[0001] The present application relates to a valve assembly. In particular, the present application
relates to a valve assembly for controlling flow of particulate material.
[0002] Conventional mechanical valves, for example gate valves or ball valves, can have
problems with rapid erosion and shortened life spans when particulate material such
as sand is flowed through them, leading to failure to seal effectively or jamming
of moving parts among other detrimental effects.
[0003] Research papers
Characterization of powder flowability using measurement of angle of repose (
Geldart D., Abdullah, E. C., Hassanpour A., Nwoke L. C., and Wouters, I., China Particuology
4 (2006) 104-107);
Characterisation of dry powders (
Geldart D., Abdullah E. C., and Verlinden A., Powder Technology 190 (2009) 70-74); and
Measuring the flowing properties of powders and grains (
Lumay, G., Boschini, F., Traina K., Bontempi S., Remy J-C., Cloots R., and Vandewalle
N., Powder Technology 224 (2012) 19-27) are useful for understanding the invention.
SUMMARY OF THE INVENTION
[0004] According to the present invention there is provided a valve assembly for controlling
flow of particulate material, the valve assembly having a storage chamber adapted
to retain particulate material, said storage chamber having an inlet to receive particulate
material and an outlet to dispense the particulate material from the storage chamber;
wherein the valve assembly comprises an outlet control member adapted to receive and
retain particulate material dispensed from the outlet of the storage chamber, said
outlet control member being spaced apart from the outlet of the storage chamber; wherein
particulate material dispensed from the outlet of the storage chamber is adapted to
accumulate on at least one surface of the outlet control member and to at least partially
block the outlet of the storage chamber, resisting flow of particulate material from
the outlet; wherein the outlet control member and the storage chamber are movable
relative to one another to disrupt accumulated particulate material on the outlet
control member and unblock the outlet of the storage chamber.
[0005] Optionally the disruption of the accumulated material on the outlet control member
disrupts the particulate material occluding the outlet and clears the outlet so that
particulate material can flow more freely from the storage chamber through the outlet.
Thus the outlet can be blocked and unblocked by switching the outlet control member
and the storage chamber between different states of relative movement. This allows
more reliable switching between open (when the outlet is unblocked and the particulate
material flows freely) and closed (when the outlet is at least partially blocked and
the particulate material has at least some resistance to flow) states of the storage
chamber.
[0006] Optionally the storage chamber and the outlet control member are separated from one
another, optionally by a clear space between them whether the outlet of the valve
is blocked or unblocked, and thus are not directly connected, but optionally the storage
chamber and the outlet control member may be indirectly connected. The clear space
between the storage chamber and the outlet control member when the valve outlet is
both blocked and unblocked allows the accumulation of the particulate material on
the outlet control member while the outlet of the storage chamber is clear, until
the accumulation of the particulate material on the outlet control member has occluded
the outlet of the storage chamber.
[0007] Optionally the storage chamber comprises walls that are at least partially inclined.
Optionally the walls of the storage chamber are flat. Optionally the walls of the
storage chamber are curved. Optionally the storage chamber comprises a funnel, optionally
leading to the outlet. Optionally the inlet of the storage chamber comprises a larger
cross-sectional area than the outlet of the storage chamber, or optionally the inlet
comprises a smaller cross-sectional area than the outlet. The ratio between the cross-sectional
area of the inlet relative to the outlet can be adjusted to suit the particulate material
that is being flowed through the storage chamber, and optionally to further control
the flow rate of the particulate material through the storage chamber. Optionally
the two cross-sectional areas are equal. Optionally the storage chamber comprises
a hopper. Optionally the particulate material flows from the outlet of the storage
chamber to the outlet control member under gravity. Optionally the particulate material
is at least partially fluidised. Optionally the storage chamber is manufactured from
metal, or optionally from a composite or ceramic material.
[0008] Optionally the storage chamber comprises an outlet compartment, optionally in the
form of a shroud disposed at the lower end of the storage container, optionally a
rectangular shroud, but this may be formed in any suitable shape. Optionally the outlet
control member is contained within the shroud. Optionally the outlet control member
is movable within the shroud, optionally relative to the shroud. Optionally the shroud
is made of the same material as the storage chamber, or optionally the shroud is made
of a different material. Optionally the shroud is insulated, and the thickness of
the insulation is optionally selected taking into account parameters such as the conductivity
of the insulating material, and the temperature gradient from inside the storage chamber
to outside the storage chamber. Optionally, one possible example of the insulation
is 50mm thick ceramic fibre insulation. Optionally the shroud is connected to the
storage chamber with fixings such as bolts, or optionally rivets, or optionally by
welding, or optionally any combination thereof.
[0009] Optionally the shroud comprises an outlet tube connected to a base portion of the
shroud. Optionally particulate material that is disrupted and released from the outlet
control member as a result of relative movement of the outlet control member and the
storage chamber falls under gravity to the base of the shroud and into the outlet
tube. Optionally the outlet tube is angled. Optionally the outlet tube dispenses the
particulate material for further processing or optionally for recycling back into
the system. Optionally the outlet tube extends at least partially into the shroud.
Optionally the outlet tube is attached to the external surface of the base of the
shroud, optionally by welding, riveting, bolting, or any other suitable fixing.
[0010] Optionally the outlet control member has an at least partially concave shape. Optionally
the outlet control member comprises a base and at least one wall. Optionally the outlet
control member has at least one channel for directing flow of particulate material
off the outlet control member; optionally the channel can comprise an edge that does
not comprise a wall, or that comprises a lower wall than other edges. Optionally the
channel faces away from the storage chamber and is adapted to direct flow of particulate
material away from the outlet control member. Optionally at least a portion of the
base of the outlet control member comprises a plate. Optionally the outlet control
member comprises a bed, which may comprise a partially walled plate.
[0011] Optionally at least a portion of the base of the outlet control member is inclined
relative to a horizontal axis. Optionally at least a portion of the base of the outlet
control member is inclined downwards, for example, at an angle between 0°-90° relative
to a horizontal axis. Optionally at least a portion of the base of the outlet control
member is inclined downwards at an angle in the range of 0°-40° relative to a horizontal
axis. Optionally at least a portion of the base of the outlet control member is inclined
downwards at an angle in the range of 10°-20° relative to a horizontal axis.
[0012] Optionally the outlet control member comprises a first plate and a second plate,
wherein the first and second plates are optionally inclined (optionally downwards)
at different angles relative to a horizontal axis. Optionally the first plate of the
outlet control member is inclined at a steeper angle than the second plate relative
to the horizontal axis. Optionally the first plate is inclined at a more shallow angle
than the second plate relative to the horizontal axis. Optionally the second plate
of the outlet control member has a greater surface area than the first plate of the
outlet control member.
[0013] Optionally the interface or transition between the first plate and the second plate
of the outlet control member is disposed beneath the outlet of the storage chamber,
optionally centrally relative to the outlet of the storage chamber.
[0014] Optionally, where the first plate is inclined at a shallower angle than the second
plate relative to the horizontal axis, the interface or transition between the two
plates is convex. Utilising a convex arrangement leads to a reduction in mass of accumulated
particulate material on the plate, which allows a given vibrating power to produce
a larger amplitude of vibration. This enhances the rate of flow of particulate material
off the plate, and reduces the energy required to flow the particulate matter. By
minimising the energy consumption, the overall effect of the renewable energy harvesting
is maximised.
[0015] Optionally the outlet control member comprises a single flat plate, optionally forming
a base for receiving and retaining particulate material. Optionally the flat plate
is surrounded at least partially by a vertical wall or walls. Optionally the flat
plate is not inclined relative to the horizontal axis. Optionally the flat plate is
surrounded on two parallel sides by walls adapted to retain particulate material received
by the flat plate. Optionally the flat plate is surrounded by walls such that there
is a single channel for directing flow of particulate material off the outlet control
member.
[0016] Optionally the outlet control member comprising a single flat plate has at least
one channel, optionally two channels, for directing flow of particulate material off
the outlet control member; optionally the channel or channels can comprise an edge
that does not comprise a wall, or that comprises a lower wall than other edges. Optionally
the channel or channels face away from the storage chamber and is/are adapted to direct
flow of particulate material away from the outlet control member. Optionally the outlet
control member comprises two channels on opposite sides of the flat plate. Optionally
the flat plate does not comprise walls and particulate material can flow from the
flat plate in any direction.
[0017] Optionally at least a portion of the flat plate is inclined at an angle, optionally
downwards, relative to the horizontal axis. Optionally the whole plate is inclined
at the same angle. Optionally the plate is inclined at an angle between 0-30° relative
to the horizontal axis, optionally approximately 15°.
[0018] Inclining the plate offers the advantage that resistance to flow of the particulate
material is lowered due to the inclination of the plate, and any movement of the plate
results in an "avalanche" effect, giving rise to high flow of particulate material
relative to the energy expended.
