[0001] The present invention relates to a canister. More particularly, but not exclusively,
it relates to canister suitable for capturing evaporative emissions from a vehicle
fuel system. Even more particularly, but not exclusively, it relates to an arrangement
of a number of such canisters to efficiently occupy a cavity within in a vehicle.
[0002] Vehicle fuel systems often emit hydrocarbon fuel vapours which can be toxic and harmful
to the environment. Typically, these emissions of hydrocarbon vapours occur during
fuel storage and delivery.
[0003] Vehicle fuel systems are often equipped with evaporative emission control systems
to reduce the emission of vapours from the vehicle fuel system to assist in complying
with hydrocarbon emission limits. Typically, such control systems comprise a vapour
entrapment canister arranged to trap hydrocarbon vapour before it can enter the environment.
[0004] Generally, a vapour entrapment canister contains an adsorbent material, such as activated
carbon. The adsorbent material adsorbs the hydrocarbon molecules present in the fuel
vapours entering the canister. This reduces the amount of hydrocarbon vapours released
into the environment.
[0005] The adsorbent material used in current vapour entrapment canisters has a finite adsorption
capacity and must be refreshed periodically. Usually, the refreshing of the adsorbent
material involves purging the canister of hydrocarbon vapours. Generally, an air stream
passes over the adsorbent material in order to desorb the hydrocarbon vapours and
purge the canister. The air/hydrocarbon mixture is the directed to the vehicle's engine,
via the engine air intake system, for combustion.
[0006] Current vapour entrapment canisters have a number of problems and disadvantages associated
with them.
[0007] The distribution of the fuel vapours in the adsorbent material in current vapour
entrapment canisters is often non-uniform. This results in localised saturation of
the adsorbent materials leading to an increase in hydrocarbon emission levels from
the vehicle.
[0008] Conversely, regions of highly restricted flow, for example regions having a high
concentration of adsorbent materials, and regions remote from a hydrocarbon inlet
may only be partially saturated at the time of purging the vapour entrapment canister.
This results in an inefficient use of the vapour entrapment system and its control
system.
[0009] Additionally, in current vapour entrapment canisters the adsorbent material is not
necessarily densely packed. This reduces the efficiency of adsorption of the hydrocarbon
vapours as flow paths can form outside the adsorbent material. These flow paths allow
the hydrocarbon vapours to escape without being adsorbed by the adsorbent material.
[0010] Exposure to moisture, alcohol fuels or variations in temperature can cause changes
in the volume of the canister, or density of packing of the adsorbent material. Changes
in the canister volume, or packing density of the adsorbent material, can result in
loosening and destruction of particles forming the adsorbent material. This loosening
and destruction of the particles of the adsorbent materials allows flow paths to occur
outside the adsorbent material.
[0011] Often, these variations in canister volume and packing density of adsorbent material
are compensated for by the insertion of a volume compensator into the vapour entrapment
canister.
[0012] The use of a volume compensator adds to the complexity of manufacturing such canisters
and increases the cost of manufacture.
[0013] An elongate vapour entrapment canister presents particular difficulties. In this
instance, it is difficult for the volume compensator to exert a suitable packing force
over the total length of the canister such that the adsorbent remains adequately packed
throughout the canister. In particular, a suitable packing force may not be exerted
towards an end of the vapour entrapment canister remote from the volume compensator.
[0014] According to a first aspect of the present invention there is provided a vapour entrapment
canister comprising a chamber, and an inlet port and an outlet port arranged such
that vapour can flow therebetween, characterised in that the distance between a tip
of either of the inlet port, or the outlet port, and an inner surface of a wall of
the chamber is uniform over the majority of the inner surface of the wall.
[0015] Such a canister results in a substantially uniform flow of vapour in between the
diffuser and the chamber's periphery, or vice versa if the direction of flow is reversed.
[0016] The chamber may be spherical. The tip may be located at the centre of the chamber.
[0017] A spherical chamber obviates the requirement for a volume compensator. Additionally,
a spherical canister can fit into a space where a conventional square or rectangular
vapour recovery canister cannot. Also, the provision of a "standardised" spherical
canister reduces the cost of production of vapour entrapment canisters compared to
the prior art.
[0018] The distance from the tip to the inner surface of the wall may be substantially equal
at all points.
[0019] The chamber may contain an adsorbent material arranged to adsorb vapour, for example
hydrocarbon vapour. The adsorbent material may comprise activated carbon.
