dip tube or a restricted tail piece ('RTP') on the valve housing to restrict flow
and introduce a pressure drop.
[0015] All such solutions involving a deliberately introduced pressure drop well ahead of
the final nozzle orifice are furthermore in effect throwing away the advantage of
the initial available pressure, and the nozzle has to be designed for a relatively
low pressure, which restricts the ability to produce a fine spray and a good spray
pattern.
[0016] The aim of the present invention is therefore to provide a way of achieving a sufficiently
consistent fine spray and good spray pattern throughout the useful life of a pressurised
dispenser, yet a low cost and without the use of moving parts.
[0017] According to the invention we achieve this simply by using, in the final nozzle leading
to atmosphere, a restricted number of channels of significantly smaller total cross-section
than used hitherto, in conjunction with a final orifice of a diameter smaller than
those used hitherto, this final orifice and channel or channels being the predominant
restriction in the flow path from the interior of the container to atmosphere, that
is to say, being of smaller cross-section than the dip tube and of any internal metering
orifice (IMO) in the valve housing or valve member.
[0018] Unexpectedly, as the examples which follow will show, this makes it possible to achieve
an acceptably constant flow rate and droplet size over a pressure range of as much
as three to one or even more.
[0019] In a preferred embodiment there are two tangential channels, or only one, leading
into a swirl chamber behind the final orifice and the or each channel is not more
than 250 micrometres wide by 175 micrometres wide. The final orifice itself is between
150 and 200 micrometres in diameter. It has been found that, using the conventional
water-based or alcohol-based products in conjunction with a nitrogen or carbon dioxide
propellant, such a nozzle can produce a more than satisfactory spray pattern and droplet
size when the pressure in the container falls from 9 bar to 2½ bar.
[0020] It is believed that one factor contributing to this unexpected result is that the
main pressure drop which controls the rate of flow is concentrated at the nozzle,
i.e. the flow rate is not influenced by any internal metering orifice (IMO) or restricted
tailpiece (RTP) at an earlier point in the flow.
[0021] The delivery rate inevitably falls to some extent as the pressure falls, and indeed
there is also some increase in the droplet size, but a compensating factor which has
been observed is that at a lower flow rate a small increase in particle size gives
no increase in perceived wetness (e.g. in a body spray).
[0022] In a typical case the initial delivery rate may be of the order of 0.6 gm/second,
falling perhaps to 0.45 gm/sec towards the end of the life of the dispenser.
[0023] The invention will now be further described by way of example with reference to the
accompanying drawings, in which:-
Figure 1 is a cross-section through a typical valve assembly for a pressurised dispenser;
Figure 2 is a section through a portion of the spray tip or button of an assembly similar
to that of Figure 1, showing the spray nozzle or insert;
Figure 3 shows a section through the insert alone, and constructed in accordance with the
invention;
Figure 4 is a view of the insert of Figure 3 looking axially at its rear face;
Figure 5 is a view similar to Figure 4 but showing an alternative form of insert;
Figure 6 is a graph showing the result of a test using the insert of Figures 3 and 4 and indicating
the fall in pressure with use;
Figure 7 is a graph showing the fall in discharge rate with use;
Figure 8 is a graph showing the change in medium particle size as the contents of the dispenser
are used up;
Figure 9 is a combined graph and histogram illustrating the particle size distribution in
the spray obtained from the insert of Figure 5 at a given discharge rate; and
Figures 10 and 11 correspond to Figure 9 but shows the particle size distribution at different pressures.
[0024] Referring first to Figure 1, a typical valve assembly for a hand-held pressurised
dispenser comprises a mounting cup 1 (for mounting as a standard 'one-inch' opening
in a container) supporting a valve housing 2 which traps a gasket 3 against the top
wall of the centre boss 4 of the mounting cap. A tail 5 on the lower end of the housing
2 receives a flexible dip tube 6 which extended down to near the bottom end of the
container in use. The tail has a restricted entry (RTP) at 7.
[0025] Within the housing 2 is a valve member 8 urged against the gasket 3 by a spring 9
and having a central stem 10 which extends up through the gasket to receive an actuating
button or spray tip 11. An outlet orifice for the product to be dispensed is formed
at 12 in a cup-shaped insert 13 which is force-fitted into a recess 14 in the button,
simultaneously fitting over a central post 15 of the button.