[0019] Optionally the outlet control member is in the form of a plurality of plates, optionally
vertically stacked one above another, optionally in a mutually parallel arrangement.
Optionally at least one, and optionally each, of the plurality of stack plates is
flat. Optionally at least a part of at least one or more of the plates is arranged
on the horizontal axis. Optionally at least one plate comprises a flat solid plate
with no edges. Optionally at least one plate comprises a convex plate with no edges,
optionally the plate at the base of the vertical stack of plates. Optionally the base
plate comprises a conical or similar shape.
[0020] Optionally at least one plate incorporates at least one aperture to permit flow of
particulate material through the plate to the plate directly underneath it under gravity.
[0021] Optionally each stack plate above the base plate comprises an aperture, optionally
more than one aperture.
[0022] Optionally the aperture in the or each plate comprises a large cross-sectional area
relative to the cross-sectional area of the plate. Optionally the or each aperture
is arranged directly underneath the outlet of the storage chamber, and optionally
centrally to the or each plate. Optionally the apertures in adjacent plates are aligned.
Optionally the or each plate comprises at least one edge with no raised walls or barriers
to the flow of particulate material. Optionally particulate material can flow off
the or each plate in all directions, i.e. substantially 360° around the or each plate.
[0023] Optionally the edge of the mound of particulate material flowing from the storage
chamber onto the plurality of plates comes to rest at or very close to the edge of
each plate. The proximity of the particulate material to the edge of each plate results
in less energy being required to flow the particulate material off each plate. Optionally
the edge of the plate from which the particulate material drops is spaced from the
edge of the mound of particulate material when the outlet is occluded. Spacing the
edge of the plate or plates from the edge of the mound of particulate material, such
that there is a margin between the edge of the particulate material and the edge of
the plate or plates, assists with rapid occlusion of the valve outlet when it is necessary
to stop the flow of particulate material through the outlet.
[0024] The particulate material optionally accumulates on the outlet control member in a
mound with an apex and with sides of the mound adopting a resting angle of repose,
at which the mound is stable on the outlet control member and wherein the apex of
the mound gradually builds up to occlude the outlet of the storage chamber. The angle
of repose of the particulate material is dependent on various parameters of the material
and the system, for example, frictional coefficient of the powder, mass of the powder,
angle of the base of the outlet control member etc. The angle of the base of the outlet
control member is usefully less than the corresponding angle of repose for the particular
powder material, so that the sides of the mound build up at a steeper angle than the
base of the outlet control member.
[0025] The arrangement of the plurality of plates with central apertures offers a greater
flow area with a smaller mass of particulate material around the edges of each plate
acting to restrict flow of particulate material disposed further towards the centre
of the plate arrangement. The total mass of particulate material accumulated on the
plate arrangement may optionally be equal to or optionally greater than the total
mass accumulated on one of the other examples of the apparatus, however, as this mass
is distributed across multiple plates, this reduces the resistance of the particulate
material to disruption and flow off each plate. This offers the advantage that for
an equivalent mass of particulate material, lower vibrational power is required to
disrupt the accumulated material. As lower power is required, this results in lower
consumption of energy.
[0026] Optionally the particulate material is hot particulate material, which can be heated
before being received in the storage chamber. Optionally the particulate material
is heated by a heating system that is powered by renewable energy, supplying intermittent
power, optionally harvested by a photovoltaic system, or optionally by wind, tidal,
or wave systems. Optionally the heating system is electrically connected to an array
of solar cells and/or modules. Optionally the heating system is electrically connected
to at least one wind or tidal turbine, or at least one other form of hydroelectric
energy harvesting. Optionally the particulate material is heated to several hundred
degrees Celsius, for example 500-700°C dependent on the material being used. Optionally
at least a part of the storage chamber is at least partially insulated, and is adapted
to resist heat exchange or loss between the heated particulate material and the environment
surrounding the valve assembly. Optionally the particulate material stacks on the
or each outlet control member at an angle of repose of approximately 30°.
[0027] Optionally the particulate material is heated by solar energy, and can be directly
heated in a concentrated solar power system having mirrors or lenses to concentrate
solar energy on a small area containing the particulate material (or through which
the particulate material passes) to heat up the particulate material prior to passage
through the valve. The valve is thus optionally used to control the distribution of
heated particulate material, e.g. sand, which can then be routed to a heat engine
such as a steam turbine, to recover heat from the hot particulate material. Hence,
in certain aspects the particular material is used as a medium for the transfer of
renewable heat energy from the concentrated solar power system to the heat exchanger
for recovery of the heat energy contained in the particulate material.
[0028] Accordingly the invention also provides a concentrated solar power system incorporating
a valve assembly as defined herein.
[0029] Optionally the first plate of the outlet control member forms a connection with at
least one shaft optionally connected to the valve and optionally adapted to support
at least a portion of the valve. Optionally the storage chamber and the outlet control
member are mounted to different supports, and the storage member is optionally not
directly connected to or is isolated from the shaft; thus movement of the outlet control
member or the shaft is not directly transmitted to the storage member and vice versa.
This enhances the relative movement between the outlet control member and the storage
chamber when one of them is moved relative to the other. Optionally the storage chamber
and the outlet control member can be remotely connected together or to the same support
structure by the at least one shaft.
[0030] Optionally the valve assembly comprises at least one movement device, configured
to move the outlet control member relative to the storage member. Optionally the at
least one shaft connects the movement device and the storage device, and optionally
the shaft transmits movement between the movement device and the outlet control member.
[0031] Optionally, the movement is cyclic, and the movement device optionally comprises
an oscillatory device, optionally adapted to cyclically move one of the outlet control
member and the storage chamber relative to the other, and disrupt particulate material
that has accumulated on the outlet control member, and optionally that has occluded
the outlet of the storage chamber. Optionally the movement is elliptical. Optionally
the movement of the outlet control member is vibration. Optionally the movement device
is adapted to cyclically move, and optionally vibrate, the outlet control member in
one or more than one scenario and which may include:--
- i) when the outlet is clear, and optionally when particulate material is flowing through
the outlet to the outlet control member; and/or
- ii) when the outlet is blocked (to clear it).
[0032] Alternatively, the outlet control member remains static when the outlet is clear,
optionally when particulate material is flowing through the outlet, optionally so
that the particulate material accumulates on the outlet control member to block the
outlet. Optionally the connection of the outlet control member to either the at least
one shaft or to the movement device comprises a cantilever connection, and optionally
the second plate of the outlet control member is connected only to the first plate
of the outlet control member.
[0033] Optionally the outlet control member and optionally the movement device are connected
to at least one shaft. Optionally the shaft is flexible and optionally comprises a
flexible beam. Optionally the shaft extends from a fixed, optionally rigid foundation
disposed above, or optionally beside, or optionally beneath the storage chamber. Optionally
the shaft extends from the foundation and along the full height of the storage chamber.
Optionally the foundation is located beneath the storage chamber and the shafts extend
vertically upwards. Optionally the shaft is flexible and supports the outlet control
member so that the shaft can flex and the outlet control member can move. Optionally
the valve assembly comprises more than one shaft, optionally two. Optionally the shafts
incorporate or support conduits and supply power to move the movement member. Optionally
the free ends of the shafts, that is the ends that are not connected to the movement
member, are rigidly constrained by the foundation. Optionally the storage chamber
is also rigidly constrained, optionally by attaching at least a portion of the shaft
or shafts to the storage container.
[0034] Optionally the movement device is pneumatically powered, and the shafts optionally
comprise or support a fluid inlet tube and a fluid outlet tube. Optionally the outlet
control member is connected to the movement device, and the movement device is connected
to the at least one shaft.
[0035] Rigid constraint of the shafts ensures that the greatest proportion of the kinetic
energy present in the fluid as it is being flowed to the movement device is transferred
to the movement device itself.
[0036] Optionally the fluid inlet and fluid outlet tubes are connected to the movement device.
Optionally fluid, for example air, nitrogen gas, or vapours, e.g. steam, is flowed
into the movement device through the fluid inlet tube and out of the movement device
through the fluid outlet tube. Optionally the fluid inlet and outlet tubes are connected
to the movement device on its upper surface, but the tubes can also be connected in
other ways, for example, to a side or to the lower surface of the movement device
according to the internal configuration of the movement device. Optionally the fluid
inlet and outlet tubes are arranged with one tube connected to the movement device
on one side of the outlet control member, and one tube connected to the movement device
on the other side of the outlet control member. Optionally the air outlet tube comprises
an exhaust.