[0020] The wall may be spaced apart from an inner surface of the chamber.
[0021] The outlet port may be opposed to the inlet port. Alternatively, the outlet port
may be inclined with respect to the inlet port.
[0022] Such freedom in the definition of the relative alignment of the inlet and outlet
ports allows production of canisters tailored for a particular space.
[0023] Embodiments of the present invention will now be described, by way of example only,
with reference to the accompanying drawings in which:-
Figure 1 is a sectional view of an embodiment of a vapour entrapment canister according
to an aspect of the present invention; and
[0024] Referring now to Figure 1, a vapour canister 10 comprises a chamber 12 having an
inlet 14 and an outlet 16. A tip 19 of the inlet 14 is located at a central. In a
preferred embodiment, shown in Figure 1, the chamber 12 is spherical.
[0025] A mesh screen 18 is mounted concentrically within the chamber 12. The mesh screen
18 is spaced apart slightly from an inner wall 20 of the chamber 12, typically by
between 3 and 4 mm. The interior of the screen 18 is filled with activated carbon
22.
[0026] A tip 19 of the inlet 14 is positioned at the centre of the chamber 12. This results
in the distance from the tip 19 to the periphery of the chamber 12 being substantially
equal in all directions. Thus, the flow path distance through the activated carbon
22 is substantially equal in all directions.
[0027] The inlet 14 connects to a fuel tank venting system (not shown) via an inlet conduit
26. The inlet 14 also connects to a purge line 28.
[0028] In use, hydrocarbon vapour from the fuel tank enters the vapour canister 10 through
the inlet conduit 26. As the hydrocarbon vapour passes radially outward towards the
mesh 18 the activated carbon 22 adsorbs the hydrocarbon vapour. A concentration gradient
of hydrocarbon vapour is established between the inlet 14 and the outlet 16, with
the concentration of hydrocarbon vapours being higher at the inlet 14 than at the
outlet 16. The spherical shape of the chamber 12 ensures that the length of the flow
path from the inlet 14 to the outlet 16 through the activated carbon 22 is uniform
irrespective of the direction of flow of the hydrocarbon vapour
[0029] Consequently, the levels of hydrocarbon vapour exiting the chamber 12 through the
outlet 16 are reduced.
[0030] To avoid build-up of hydrocarbon molecules in the activated carbon 22, the vapours
must be purged at regular intervals. The vapours are generally desorbed by means of
an air stream entering the chamber 12 through the purge line 16. The desorbed vapours
are then sent to the engine air intake system (not shown) for combustion.
[0031] It will be appreciated that, although shown with the inlet 14 at the centre of the
chamber 12 and the outlet 16 at the periphery of the chamber 12, the respective positions
of the input 14 and output 16 may be reversed without affecting the operation of the
vapour entrapment canister 10.
[0032] It will be appreciated that although describe with reference to a spherical canister
any convenient shape of canister, for example ovoid, may be used if an appropriate
flow path can be achieved. An appropriate flow path is one where the inlet to outlet
distance is approximately constant irrespective of the flow path taken between them.
[0033] Various modifications and improvements may be made to the above without departing
from the scope of the present invention.
1. A vapour entrapment canister (10) comprising a chamber (12), and an inlet port (14)
and an outlet port (16) arranged such that vapour can flow therebetween, characterised in that the distance between a tip (18) of either of the inlet port (14), or the outlet port
(16), and an inner surface of a wall (20) of the chamber is uniform over the majority
of the inner surface of the wall (20).
2. A canister (10) according to claim 1 further characterised in that the chamber is spherical.
3. A canister (10) according to either claim 1 or claim 2 further characterised in that the tip (18) is located at the centre of the chamber (12).
4. A canister (10) according to any preceding claim further characterised in that the distance from the tip (18) to the inner surface of the wall (20) is equal at
all points.
5. A canister (10) according to any preceding claim further characterised in that the chamber (12) contains an adsorbent material (22) arranged to adsorb hydrocarbon
vapour.
6. A canister (10) according to claim 5 further characterised in that the adsorbent material (22) comprises activated carbon.
7. A canister (10) according to any preceding claim further characterised in that the wall (20) is spaced apart from an inner surface of the chamber.
8. A canister (10) according to any preceding claim further characterised in that the outlet port (16) is opposed to the inlet port (14).
9. A canister (10) according to any one of claims 1 to 7 further characterised in that the outlet port (16) is inclined with respect to the inlet port (14).