[0026] A small radial hole 16 leading into a central passage 17 in the stem 10 is covered
by the gasket 3 in the rest position of the valve but when the button is depressed,
carrying the valve member downwards with it, the liquid product in the container,
under the pressure of the propellant gas also present in the container, is forced
up the dip tube 6, though the housing and the hole 16 into the passage 17 and through
passages 18 and 19 in the button 11 to the insert 13 to emerge as a spray through
the orifice 12.
[0027] All that has been described so far is well known. The passage 19 in the button leads
into four tangential channels which are defined between the back of the insert 13
and the face of the post 15 to converge on a swirl chamber from which the product
passes through the orifice 12 with a swirling action. This is what achieves the so-called
mechanical break-up.
[0028] The heart of the present invention lies in a novel construction of the channels (there
may only be one) and the orifice. For this we refer to Figures 3 and 4. Instead of
four tangential channels we have only a single one, shown at 20 in Figure 4, formed
by a groove in the back of the insert and having an axial depth of between 150 and
200 micrometres. The width is the same. Thus the cross-sectional area is between 0.0225
and 0.04 square millimetres. The back wall of the channel is formed by the end face
of the post. The length is of the order of 1mm, but will depend on the diameter of
the post and the diameter of the swirl chamber, shown at 21. The orifice 12 has a
diameter of between 200 and 250 micrometres giving it a cross-sectional area of between
0.003 and 0.05 square millimetres, i.e. a mean value rather greater than the cross-sectional
area of the channel 20. Thus it is the channel 20, immediately preceding the orifice
12, which is the governing restriction in the flow path between the interior of the
container and atmosphere. This cross-section is significantly smaller than any other
ahead of it in the flow path, in particular it is smaller than the radial hole (IMO)
16 in the stem and the restriction (RTP) 7 at the inlet to the housing 2. Generally
speaking, each of these last-mentioned holes will be at least 450 micrometres in diameter.
[0029] Both the channel size and the size of the orifice 12 are believed to be substantially
below those hitherto ever used in production in the nozzles of pressurised dispensers.
The axial length of the orifice 12 in the example shown is 150 micrometres, i.e. rather
less than its diameter, whereas the figures above show that in the case of the channel
20 the length is five or six times the width. Generally speaking it should be at least
four times the width.
[0030] We are not limited to there being only a single channel. Figure 5 shows an insert
with two tangential channels 20 and 20′. They are each of the same dimensions as the
single channel 20 of Figures 3 and 4, and allow an increased flow rate, although with
an orifice 12 of the same size as before the flow rate is by no means doubled. In
practice we prefer to use not more than two channels.
[0031] The remaining Figures are graphs and histograms illustrating test results obtained
with the arrangement according to the invention. Figure 6 shows how, with a typical
hand-held pressurised dispenser fitted with the valve assembly described and using
nitrogen as the propellant gas, the pressure inside the container may fall from an
initial pressure of 9 bar when the container is new to as little as 2½ bar when 95%
of the useful contents have been dispensed. With the known nozzles, in the absence
of any compensator, this would result in a very poor spray pattern and very large
droplets towards the end of the useful life of the dispenser, and possibly even dribbling
rather than spraying.
[0032] As shown in Figure 7, however, it will be seen that, using the nozzle described,
the discharge rate (with the valve fully open) falls from an initial 0.56 gm per second
in a typical case down to 0.36 gm per second, a fall of only 35% over this period.
Moreover, as shown in Figures 8, 9, 10 and 11, the mean particle size increases only
slightly as the pressure falls, and the distribution of particle sizes does not change
significantly at all. Figures 9, 10 and 11 have a logarithmic horizontal axis. It
will be seen that, when the pressure in the container was 9 bar (Figure 9), the predominant
particle size was about 50 micrometres, fifty per cent of them being of this size
or smaller and the discharge rate was measured at 0.64 gm/sec. When, as shown in the
graph of Figure 10, the pressure had fallen to 4.9 bar and the discharge rate to 0.44
gm/sec, the mean particle size had shifted only slightly. Figure 11 shows the position
when the pressure had fallen to 3.2 bar and it will be seen that the predominant particle
size is still only between 60 and 70 micrometres. The discharge rate has fallen to
0.34 gm/sec and, as mentioned above, the perceived wetness on the human skin is no
greater for a larger particle size where at the same time the rate of delivery onto
the skin has fallen.