[0037] Optionally the movement device comprises a turbine. Optionally the turbine comprises
an out of balance weight. Optionally the movement device comprises at least one bearing
in a race, optionally a ball bearing, forming a bearing assembly. Optionally the movement
device is manufactured from metal, optionally stainless steel. Optionally the movement
device comprises a ceramic material; for example zirconia, silicon nitride, silicon
carbide. Optionally fluid flow into the movement device sets up an eccentric movement
within the device. Optionally fluid flow into the movement device causes cyclic rotational
movement of the air turbine or of the bearing. Optionally fluid flow into the movement
device drives the turbine and generates eccentric movement. Optionally fluid flow
into the movement device pushes the bearing around the race and leads to eccentric
movement of the movement device. Optionally the race is circular, or elliptical. Optionally
the race is arranged in a horizontal plane. Optionally the movement device generates
vibrations in a horizontal plane. Optionally the movement device generates vibrations
off the horizontal plane, optionally at an angle less than 30°. Optionally the movement
device is angled off the horizontal plane.
[0038] Optionally the movement device comprises a port, optionally in the wall of the connection
of the fluid inlet tube. Optionally fluid flows through the port and into the body
of the movement device. Optionally the moving part of the movement device, for example
the bearing, or the fluid turbine, is contained within at least a portion of the movement
device. Optionally the portion of the movement device restrains movement of the moving
part in a cyclic (e.g. a circular) path, or optionally an elliptical path. Optionally
the portion of the movement device comprises apertures to permit exit of fluid flow
away from the moving part of the movement device, optionally to maintain the fluid
within the device at a given pressure value, and flowing in a given direction.
[0039] Optionally the apertures pass through a wall, optionally a horizontal wall, of the
movement device, into a circular or optionally elliptical air outlet manifold. Optionally
fluid flows into the manifold and exits the movement device through a port in the
wall of the connection of the fluid outlet tube.
[0040] Optionally the movement of the movement device moves the outlet control member relative
to the storage member, which optionally remains static, but the in other examples
this arrangement can be reversed, or both the outlet control and the storage member
can be moved. Optionally the movement is vibration or oscillation. Optionally the
movement of the outlet control member is in one plane, for example towards and away
from the at least one shaft, or backwards and forwards. Optionally the movement of
the outlet control member is side to side. Optionally the movement of the outlet control
member can be in more than one plane. Optionally the movement of the outlet control
member disrupts the particulate material, and the particulate material optionally
falls from one end of the outlet control member, for example, via a low side of the
outlet control member, optionally onto the base of the shroud, or optionally into
a further container, or optionally the particulate material is directly dispensed
from the outlet control member. Optionally the particulate material is adapted to
flow or fall from more than one end or side of the outlet control member. Optionally
the particulate material is adapted to flow or fall from the full perimeter of the
outlet control member.
[0041] Optionally the movement device is arranged in close proximity to the outlet control
member. Optionally in the example of the apparatus where the outlet control member
comprises a plurality of plates, the movement device is optionally arranged in close
proximity to the plurality of plates. Optionally the movement device and the outlet
control member (e.g. the plurality of plates) are constrained to move together. Optionally
this effectively creates a point load, which advantageously reduces stress on the
connections between the movement device and the supporting structure for said movement
device. Optionally the movement device and the plurality of plates are held in a proximal
arrangement by an upper and a lower plate, the upper and lower plates optionally adapted
to vertically restrain the movement device and the plurality of plates while optionally
permitting horizontal movement. Optionally the movement device, plurality of plates,
and upper and lower plates are adapted to move as one unit. Optionally in the example
of the apparatus where the outlet control member comprises a single plate, or optionally
a first and second plate connected together at an interface, the movement device is
optionally connected to both the plate and the shaft. Optionally the outlet control
member (e.g. the plate) is connected to the movement device by a threaded fixing.
Optionally the connection of the plate and the movement device maintains the movement
device in close proximity to the plate and optionally adapts the plate and the movement
device arrangement to move as a single unit. The close proximity of the movement device
to plates reduces the overhang of mass from the shafts and acts to resist fatigue
in the metal or other material used to manufacture the apparatus and its fixings.
[0042] Optionally at least one movement device is connected to the storage chamber. Optionally
the movement device vibrates the storage chamber and disrupts the particulate material
therein, for example to release or disperse clumps or agglomerations of particulate
material supported on the outlet control member. Optionally at least one movement
device is connected to the storage chamber and at least one movement device is connected
to the outlet control member. Optionally the movement devices on the storage chamber
and on the outlet control member are operated at different times, or optionally at
the same time, according to the required flow rate of particulate material. For example,
operating both movement devices at the same time will increase the flow rate of particulate
material through the outlet of the storage chamber, into the outlet control member,
and away from the outlet control member. Optionally the movement devices are operated
in a synchronised manner, optionally in an asynchronous manner. Optionally the storage
member and the outlet control member can be moved at the same time in different planes,
or directions.
[0043] Optionally fluid flowing through the fluid inlet and outlet tubes and through the
movement device can be heated, for example, by the heat from the heated particulate
material. Optionally the heated fluid passes from the fluid outlet tube into a heat
exchanger device. Optionally the heat exchanger device comprises at least one cool
fluid intake. Optionally the cool fluid intake is separated from the intake of hot
fluid from the fluid outlet tube. Optionally as the cool fluid passes through the
heat exchanger, at least a portion of the heat from the hot fluid stream is transferred
to the cool fluid. Optionally the transfer of heat from the hot fluid stream creates
two separate warm fluid streams. Optionally one warm fluid stream is directed to the
valve for input into the movement device, and one warm fluid stream is output to,
for example, a heat engine such as a Stirling engine, where the heat from the fluid
is used to power the engine. Optionally the heat from the fluid is used to heat water
and create steam to provide power to an engine.
[0044] Pre-heating the warm fluid stream that is directed to the movement device reduces
the loss of thermal energy from the particulate material on the outlet control member
to the fluid, in turn reducing the energy that is required to be input into the system
to heat the particulate material.
[0045] According to the present invention there is also provided a method of controlling
flow of particulate material through a valve assembly, the method including flowing
the particulate material into a storage chamber through an inlet formed in said storage
chamber, wherein the storage chamber is adapted to retain particulate material; dispensing
the particulate material from the storage chamber through an outlet formed in the
storage chamber onto an outlet control member adapted to receive and retain particulate
material, the outlet control member being spaced apart from the outlet of the storage
chamber; accumulating particulate material on at least one surface of the outlet control
member; and at least partially occluding the outlet of the storage chamber with particulate
material that has accumulated on at least one surface of the outlet control member;
wherein the method includes moving one of the outlet control member and the storage
chamber relative to the other to disrupt accumulated particulate material on the outlet
control member and unblock the outlet of the storage chamber.
[0046] The various aspects of the present invention can be practiced alone or in combination
with one or more of the other aspects, as will be appreciated by those skilled in
the relevant arts. The various aspects of the invention can optionally be provided
in combination with one or more of the optional features of the other aspects of the
invention. Also, optional features described in relation to one aspect can typically
be combined alone or together with other features in different aspects of the invention.
Any subject matter described in this specification can be combined with any other
subject matter in the specification to form a novel combination.
[0047] Various aspects of the invention will now be described in detail with reference to
the accompanying figures. Still other aspects, features, and advantages of the present
invention are readily apparent from the entire description thereof, including the
figures, which illustrates a number of exemplary aspects and implementations. Any
subject matter described in the specification can be combined with any other subject
matter in the specification to form a novel combination. The invention is also capable
of other and different examples and aspects, and its several details can be modified
in various respects, all without departing from the scope of the present invention.
Accordingly, the drawings and descriptions are to be regarded as illustrative in nature,
and not as restrictive. Furthermore, the terminology and phraseology used herein is
solely used for descriptive purposes and should not be construed as limiting in scope.
Language such as "including", "comprising", "having", "containing", or "involving"
and variations thereof, is intended to be broad and encompass the subject matter listed
thereafter, equivalents, and additional subject matter not recited, and is not intended
to exclude other additives, components, integers or steps. Likewise, the term "comprising"
is considered synonymous with the terms "including" or "containing" for applicable
legal purposes. Thus, throughout the specification and claims unless the context requires
otherwise, the word "comprise" or variations thereof such as "comprises" or "comprising"
will be understood to imply the inclusion of a stated integer or group of integers
but not the exclusion of any other integer or group of integers.
[0048] Any discussion of documents, acts, materials, devices, articles and the like is included
in the specification solely for the purpose of providing a context for the present
invention. It is not suggested or represented that any or all of these matters formed
part of the prior art base or were common general knowledge in the field relevant
to the present invention.
[0049] In this disclosure, whenever a composition, an element or a group of elements is
preceded with the transitional phrase "comprising", it is understood that we also
contemplate the same composition, element or group of elements with transitional phrases
"consisting essentially of", "consisting", "selected from the group of consisting
of", "including", or "is" preceding the recitation of the composition, element or
group of elements and vice versa. In this disclosure, the words "typically" or "optionally"
are to be understood as being intended to indicate optional or non-essential features
of the invention which are present in certain examples but which can be omitted in
others without departing from the scope of the invention.
[0050] All numerical values in this disclosure are understood as being modified by "about".
