[0001] This invention relates to a powder flow control valve and to a method of controlling
powder flow.
[0002] The term "powder" as used herein refers to materials made up of discrete particles.
As will be clear from the description below the term includes a relatively fine powder
such as flour and also a granular material such as granulated salt (5 mm maximum
particle dimension) or agglomerated coffee powder (3 mm maximum particle dimension).
[0003] When a container is to be filled with a powder, it may be desirable to measure the
weight of powder accurately. For example in the food industry it may be necessary
to fill a container with a measured weight of powder such as coffee or milk powder.
It is desirable that the measurement of the weight of powder should be as accurate
as possible since a minimum quantity of powder must be provided in the container but
once that minimum weight is reached any extra powder in the container is wasted.
[0004] Various problems have to be overcome in producing an accurate measurement of the
powder but one problem is providing a valve that can operate reliably over a prolonged
period and that is not too difficult to maintain and in particular clean. The valve
may also have to be sterilisable.
[0005] According to the invention there is provided a powder flow control valve in which
a powder flow path is surrounded by a perforated boundary surface and means are provided
for creating a drop in pressure across the boundary surface with the higher pressure
on the powder flow path side of the boundary surface.
[0006] When the pressure drop is created powder flowing through the valve is drawn towards
the boundary surface and held there so that flow of powder through the valve is terminated.
A major advantage of this design is that there need be no moving parts in the powder
flow path resulting in a very simple design which is also easy to clean.
[0007] The means for creating a drop in pressure across the boundary surface preferably
operates by reducing the pressure on the opposite side of the boundary surface to
the powder flow path without reducing (or without reducing so much) the pressure
along the powder flow path. Alternatively, but less desirably, it could operate by
increasing the pressure along the powder flow path without increasing (or without
increasing so much) the pressure on the opposite side of the boundary surface.
[0008] The cross-sectional area of the flow path surrounded by the perforated boundary
surface preferably decreases in the downstream direction.
[0009] Preferably the boundary surface has rotational symmetry and preferably includes a
substantially frusto-conical portion with the smaller diameter portion downstream
of the large diameter portion. In use the portion of the powder flow path surrounded
by the perforated boundary surface is advantageously substantially vertical.
[0010] The precise dimensions and shape of the boundary surface may be chosen by experiment
and different dimensions and shapes may be used for different powders. In this way
the valve may be used to control the flow of a wide variety of powders including,
for example, flour, powdered milk, agglomerated coffee powder and granulated salt.
[0011] The perforated boundary surface may be made of a porous material, for example sintered
metal powder, glass or a plastics material, or may be made by a component with apertures
formed therein at a multiplicity of predetermined locations. In the latter case the
locations are preferably evenly distributed around the boundary surface.
[0012] In addition to providing means for creating a pressure drop across the boundary surface
with the higher pressure on the powder flow path side of the boundary surface means
may be provided for creating a pressure rise across the boundary surface with the
lower pressure on the powder flow path side of the boundary surface. When the pressure
rise is created powder flowing through the valve is inhibited from adhering to the
boundary surface or forming a stable arch. This technique of preventing powder sticking
to a surface is already known
per se but its use in a valve according to the invention is original.
[0013] According to another aspect of the invention there is provided a method of controlling
the flow of a powder in which a portion of the path along which powder flows is surrounded
by a perforated boundary surface and powder flow is stopped by creating a drop in
pressure across the boundary surface with the higher pressure on the powder flow path
side of the boundary surface.
[0014] By way of example a powder flow control valve embodying the invention will be described
with reference to the accompanying drawing which is a side sectional view of the valve.
[0015] The control valve 1 is sited at the bottom of a shaft 2 of circular cross-section
and includes a frusto-conical part 3 made of porous plastics material which in this
particular example is that sold by Porvair Ltd. under the trademark VYON. Immediately
below the frusto-conical part 3 is a cylindrical part 4 leading to an outlet 5 of
the valve. A plenum chamber 6 is defined between the outside of the frusto-conical
part 3 and the walls of the shaft 2. The plenum chamber 6 is connected to a pumping
system when can be arranged to suck air out of, or force air into, the chamber 6.
The pumping system comprises a duct 11 which is connected, on the one hand, via a
duct 7 and a valve 8 to a reservoir 9 of low pressure air maintained at low pressure
by a pump 10 and, on the other hand, via a duct 12 and a valve 13 to a compressed
air cylinder 14.
[0016] In use, powder is supplied to the top of the shaft 2 and falls down the shaft. When
the valve 8 is open and the valve 13 closed, air is sucked out of the plenum chamber
6 and into the reservoir 9. Consequently, air is caused to flow from the shaft through
the frusto-conical part 3 into the chamber 6 and this causes powder to adhere to
the surface of the part 3 and no powder reaches the outlet 5; this situation corresponds
to the "closed" state of the valve. If, on the other hand, the valve 8 is closed and
the valve 13 opened then air is blown into the plenum chamber 6 from the cylinder
14, the air flow through the part 3 is reversed and powder is prevented from sticking
to the part 3 and falls through the outlet 5; this situation corresponds to the "open"
state of the valve.