[0033] Figure 8 is a graph obtained from a repeated series of tests like those of Figures
9, 10 and 11, and it will be seen that the median particle size only increased from
about 41 micrometres to about 60 micrometres as the amount of the product in the dispenser
fell from an initial 100% of the full charge down to 5%, ie. after 95% of the contents
had been dispensed.
[0034] All in all, the above test results show that the use of the fine channel or channels
in the nozzle of the spray button, representing the dominant restrictions in the flow
path and of dimensions significantly smaller than those used hitherto, has achieved
an acceptable spray quality throughout the useful life of the dispenser when using
a permanent gas as the propellant, yet without having to resort to expensive and unreliable
compensating devices. It is believed that this represents an important and unexpected
break through which advances substantially the ability to switch to non-CFC and non-hydracarbon
propellants without significant detriment to the acceptability of aerosols.
[0035] Whilst the above test results are those using nitrogen or air, similar results are
obtainable with nitrous oxide, and if carbon dioxide is used even better results are
obtained in the case of some products, by virtue of its partial solubility in many
mixtures.
[0036] Without departing from the invention one could provide a so-called 'vapour tap' of
a known kind in the valve housing, as indicated at 21 in Figure 1, and this could
be as small as, or even smaller than, the channels 20 but it is only in the path of
the gas, not the path of the liquid product.
[0037] In the example described the or each channel is formed in the back of a moulded insert,
made for example from acetal resin. However it will be understood that the particular
geometrical layout shown is by no means essential, and in practice the channels could
be formed in another way, for example in the top of the post onto which the insert
is pressed, or, as in some known spray buttons, one could dispense with a separate
insert altogether and make the spray button in one piece, complete with channels and
final orifice, although this could be very difficult to mould, bearing in mind the
very small cross-sections involved.
[0038] Moreover, for small discharge rates, for example in handbag size mini-dispensers
for perfume, even smaller dimensions than those specified may be used.
1. A pressurised dispenser comprising a container fitted with a manually operated
valve assembly equipped with a dip tube and having a spray tip (11) with at least
one outlet channel (20) leading to a spraying orifice (12) designed to produce a spray
of droplets of a liquid product from within the container under the action of a compressed
gas propellant, in which the propellant gas is a permanent gas, distinguished by the
feature that the cross-section of the or each channel (20) leading to the orifice
(12) is smaller than that of any other restrictions preceding it in the flow path
from the interior of the container to the orifice (12) and is not greater than 0.05
square millimetres.
2. A pressurised dispenser according to claim 1 in which the said cross-section is
not greater than 0.04 square millimetres.
3. A pressurised dispenser according to claim 2 in which the said cross-section is
not greater than 0.03 square millimetres.
4. A pressurised dispenser according to claim 1 in which the said cross-section lies
between 0.0225 and 0.04 square millimetres.
5. A pressurised dispenser according to any one of claims 1 to 4 in which there are
not more than two such channels (20,20′).
6. A pressurised dispenser according to claim 5 in which there is only one such channel
(20).
7. A pressurised dispenser according to any one of claims 1 to 6 in which the or each
channel (20) has a length which is at least four times its mean width.
8. A pressurised dispenser according to any one of claims 1 to 7 in which the or each
channel (20) is directed tangentially into a swirl chamber which leads to the spraying
orifice (12).
9. A pressurised dispenser according to any one of claims 1 to 8 in which the spraying
orifice (12) is round and has a diameter which is not greater than 250 micrometres.
10. A pressurised dispenser according to claim 9 in which the diameter of the spraying
orifice (12) is substantially 200 micrometres.
11. A pressurised dispenser according to claim 9 or claim 10 in which the length of
the orifice (12) is less than its diameter.
12. A pressurised dispenser according to any one of claims 1 to 11 in which the pressure
in the container is initially of the order of 9 bar and falls to around 3 bar by the
time 95% of the product within it has been dispensed.
13. A spray tip assembly for a pressurised dispenser according to claim 1 having at
least one outlet channel (20) leading to a spraying orifice (12) designed to produce
a spray of droplets, in which the cross-section of the or each channel (20) is not
greater than 0.05 square millimetres.
14. An insert for fitting to a spray tip (11) to form a spray tip assembly according
to claim 13 and having a spraying orifice (12) and, leading to it, at least one groove
designed (20) to co-operate with a face on the spray tip (11) to form the or each
said channel, the groove having a width and depth not exceeding 220 micrometres.
15. An insert according to claim 14 in which the groove (20) has a length at least
four times its width.