All singular forms of elements, or any other components described herein are understood
to include plural forms thereof and vice versa. References to directional and positional
descriptions such as upper and lower and directions e.g. "up", "down" etc. are to
be interpreted by a skilled reader in the context of the examples described to refer
to the orientation of features shown in the drawings, and are not to be interpreted
as limiting the invention to the literal interpretation of the term, but instead should
be as understood by the skilled addressee.
BRIEF DESCRIPTION OF THE DRAWINGS
[0051] In the accompanying drawings:
Figure 1 shows a perspective view of the valve assembly;
Figure 2 shows a close-up view of the outlet control member underneath the outlet
of the storage chamber;
Figure 3 shows a side view of the valve assembly with lower section A circled;
Figure 4 shows a close-up view of the lower section A as highlighted in Figure 3;
Figure 5 shows the valve assembly of Figure 1 with a shroud attached to the lower
portion of the storage chamber;
Figure 6 shows a side view of the outlet control member and shaft assembly without
the storage chamber;
Figure 7 shows a perspective view of Figure 6;
Figure 8 shows a close-up view of an example of the movement device;
Figure 9 shows a close-up view of a horizontal cross-section of the movement device
of Figure 8;
Figure 10 shows a vertical cross-section of the movement device of Figures 8 and 9;
and
Figure 11 shows a fluid flow pathway through the movement device of Figures 8-10 and
flowing through a heat exchanger
Figure 12 shows a side view of a further example of the outlet control member in the
form of a flat plate parallel to the horizontal axis;
Figure 13 shows a side view of a further example of the outlet control member in the
form of a flat plate incline relative to the horizontal axis;
Figure 14 shows a side view of a further example of the outlet control member in the
form of two plates joined together at a convex angle, both plates inclined relative
to the horizontal axis;
Figure 15 shows a side view of a further example of the outlet control member in the
form of a plurality of flat plates disposed parallel to the horizontal axis;
Figure 16 shows a perspective view of an example of the outlet control member with
multiple plates;
Figure 17 shows an exploded view of the example of Figure 16;
Figure 18 shows a close-up view of the outlet control member with multiple plates,
in position next to the movement member; and
Figure 19 shows the calculation of curtain area for the example of the outlet control
member illustrated in Figure 14.
DETAILED DESCRIPTION OF EXAMPLES OF THE INVENTION
[0052] Referring now to the drawings, a valve assembly 1 comprises a storage chamber, in
this example in the form of a hopper 10, adapted to retain particulate material, in
this example powder 28, but sand, grit, flour, granules, grains, or other particulate
materials can be used, and "powder" is merely used here as a general term. The hopper
10 comprises an inlet 15, adapted to receive the powder 28 into the body 11 of the
hopper 10, and an outlet 14 to dispense the powder 28 from the lower, funnelled section
12 of the hopper 10. The valve assembly 1 comprises an outlet control member, in one
example, herein described, in the form of a bed 20 forming a platform underneath the
outlet 14 of the hopper 10, adapted to receive and retain powder 28 dispensed from
the outlet 14 of the hopper 10. Other examples of the outlet control member will be
described in detail later in the description. The bed 20 is spaced apart from the
outlet 14 of the hopper 10, with clearance between the outlet 14 and the bed 20 of
around, for example, 5-50mm, but optionally greater or lesser spacing dependent on
the parameters of the particulate material, the plates, and the relative angles thereof.
Powder 28 dispensed from the outlet 14 of the hopper 10 accumulates on at least one
surface of the bed 20, in this example on first 21 and second 22 sections of the base
of the bed 20, which are each arranged at non-horizontal angles underneath the outlet
14. The first and second plates 21, 22 are canted at different angles; in this case,
the first plate 21 is canted at a steeper angle than the second plate 22, as best
seen in the side view of Figure 4. As the powder 28 accumulates on the first and second
plates 21, 22, it is retained on the bed 20 by side wall 25 extending upwards from
the first and second plates 21, 22 around a part of the circumference of the bed 20,
but in this case, the wall 25 is not entirely continuous around the bed 20, and at
one side the bed 20 has an outlet 20o which is not bounded by the wall 25, and at
which the powder 28 is free to fall from the bed 20. In this example, the outlet 20o
is at the open side of the second plate 22. The first and second plates 21, 22 of
the base of the bed 20 are both canted downwards towards the outlet 20o of the bed
20, at different angles. The side walls 25 retain the powder on the bed 20, but at
the outlet 20o, the powder is relatively unconstrained and so preferentially falls
from the bed 20 at the outlet 20o. By this arrangement the powder 28 accumulating
on the bed 20 gradually rises in a mound underneath the outlet 14 until the upper
tip of the mound extends into and at least partially occludes the outlet 14 of the
hopper 10. As the mound of powder 28 on the bed 20 grows and occludes the outlet 14,
it reduces the open surface area of the outlet 14, and resists flow of further powder
28 from the outlet 14. The bed 20 and the hopper 10 generally remain static with respect
to one another when powder 28 is supported by the bed 20, so in this phase, with the
bed 20 accumulating powder 28 prior to occlusion, or with the outlet 14 blocked by
the tip of the mound, the outlet control member does not move relative to the storage
chamber or vice versa. When the outlet 14 is to be unblocked, the accumulated powder
28 is disrupted by relative movement of the bed 20 and the hopper 10, and the bed
20 relative to the ground, as will now be described.
[0053] Figure 1 shows the valve assembly 1 connected to a supporting structure comprising
a parallel arrangement of rails forming a supporting frame 3, with the inlet 15 connected
to a lid 16 covering over the hopper body 11. Here the lid 16 is bolted on to the
hopper body 11. Optionally, if cold powder is being flowed into the hopper 10, it
is not necessary to include a lid and the hopper 10 can be uncovered. Optionally when
the powder is heated, a lid can be used, and optionally the lid can be insulated.
The inlet 15 is in the form of a tube or a pipe in this example, which can comprise
a straight or an angled connection to the powder input. The powder 28 flows into the
hopper 10 via a supply line (not shown) connected to the inlet 15 into the body 11
of the hopper 10 and into a funnelled lower section 12, where at least one (and optionally
more than one) of the hopper walls is inclined in a downwards direction, and is optionally
generally flat. The funnelled section 12 is in this example a separate section from
the body of the hopper 11, connected to the body 11 of the hopper by fixings such
as bolts or rivets, but could alternatively be integral with the body 11. The bed
20 is positioned underneath the outlet 14, leaving a clearance between the upper edges
of the bed 20 and the lower surfaces of the outlet 14, and provides a surface on which
the powder accumulates after falling from the outlet 14. The bed 20 is spaced apart
from the outlet 14 to allow the powder to build up into a heap or a mound, and thus
the hopper 10 and the bed 20 are not connected.
[0054] In this example, and as best seen in Figure 1, the inlet 15 of the hopper 10 comprises
a smaller cross-sectional area than the outlet 14 of the hopper 10. The powder 28
flows from the outlet 14 of the hopper 10 onto the bed 20 under gravity.
[0055] Figure 2 shows the bed 20 comprising a base having flat first plate 21 and flat second
plate 22 forming the base of the bed 20. The first plate 21 is generally semicircular,
and the second plate 22 is generally trapezoidal, with two parallel sides, the narrower
of which transitions into the first plate 21, and the wider of which forms the outlet
20o at the lower side of the bed 20, unconstrained by the wall 25. The base of the
bed 20 is inclined downwards relative to a horizontal axis x-x (best seen in Figure
4), at an angle in the range of 10°-20° with respect to the horizontal axis x-x, but
the angle can be greater or smaller depending on the type of powder and its frictional
coefficients, for example. The angle of the bed 20 with respect to the horizontal
plane is usefully less than the angle of repose for the particular powder material.
In this example, the angle of repose shown is 30°. The first plate 21 and the second
plate 22 of the base of the bed 20 are each inclined at different angles relative
to the horizontal axis x-x. The first plate 21 of the bed 20 is inclined at a steeper
angle than the second plate 22 relative to the horizontal axis. The transition between
the first plate 21 and the second plate 22 is in this example positioned directly
underneath the outlet 14 of the hopper 10, optionally slightly off-centre, so that
the central vertical axis of the outlet 14 is slightly in front of the transition
between the first plate 21 and the second plate 22, closer to the outlet of the relative
to the outlet 14, directly above the second plate 22 with the shallower angle. The
first plate 21 has a greater surface area than the second plate 22. The wall 25 extends
partially around the first 21 and second 22 sections of the base, leaving a space
at the outlet 20o of the second plate 22 to form a channel for directing flow of accumulated
powder 28 off the bed 20. The channel faces away from the hopper 10 and is adapted
to direct the accumulated powder 28 away from the bed 20.