[0017] The valve 1 can therefore be used very effectively to control powder flow.
[0018] One particular example of a valve and powder that have been used successfully together
will now be described. In this example the shaft 2 had an internal diameter d of
60 mm, the frusto-conical part 3 had a height h of 42 mm and a minimum internal diameter
d₂ of 15 mm. The inclination α of the frusto-conical boundary surface to the horizontal
was 60°. The powder used was agglomerated coffee which when subjected to a sieve analysis
gave the results shown in the table below:

[0019] The porous material defining the boundary surface had a mean pore size of 70 microns
and a thickness of 4.75 mm. The thickness is not however believed to be particularly
significant. The porous material allowed a flow of air of 3.5 cm³/m²/min at a pressure
of 3 kN/m².
[0020] In the "closed" state of the valve, the pressure in the plenum chamber 6 was 15"
Hg (about 51 kN/m²) below atmospheric pressure and there was an air flow rate of
48 litres per minute (at atmospheric pressure). In the "open" state of the valve,
the pressure in the plenum chamber was 6 psi (about 41 kN/m²) above atmospheric pressure
and there was an air flow rate of 47 litres per minute (at atmospheric pressure).
[0021] The same valve was also tested with powdered milk and proved entirely satisfactory.
Nonetheless it should be understood that the dimensions of the valve may need to be
altered for different powders and in particular the dimensions d₂ may need to be varied.
It is also possible to omit the cylindrical part 4 at the outlet of the valve without
affecting the operation of the valve.
[0022] Tests have also been performed on powdered coffee, freeze dried coffee, household
salt, granulated salt, coffee creamer, talc and flour and the valve of the invention
has proved able to handle all these materials.
[0023] While in the described embodiments of the valve, the boundary surface is frusto-conical,
other shapes of boundary surface could be employed. For example a surface of inverted
pyramid shape could be used, or even a cylindrical shape.
[0024] Although the valve has been described almost exclusively in relation to controlling
the flow of food powders it will be understood that applications of the valve may
also be found outside the food industry.
1. A powder flow control valve in which a powder flow path is surrounded by a perforated
boundary surface and means are provided for creating a drop in pressure across the
boundary surface with the higher pressure on the powder flow path side of the boundary
surface.
2. A valve as claimed in claim 1 in which the means for creating a drop in pressure
across the boundary surface operates by reducing the pressure on the opposite side
of the boundary surface to the powder flow path without reducing, or without reducing
so much, the pressure along the powder flow path.
3. A valve as claimed in claim 1 or 2 in which the cross-sectional area of the flow
path surrounded by the perforated boundary surface decreases in the downstream direction.
4. A valve as claimed in any preceding claim in which the boundary surface has rotational
symmetry.
5. A valve as claimed in claim 4 in which the boundary surface includes a substantially
frusto-conical portion with the smaller diameter portion downstream of the larger
diameter portion.
6. A valve as claimed in any preceding claim in which the portion of the powder flow
path surrounded by the perforated boundary surface is substantially vertical.
7. A valve as claimed in any preceding claim in which the perforated boundary surface
is made of a porous material.
8. A valve as claimed in any of claims 1 to 6 in which the perforated boundary surface
is provided by a component with apertures formed therein at a multiplicity of predetermined
locations.
9. A valve as claimed in claim 8 in which the locations are evenly distributed around
the boundary surface.
10. A valve as claimed in any preceding claim further including means for creating
a pressure rise across the boundary surface with the lower pressure on the powder
flow path side of the boundary surface.
11. A method of controlling the flow of a powder in which a portion of the path along
which powder flows is surrounded by a perforated boundary surface and powder flow
is stopped by creating a drop in pressure across the boundary surface with the higher
pressure on the powder flow path side of the boundary surface.
12. A method as claimed in claim 11 in which the drop in pressure is created by reducing
the pressure on the opposite side of the boundary surface to the powder flow path
without reducing, or without reducing so much, the pressure along the powder flow
path.
13. A method as claimed in claim 11 or 12 in which the cross-sectional area of the
flow path surrounded by the perforated boundary surface decreases in the downstream
direction.
14. A method as claimed in any of claims 11 to 13 in which the boundary surface has
rotational symmetry.
15. A method as claimed in claim 14 in which the boundary surface includes a substantially
frusto-conical portion with the smaller diameter portion downstream of the larger
diameter portion.
16. A method as claimed in claim 14 or 15 in which the portion of the powder flow
path surrounded by the perforated boundary surface is substantially vertical.
17. A method as claimed in any of claims 11 to 16 in which the perforated boundary
surface is made of a porous material.
18. A method as claimed in any of claims 11 to 17 in which the perforated boundary
surface is provided by a component with apertures formed therein at a multiplicity
of predetermined locations.
19. A method as claimed in claim 18 in which the locations are evenly distributed
around the boundary surface.
20. A method as claimed in any of claims 11 to 19 further including the step of creating
a pressure rise across the boundary surface with the lower pressure on the powder
flow path side of the boundary surface.