[0056] The bed 20 is connected to a movement device, which in this example comprises an
oscillatory device driving the bed 20 in cyclic movements or vibrations, and here
comprising a bearing assembly 40, but can instead comprise an air turbine or similar
device. On one side of the connection there is a fluid inlet conduit in the form of
an air inlet tube 51 which connects to the bearing assembly 40 and flows air into
the bearing assembly 40. Any type of industrial air can be used to drive the bearing
assembly 40. On the other side, there is optionally an air outlet conduit in the form
of a tube 52 through which the air flows out of the bearing assembly 40. This will
be discussed in more detail below. The outlet is not essential and can be omitted
in some examples. However, it is useful to divert air flow away from the mound of
powder on the outlet control member in some examples.
[0057] The hopper 10 is connected to a supportive brace 55, as seen in Figure 3. In this
example, the two tubes 51,52 are fixed to the hopper 10 structure, but in other examples,
they could alternatively be fixed to another supporting structure. The brace 55 is
bolted to the hopper and provides a passageway for the fluid inlet and outlet tubes
51, 52, which are disposed within the brace 55, and pass up the external surface of
the rear wall of the hopper 10, where the term "rear" is used here merely for clarity
in relation to the drawings. In this example the rear wall of the hopper 10 is vertical
for ease of fixing of the hopper 10 to the brace, and the remaining three walls of
the funnelled section 12 are inclined downwards.
[0058] The area A circled in Figure 3 is shown close-up in Figure 4. Figure 4 shows a schematic
illustration of the accumulation of a mound of powder 28 on the bed 20 and occlusion
of the outlet 14 by the mound of powder 28. The powder 28 is funnelled by the funnelled
lower section 12 of the hopper 10 out of the hopper 10 via the outlet 14. The clear
space between the lower extent of the outlet 14 and the upper extent of the bed 20
allows space for the accumulation of the powder 28 on the bed 20 while the outlet
14 of the hopper 10 is clear. After a given period of time, the accumulated powder
28 builds up sufficiently to begin to occlude or block the outlet 14, and slow down
or resist the flow of more powder 28 out of the hopper 10 and onto the bed 20.
[0059] The powder 28 can be heated before it is received by the hopper 10. The energy required
for heating the powder 28 can be provided by renewable sources. For example, a photovoltaic
system such as a solar array could be used to transfer electrical energy harvested
by the array to a heating system. The powder 28 is optionally heated to temperatures
of several hundred degrees Celsius, for example around 600°C, although this can be
higher or lower depending on the properties of the materials involved. In order to
maintain the temperature and to resist loss of heat from the powder 28 into the environment
around the hopper 10, the hopper 10 is at least partially insulated. In this example,
all walls of the hopper 10 and the lid of the hopper 16 comprise a layer of insulation.
The hopper inlet 15 (and any pipes feeding it) can also be at least partly insulated
for a portion of its length.
[0060] The bed 20 is connected to the bearing assembly 40 by a fixing which here comprises
a nut and bolt 26, which passes through an orifice 49 in the body of the bearing assembly
40 (best seen in Figure 10). In other examples, the bed could be formed integrally
with the bearing assembly, or it could be welded to at least a portion of the bearing
assembly. The bolt optionally does not protrude into the base of the bed 20, and is
instead welded or received into a blind threaded socket on the lower surface of the
first portion 21 of the bed 20, thus avoiding interference with the accumulation of
the powder 28 on the top of the bed 20 and the subsequent disruption thereof. The
bed 20 is thus directly connected to the movement device at one end, by a cantilever
connection, and this permits some minor flexing in a vertical direction, amplified
by the weight of the powder 28 as it accumulates on the bed 20.
[0061] Optionally the bearing assembly 40 and bed 20 are contained within an outlet compartment
that is attached to the lower end of the funnelled section 12 of the hopper 10. In
this example, the outlet compartment is in the form of a shroud 18 with an outlet.
The outlet here is in the form of an outlet pipe 19 connected to the base of the shroud
18, however this can be another form of conduit. For example, the shroud could also
comprise inclined walls and form a smaller funnel containing the bearing assembly
40 and bed 20. The outlet tube 19 can be angled or can be directed vertically downwards.
The outlet tube 19 can extend at least partially into the shroud 18, or can be connected
to the external surfaces of the shroud 18, for example by welding or another suitable
type of fixing. The shroud 18 is connected to the funnelled section 12 of the hopper
10 with fixings such as bolts, or optionally rivets, or optionally by welding, or
optionally another means of attachment. The shroud could be insulated in certain examples.
[0062] Figures 6 and 7 show the bed 20 and shaft assembly 50 comprising the air inlet 51
and outlet 52 tubes without the hopper 10 in place for clarity. The air inlet 51 and
outlet 52 tubes can be contained within bores in one or two flexible beams that pass
behind the rear wall of the hopper 10. The beams are secured at their top ends by
a rigid foundation 57, and at their bottom ends to the movement device. The air inlet
51 and outlet 52 tubes can either be connected to the rest of the air flow conduit
through apertures in the beams that permit connection or passage of tubes, or through
connection points in the foundation 57. For example, the inlet and outlet tubes 51,52
can be rigidly fixed in a bulkhead fitting. Alternatively, the movement device can
be connected to the foundation 57 via flexible beams and the air inlet and outlet
tubes can be connected to the beams (e.g. by clips etc.).
[0063] When the outlet of the hopper is occluded by the mound of powder 28 accumulated on
the bed 20, and is to be unblocked to resume flow of the powder 28 from the hopper
10, air is flowed through the air inlet tube 51 into the bearing assembly 40. The
air moves the bearing eccentrically around the track, which is in a horizontal plane.
The eccentric movement of the bearing around the horizontal track causes oscillations
in the movement device, which moves cyclically. The cyclic movements are most pronounced
(with the highest amplitude) in the horizontal plane parallel to the plane of the
track constraining the bearing. These vibrations experienced by the movement device
when the air flows are transmitted directly to the bed 20 by the bolt or other fixing
between the movement device and the outlet control member, which vibrates the bed
20 back and forth in the horizontal plane as shown in Figure 6, although other planes
of vibration can be evident; this will be discussed in greater detail below. Thus,
the movement of the outlet control member can be in the form of vibrations. The beam
or beams that contain the air inlet and outlet tubes 51, 52 flex with the movement
of the movement device and the bed 20. The vibrations are not transmitted to the hopper
10 (or at least are not transmitted at the same intensity), as there is no direct
connection between the movement device and the hopper 10. The cantilever connection
of the movement device and bed 20 to the ends of the beams allows free cyclic oscillatory
movement of the bed 20 in concert with the vibrations of the movement device.
[0064] The vibration of the bed 20 relative to the more static hopper 10 disrupts the stacked
configuration of the accumulated powder 28, causing a collapse of the powder mound
on the bed 20, as the grains of powder in the mound experience less friction tending
to retain the structure of the mound. The grains of powder 28 that are liberated by
the vibrations of the bed 20 fall under gravity towards the outlet 20o, and eventually
some will drop off the edge of the bed 20. The collapse of the powder mound clears
the occlusion of the outlet 14 and, if there is powder remaining within the hopper
10, resumes powder flow onto the bed 20. The outlet 14 can thus be occluded and cleared
by switching the bed 20 and the hopper 10 between different states of relative movement,
i.e. by switching on and off the movement device to vibrate the bed 20 relative to
the hopper 10. The movement device is thus adapted to optionally move the outlet control
member cyclically when the valve is unblocked, and optionally the cessation of the
cyclic movement leads to occlusion of the valve by accumulated powder while the outlet
control member is static. More cohesive powder types require greater vibrational displacement
of the plate in order to encourage flow of the powder over the bed. The vibrational
power of the bearing assembly is related to the displacement amplitude and the oscillating
frequency of the assembly. The frequency of oscillation of the bearing may be adjusted
according to the type of powder that is being flowed, to improve the flow performance,
for example by reducing compaction of the powder on the plate.
[0065] Figures 8-10 show the bearing assembly 40, comprising a bearing 41 restrained in
a circular race 42. The air inlet tube 51 is inserted into an inlet channel 51 a,
which comprises a tangential port 44. The tangential port 44 is configured to direct
the flow of air from the air inlet tube 51 into the bearing race 42, and thus drive
the movement of the bearing 41 around the race 42 on an eccentric path. Optionally
the bearing track can be circular, but in some examples, the track can be elliptical,
to enhance the eccentric movement of the movement device. In this case the track is
disposed in a horizontal plane, which amplifies the vibrations in parallel planes.
On the opposite side of the bearing assembly 40, the air outlet tube 52 is also connected
to the bearing assembly 40 by insertion into an outlet channel 52a, which comprises
a port 48 disposed perpendicularly to the bearing assembly 40, and through which air
flows out of the bearing assembly 40. The air inlet 51 and outlet 52 tubes can be
inserted into the bearing assembly 40 in different locations as required.
[0066] The bearing assembly 40 comprises an outlet air manifold 46, in this example a circular
cavity forming a substantially separate layer of the bearing assembly 40 while remaining
in fluid communication with the bearing race 42. The manifold 46 includes apertures
47 which permit the flow of air out of the bearing race 42, and through the outlet
port 48. The outlet port 48 is connected to the manifold 46, and not to the race 42,
while the inlet port 44 is connected to the race 42 and not to the manifold 46.
[0067] When it is desirable to unblock the outlet 14 of the hopper 10, the air flow pathway
is opened and air begins to flow into the bearing race 42. The bearing 41 is driven
around the race 42, and as the bearing 41 picks up speed, the vibration of the bed
20 intensifies and collapses the pile of powder 28 on the bed 20. The movement of
the bearing 41 is cyclic, oscillatory, and due to the angle of the tangential port
44, eccentric, i.e. larger in one direction, so that the bed 20 moves substantially
backwards and forwards in a shallow arc determined by the length of the tubes 51,
52. The oscillatory movement can be in a different arc, or in a single plane in other
examples. The hopper 10, and optionally the shroud 18, remains static as the bed 20
moves.
[0068] Optionally air flowing through the air inlet 51 and outlet 52 tubes and through the
bearing assembly 40 is heated, for example, by the heat from the hot powder. Optionally,
the beam through which the air inlet 51 and outlet 52 tubes pass behind the hopper
10 is insulated, and optionally the portion of the rear wall of the hopper 10 that
is proximal to the air inlet 51 and outlet 52 tubes is not insulated, to allow heat
to flow towards the tubes 51,52 from the powder. The shroud 18 containing the bearing
assembly 40 and the bed 20 is optionally insulated to retain heat and resist heat
loss from the powder. The accumulation of hot powder in the bed 20 raises the ambient
temperature within the shroud 18, optionally to several hundred degrees Celsius. Heat
is absorbed by the inflowing air, and as the bearing assembly 40 is also within the
hot inner cavity of the shroud 18, the temperature of the air within the bearing assembly
40 is maintained.
[0069] The air inlet and outlet tubes 51, 52 are connected to a heat exchanger 60 as shown
in Figure 11. The heated air then passes out of the bearing assembly 40, through the
air outlet tube 52, and into the heat exchanger 60. The heat exchanger 60 comprises
at least one cool air intake. The heat exchanger 60 comprises at least two separate
air flow layers 61, 62, with the hot air from the bearing assembly outlet tube 52
flowing through one layer 61, and the cooler input air flowing into the bearing assembly
40 flowing through the other layer 62. As the cooler air being directed to the bearing
assembly 40 passes through the heat exchanger 60, at least a portion of the heat from
the hot air stream is transferred to the cooler air, creating two separate warm air
streams as best shown in Figure 11. One warm air stream is returned to the valve assembly
1 for input into the bearing assembly 40, where it is again heated by the hot powder,
and the other warm air stream returning from the bearing assembly 40 is output from
the heat exchanger 60 for use elsewhere. Examples of uses for the warm air stream
from the heat exchanger 60 include powering a heat engine such as a Stirling engine,
or heating water to create steam, optionally again to power an engine device.
[0070] Pre-heating the air before injecting it to the bearing assembly 40 results in less
thermal energy being removed from the particulate material on the outlet control member
in order to heat the incoming air powering the bearing assembly 40, meaning that the
temperature of the powder and the system overall can be more efficiently maintained
at the desired level.
[0071] Figures 12-18 show some further examples of the outlet control member. In each separate
example, the reference numbers are increased by 100. The rest of the features of the
following examples remain as described above, and for the sake of conciseness, the
descriptions will not be repeated here; however, any of the following examples of
outlet control member could be used in any of the preceding examples, and features
of the preceding examples can be combined with any of the following examples of outlet
control member, hence combinations thereof are specifically contemplated by the present
disclosure.
[0072] Figure 12 shows an example of a valve assembly 101 in which the drawing is simplified
to remove other features, but which shares some or all of the features of the previous
examples. In the present example, the valve assembly 101 includes an outlet control
member in the form of bed 120 disposed below the outlet of hopper funnel 112. Bed
120 is flat and in line with the horizontal axis x-x. Powder exits the outlet of the
hopper funnel 112 and is received by the bed 120. The mound of powder 128 accumulated
on the bed 120 is occluding the outlet of the hopper and is heaped on the bed 120.
The edges of the powder 128 have an angle of repose of 30°, and the mound of powder
stops just before the edges of the bed. In this example there is a spacing of approximately
5mm between the edge of the bed and the edge of the mound of powder, which stops the
powder from falling from the outlet control member when the outlet to the storage
chamber is occluded. The bed 120 does not have any surrounding walls. When the bed
120 is vibrated, powder falls from the full perimeter of the bed 120.
[0073] Figure 13 shows a further example of a valve assembly 201 in which the drawing is
simplified to remove other features, but which shares some or all of the features
of the previous examples with corresponding reference numbers prefixed by 2. The valve
assembly 201 comprises an alternative outlet control member in the form of a flat
bed 220, inclined downwards at an angle relative to the horizontal axis x-x. The angle
of inclination can be between 0°-90°, optionally 10°-20°, to facilitate powder run-off.
In this example, the bed 220 is angled at 15°. The bed 220 does not comprise walls,
and thus powder can flow off both at the lower end of the bed 220 and from the sides
when the mound of powder 228 is disrupted. In this example, the mound of powder is
on the tipping point of collapse due to the angle of repose relative to the inclination
of the bed 220 and the mass of the powder 228 on the bed 220. Any vibration of the
bed 220 results in significant flow of powder off the bed 220.
[0074] Inclining the bed 220 offers the advantage that resistance to flow of the powder
is lowered due to the inclination of the bed 220, and any movement of the bed, for
example the vibration from the bearing assembly, results in an "avalanche" effect,
giving rise to high powder flow relative to the energy expended.
[0075] Figure 14 shows a further example of a valve assembly 301 in which the drawing is
simplified to remove other features, but which shares some or all of the features
of the previous examples with corresponding reference numbers prefixed by 3. The valve
assembly 301 comprises an alternative outlet control member in the form of a convex
example of a bed 320, with a first plate 321 and a second plate 322 joined at an interface
that is centrally disposed under the outlet of the hopper funnel 312. Both the first
plate 321 and the second plate 322 are inclined downwards relative to the horizontal
axis x-x. The angle of repose in this case (α as indicated in Figure 19) is again
30°.The first plate 321 is inclined at a shallower angle than the second plate 322
relative to the axis x-x, thus creating a shallow apex at the interface between the
plates, and therefore an overall convex shape. Bed 320 comprises a wall along one
end of the first plate 321, which prevents powder run-off towards the rear of the
bed 320, and instead directs the flow of powder off the lowest edge of the bed 320.
The convex nature of the bed 320 reduces the mass of powder that is retained before
the outlet is obstructed, which in turn means that a larger amplitude of vibration
of the bed can be achieved for a given vibrational power exerted by the movement device.
This design may be more suitable for powder with a higher frictional coefficient that
is more cohesive or prone to accumulation in clumps and less adapted to flow from
the bed 320.
[0076] An example of an alternative outlet control member in the form of a bed with a plurality
of vertically stacked plates is shown in Figures 15-18, with features in common with
previous examples prefixed by 4. In this example, there is a top plate 420t, comprising
an aperture 420a that is centrally disposed beneath the outlet of the hopper funnel
412. This top plate 420t comprises an extension that is adapted to sit above the bearing
assembly 440. The top plate 420t comprises two pairs of legs 471, 472. The legs 471
extend on either side of the stack of plates 420p, while the legs 472 extend on either
side of the bearing assembly 440. At the end of each leg is a threaded hole for passing
through a bolt or other fixing. The top plate 420t is bolted onto a base plate 420b,
enclosing and securing the stack of plates 420p and the bearing assembly 440 together,
as best shown in Figure 18. The base plate 420b in this example is flat, however it
can take a conical or otherwise convex form in order to further reduce the mass of
powder that is accumulated on it, and subsequently on the arrangement of plates as
a whole.
[0077] The plates 420p each comprise a central aperture 420a aligned with the aperture in
the top plate 420t and with the outlet of the hopper through which powder can flow
from the hopper funnel 412 to the base plate 420b. As the powder builds up on the
base plate 420b, it forms a mound with an apex and adopting a resting angle of repose
of 30°. The resulting mound of powder obturates the aperture 420a of the next plate,
and flows over onto the upper surface of each successive plate 420p, so that each
of the plates 420p in the stack gradually accumulates a mound of powder on the surface
area of the plate 420p between its aperture 420a and its outer perimeter, and accommodates
the central mound within the aperture 420a. As powder continues to flow from the hopper,
the mound of powder 428 increases in height and obturates each aperture 420a of each
plate 420p in turn until it reaches and blocks the outlet 414 of the hopper.
[0078] The mound of powder 428 remains at rest and in a stable configuration close to the
edge of each plate 420p, 420b, with a gap of approximately 5mm between the perimeter
of each plate 420p, 420b, and the edge of the mounds of powder, with an angle of repose
of 30°, until the outlet control member is vibrated by input of air or another fluid,
for example nitrogen or steam, into the bearing assembly 440, transmitting vibrations
along the plates 420p into different parts of the mound of powder 428. As none of
the plates 420p have any walls around their perimeters, powder can flow from all points
around the perimeter of the plates 420p, 420b, 420t. As the edges of the mound of
powder are close to the edges of each of the plates, flow of powder occurs rapidly
from each plate after disruption of the mound of powder by vibrations from the bearing
assembly. Thus, the stacked arrangement of multiple plates allows faster run-off of
powder from the outlet control member.
[0079] The angle of repose of the particulate material is dependent on various parameters
of the material and the system, for example, frictional coefficient of the powder,
mass of the powder, particle size, homo- or heterogeneity of the particle sizes etc.
The angle of the base of the bed (20,120,220,320,420) is usefully less than the corresponding
angle of repose for the particular powder material, so that the sides of the mound
build up at a steeper angle than the base of the bed ; for example, a powder with
good flowability may exhibit an angle of repose of less than 40° and a compressibility
index of 1.0-1.25, and the valve may operate satisfactorily with a bed (20,120,220,320,420)
that is inclined at an angle in the range of 0°-30°. A powder with fair-poor flowability
may exhibit an angle of repose of 40°-55°, with a compressibility index of 1.25-1.5,
and the valve may then operate with a bed (20,120,220,320,420) that is inclined at
an angle in the range of 30°-40° to the horizontal axis x-x.
[0080] The arrangement of the bed 420 with the plurality of plates 420p with central apertures
420a offers a greater flow area with a smaller mass of powder around the edges of
each plate 420p acting to restrict flow of powder disposed further towards the centre
of the bed 420. The total mass of powder 428 accumulated on the bed 420 may optionally
be equal to or optionally greater than the total mass accumulated on one of the other
examples of the apparatus (20,120,220,320), however, as this mass is distributed across
multiple plates 420p, this reduces the resistance of the powder to disruption and
flow off each plate 420p. This offers the advantage that for an equivalent mass of
powder, lower vibrational power is required to disrupt the accumulated material. As
lower power is required, this results in rapid flow of powder from the outlet control
member, yet low consumption of energy.
[0081] The type of bed to be used can be selected according to the characteristics of the
powder to be flowed through the valve assembly, for example the flowability and the
cohesiveness of the powder. A single inclined plate may be better suited to a powder
with poor flowability and cohesiveness, as the distance between the plate and the
hopper can be selected accordingly. The plurality of plates 420p may be better suited
to a powder with excellent flowability and no cohesiveness, as this arrangement 420
benefits from a greater curtain area and compact configuration.
[0082] Table 1 shows a comparison of some parameters of the examples of the outlet control
members in the form of beds (120,220,320,420) shown in Figures 12-15. This shows the
"curtain area" in mm
2, and the ratio of the curtain area to the area of the hopper outlet. In this example,
the hopper outlet is square with sides of 40mm, therefore it has an area of 1600mm
2. It should be understood that the curtain area is applicable for any dimension or
shape of outlet and these examples are not limiting.
[0083] The curtain area refers to the window that is created by the distance between the
bed (20,120,220,320,420) and the hopper outlet (14,114,214,314,414) when the powder
is flowing, e.g. when the bearing assembly sets up vibrations in the bed that clear
the hopper outlet and recommence flow of the powder. Effectively, the curtain area
can be imagined as the area that a flat curtain would have if it were dropped from
the perimeter of the hopper outlet down to the bed.
[0084] In these examples, the hopper aperture is square, and thus l
1 = l
2 = l
3 = l
4 = l. Thus, the simplest example of the curtain area can be calculated using the arrangement
shown in Figure 12, where the distance d, or "lift", from the bed 120 to the hopper
outlet 114 is constant across the bed 120. In this case:

[0085] For the parameters given in this example, d = 10mm, l = 40mm and thus the curtain
area = 4 x 10 x 40 = 1600mm
2.
[0086] This can effectively be extrapolated for the other examples of the bed and hopper
outlet. For example, the example illustrated in Figure 15 with multiple plates is
merely the above equation for a single plate, multiplied by the number of plates n
in the arrangement:

[0087] For the parameters in this example, d = 10mm, l = 40mm, n = 6, therefore the curtain
area = 4 x 6 x 10 x 40 = 4800mm
2.
[0088] Where there is an inclined bed as in Figure 13, there are three different values
of lift; a small one (i.e. d
1) where the bed is nearest the outlet, a large one (i.e. d
2) where the bed is inclined furthest away from the outlet, and two equally continuously
changing distances on either side of the hopper perpendicular to both d
1 and d
2 (i.e. d
3). In this case, the average distance or lift between d
1 and d
2, <d
3>, can be used, giving the equation:

[0089] Taking Figure 13 as an example, d1 = 10mm, d2 = 20.7mm <d
3> = ½ (d
1 + d
2) = 15.35mm; l = 40mm, thus:

[0090] In the example given in Figure 14, the curtain area is illustrated in Figure 19.
There are four separate area calculations to be performed, which are then combined
in order to calculate the curtain area.
[0091] In the example shown in Figure 14 with dimensions illustrated in Figure 19, there
are three different values of lift; a small one (i.e. d
1) where the bed is nearest the outlet, a large one (i.e. d
2) where the bed is inclined furthest away from the outlet, and one at the point of
intersection of the two plates (d
3).

[0092] There are similarly three different length dimensions; l
1, l
2, and l
3. In this example, as the outlet is square, l
1=l
2, and l
3 = 0.5×l
1. However this relationship is not restrictive and is merely exemplary.
[0094] Combining the calculated values for these areas into a formula for the total curtain
area:

[0095] An exemplary calculation for the curtain area illustrated in Figure 19 is as follows,
where l
1 = 40mm; l
2 = 40mm; l
3 = 20mm; d
1 = 10mm; θ = 7.5°; and ϕ = 15°.

and

[0096] The total curtain area for these exemplary dimensions for the example shown in Figure
19 is therefore:

[0097] Increasing the curtain area of the valve allows faster flow through the valve when
the valve is unblocked. The curtain area can be adjusted to account for desired flow
rates and flow characteristics of the particulate material and particle size. For
example, a small curtain area would suffice for a free-flowing powder. A smaller curtain
area in this example would also permit rapid closure of the outlet when required.
If the outlet control member was located too far away from the outlet, it could be
the case that the powder would not stack sufficiently well to reach the outlet to
occlude it, and would instead be prone to flowing off the sides of the mound of powder.
For example, the mound of powder may not achieve the exemplary 5mm border around the
perimeter of the surface of the outlet control member. This can be overcome by increasing
the size of the plate or plates forming the base of the outlet control member, offering
a greater cross-sectional area for the powder to accumulate on.
[0098] However for e.g. cohesive aggregate, which comprises larger clumps and may not flow
so freely, a larger curtain area may be advantageous to encourage flow of the particulate
material when the valve is unblocked. This would allow stacking of the particulate
material to occlude the valve, while providing enough space for the material to flow.
Spacing the outlet control member too close to the outlet, in this example, could
result in difficulties in unblocking the valve.
[0099] It is therefore understood that the curtain area can optionally be adjusted to account
for the outlet shape, the inclination of the outlet control member, and the type of
particulate material that will be flowed through the valve.
[0100] In one example of a practical application for the valve assembly particulate material
in the form of sand is heated directly by solar energy in a concentrated solar power
system having mirrors or lenses to concentrate solar energy on a small area such as
a section of a conveyor belt conveying the sand. The concentrated solar energy heats
up the sand prior to passage of the sand through the valve assembly, which is used
to control the distribution of the hot sand, and to rout it to a heat engine such
as a steam turbine, to recover heat from the hot sand, which functions as a medium
for the transfer of renewable heat energy from the concentrated solar power system
to the heat exchanger for recovery of the heat energy.
Table 1: A comparison of exemplary parameters for the examples of the apparatus given
in Figures 12-15
Comparison of Examples |
Type |
Curtain Area (mm2) |
Ratio Curtain/Hopper outlet |
Flat Plate (Figure 12) |
1600 |
1.00 |
Inclined Plate (Figure 13) |
2456 |
1.56 |
Convex Inclined Plate (Figure 14) |
2178 |
1.36 |
Stacked Plates (Figure 15) |
4800 |
3.00 |
Hopper (10) outlet area = 40 x 40 = 1600 mm2 |
Curtain area indicates the flow area available to the powder travelling away from
beneath the hopper outlet |
1. A valve assembly for controlling flow of particulate material (28, 128, 228, 328,
428), the valve assembly (1, 101, 201, 301, 401) having a storage chamber (10) adapted
to retain particulate material (28, 128, 228, 328, 428), said storage chamber (10)
having an inlet (15) to receive particulate material (28, 128, 228, 328, 428) and
an outlet (14, 114, 214, 314, 414) to dispense the particulate material (28, 128,
228, 328, 428) from the storage chamber (10); wherein the valve assembly (1, 101,
201, 301, 401) comprises an outlet control member (20, 120, 220, 320, 420) adapted
to receive and retain particulate material (28, 128, 228, 328, 428) dispensed from
the outlet (14, 114, 214, 314, 414) of the storage chamber (10), said outlet control
member (20, 120, 220, 320, 420) being spaced apart from the outlet (14, 114, 214,
314, 414) of the storage chamber (10); wherein particulate material (28, 128, 228,
328, 428) dispensed from the outlet (14, 114, 214, 314, 414) of the storage chamber
(10) is adapted to accumulate on at least one surface of the outlet control member
(20, 120, 220, 320, 420) and to at least partially block the outlet (14, 114, 214,
314, 414) of the storage chamber (10), resisting flow of particulate material (28,
128, 228, 328, 428) from the outlet (14, 114, 214, 314, 414); wherein the outlet control
member (20, 120, 220, 320, 420) and the storage chamber (10) are movable relative
to one another to disrupt accumulated particulate material (28, 128, 228, 328, 428)
on the outlet control member (20, 120, 220, 320, 420) and unblock the outlet (14,
114, 214, 314, 414) of the storage chamber (10).
2. A valve assembly as claimed in claim 1, wherein at least a portion of the outlet control
member (20, 120, 220, 320, 420) is disposed beneath the outlet (14, 114, 214, 314,
414) of the storage chamber (10).
3. A valve assembly as claimed in claim 1 or claim 2, wherein the outlet control member
(20, 120, 220, 320, 420) is disposed within a shroud (18) connected to the storage
chamber, wherein the shroud (18) is connected to the lower portion of the storage
chamber (10); wherein the shroud (18) comprises an outlet tube (19) for dispensing
particulate material (28, 128, 228, 328, 428) that has been disrupted and fallen from
the outlet control member (20, 120, 220, 320, 420) as a result of relative movement
of the outlet control member (20, 120, 220, 320, 420) and the storage chamber (10).
4. A valve assembly as claimed in any one of claims 1-3, the outlet control member (20,
120, 220, 320, 420) having a base wherein at least a portion of the base of the outlet
control member (20, 120, 220, 320, 420) comprises at least one plate, wherein at least
a portion of the base of the outlet control member (20, 120, 220, 320, 420) is aligned
parallel to a horizontal axis.
5. A valve assembly as claimed in claim 4, wherein at least a portion of the base of
the outlet control member (20, 120, 220, 320, 420) is inclined relative to a horizontal
axis.
6. A valve assembly as claimed in claim 5, wherein the outlet control member (420) comprises
a plurality of plates (420p, 420t, 420b), wherein the plurality of plates (420p, 420t,
420b) are vertically stacked in a parallel arrangement relative to each other, and
wherein at least one plate (420p, 420t) comprises an aperture (420a) through which
particulate material (428) can pass, when said particulate material (428) is dispensed
from the outlet (414) of the storage chamber; wherein said particulate material (428)
flows from the outlet (414) of the storage chamber through the apertures (420a) in
the plates (420p, 420t) under gravity; and wherein at least one plate (420b) is a
solid plate with no aperture, wherein said solid plate (420b) is adapted to be a base
plate, and wherein the base plate (420b) is adapted to initiate accumulation of particulate
material (428) within the stack of plates (420p, 420t, 420b) as particulate material
(428) flows through the apertures (420a) of the plates (420t, 420p) disposed proximal
to the storage chamber.
7. A valve assembly as claimed in any one of claims 1-6, wherein the spacing between
the outlet control member (20, 120, 220, 320, 420) and the outlet (14, 114, 214, 314,
414) of the storage chamber (10) creates a curtain area, wherein the curtain area
is the vertical two-dimensional area defined in a first plane by the perimeter of
the outlet (14, 114, 214, 314, 414), and in a second plane by the distance between
the outlet control member (20, 120, 220, 320, 420) and the outlet (14, 114, 214, 314,
414), wherein the second plane is perpendicular to the first plane, wherein when the
valve outlet (14, 114, 214, 314, 414) is unblocked, the dimensions of the curtain
area at least partially influence the rate of flow of particulate material (28, 128,
228, 328, 428) through the valve outlet (14, 114, 214, 314, 414).
8. A valve assembly as claimed in any one of claims 1-7, wherein the (20, 120, 220, 320)
outlet control member comprises a first section (21, 321) and a second section (22,
322), wherein the first (21, 321) and second (22, 322) sections are inclined at different
angles relative to a horizontal axis; wherein the first section (21, 321) of the outlet
control member (20, 120, 220, 320) forms a connection with at least one shaft (50)
of the valve, wherein the connection comprises a cantilever connection, and wherein
the second section (22, 322) of the outlet control member (20, 120, 220, 320) is connected
only to the first section (21, 321) of the outlet control member (20, 120,220,320).
9. A valve assembly as claimed in claim 8, wherein the interface between the first (21,
321) and second (22, 322) sections of the outlet control member (20, 120, 220, 320)
is disposed beneath the outlet (14, 314) of the storage chamber (10).
10. A valve assembly as claimed in claim 8 or claim 9, wherein the second section (22,
322) of the outlet control member (20, 120, 220, 320) has a greater surface area than
the first section (21, 321) of the outlet control member (20, 120, 220, 320).
11. A valve assembly as claimed in any one of claims 1-10, comprising at least one movement
device (40, 440) adapted to cyclically move one of the outlet control member (20,
120, 220, 320, 420) and the storage chamber (10) and disrupt accumulated particulate
material (28, 128, 228, 328, 428).
12. A valve assembly as claimed in claim 11, wherein the movement of the movement device
(40, 440) causes a corresponding vibration of the outlet control member (20, 120,
220, 320, 420) and/or the storage chamber (10).
13. A valve assembly as claimed in claim 11 or claim 12, wherein the movement device (40,
440) comprises at least one bearing (41) contained within a race (42), forming a bearing
assembly (40, 440), wherein the bearing assembly (40, 440) comprises an inlet (51)
and outlet (52) adapted to provide a flow of fluid within the bearing assembly (40,
440), wherein the flow of fluid moves the bearing (41) rotationally in the race (42),
wherein rotational movement of the bearing (41) in the race (42) causes cyclic rotational
movement of the bearing assembly (40, 440), and wherein the fluid passing into the
bearing assembly (40, 440) is heated and heat is extracted from fluid passing out
of the bearing assembly (40, 440).
14. A method of controlling flow of particulate material (28, 128, 228, 328, 428) through
a valve assembly (1, 101, 201, 301, 401), the method including flowing the particulate
material (28, 128, 228, 328, 428) into a storage chamber (10) through an inlet (15)
formed in said storage chamber (10), wherein the storage chamber (10) is adapted to
retain particulate material (28, 128, 228, 328, 428); dispensing the particulate material
(28, 128, 228, 328, 428) from the storage chamber (10) through an outlet (14, 114,
214, 314, 414) formed in the storage chamber (10) onto an outlet control member (20,
120, 220, 320, 420) adapted to receive and retain particulate material (28, 128, 228,
328, 428), the outlet control member (20, 120, 220, 320, 420) being spaced apart from
the outlet (14, 114, 214, 314, 414) of the storage chamber (10); accumulating particulate
material (28, 128, 228, 328, 428) on at least one surface of the outlet control member
(20, 120, 220, 320, 420); and at least partially blocking the outlet (14, 114, 214,
314, 414) of the storage chamber (10) with particulate material (28, 128, 228, 328,
428) that has accumulated on at least one surface of the outlet control member (20,
120, 220, 320, 420); wherein the method includes moving one of the outlet control
member (20, 120, 220, 320, 420) and the storage chamber (10) relative to the other
to disrupt accumulated particulate material (28, 128, 228, 328, 428) on the outlet
control member (20, 120, 220, 320, 420) and unblock the outlet (14, 114, 214, 314,
414) of the storage chamber (10).
15. A method as claimed in claim 14, including heating the particulate material (28, 128,
228, 328, 428) before said particulate material (28, 128, 228, 328, 428) is received
in the storage chamber (10).
16. A method as claimed in claim 14 or claim 15, including connecting at least one of
the storage chamber (10) and the outlet control member (20, 120, 220, 320, 420) to
a shaft (50), wherein the shaft (50) is connected to at least one movement device
(40, 440), and including flowing fluid into an inlet (51) in the movement device (40,
440), and out of an outlet (52) in the movement device (40, 440), wherein the movement
device (40, 440) comprises a bearing (41) on a race (42), and wherein the fluid flow
within the movement device (40, 440) moves the bearing (41) around the race (42).