SEPARATOR

Abstract

A separator (1) for removing contaminants from a liquid, the separator comprising a rotatably mounted chamber (2) arranged to rotate about an axis of rotation, and the separator further comprising an inlet (23) for liquid to enter the chamber and an outlet (33) for liquid to leave the chamber, and wherein the inlet is at a greater radial position from the axis of rotation as compared to the outlet, and further wherein the flow of liquid into the chamber arranged to cause the chamber to rotate, and a thickness of contaminant sludge cake (30) caused to accumulate on an inner wall of the chamber.

Claims

1. A separator for removing contaminants from a liquid, the separator comprising a rotatably mounted cylindrical chamber arranged to rotate about an axis of rotation, the chamber comprising multiple drive surfaces arranged, which when impacted by inflowing liquid, imparts a turning moment thereby rotating said chamber, and the separator comprising multiple disks or cone separators, arranged in said chamber, and the separator further comprising an inlet for liquid to enter the chamber and an outlet for liquid to leave the chamber, and wherein the inlet is at a greater radial position from the axis of rotation as compared to the outlet, and, in use, the thickness of contaminant sludge caused to accumulate on the inner wall of the chamber comprises a liquid porous component that is located in the flow path of liquid from said chamber to the outlet to the separator, the porous component is arranged in use to progressively block over time, thereby reducing to flow area available for liquid to flow through and so impact on the rotational speed at which the separator is driven by liquid flow.

2. A separator as claimed in claim 1 which comprises a rotational speed sensor which is arranged to sense the speed of rotation of the chamber.

3. A separator as claimed in claim 2 which comprises an alert signal generator arranged to issue an alert signal if the rotational speed of the chamber is determined to have fallen below a predetermined threshold speed.

4. A separator as claimed in claim 3 in which the threshold speed is indicative of a predetermined thickness of sludge having accumulated on the inner wall.

5. A separator as claimed in claim 1 wherein the inner wall of the chamber is substantially cylindrical.

6. A separator as claimed in claim 1 wherein the inlet comprises a plurality of channels into the chamber.

7. (canceled)

8. A separator as claimed in claim 1 in which each drive surface is curved or of varying gradient, or multi-radiussed, when viewed in plan.

9. A separator as claimed in claim 1 in which the drive surfaces are of substantially (part-) spiral shape.

10. A separator as claimed in claim 1 in which the drive surfaces are circumferentially spaced, preferably at substantially equal of regular angular intervals.

11. A separator as claimed in claim 1 in which the drive surfaces are arranged on or adjacent to a basal surface or in a lower region of the chamber.

12. A separator as claimed in claim 1 in which each of the operative drive surfaces is aligned or associated with on e or more respective inlet channels.

13. A separator as claimed in claim 1 in which the drive surfaces are radially spaced from the axis of rotation of the chamber.

14. A separator as claimed in claim 1 in which the inlet to the chamber is in fluid communication with a conduit in a spindle to which the chamber is rotatably mounted, wherein inflowing liquid is arranged to flow through the conduit and into the chamber through the inlet.

15. A separator as claimed in claim 1 in which the outlet comprises an outlet orifice which communicated with a separator outlet and the inlet comprises an inlet orifice which communicates with a separator inlet.

16. A separator as claimed in claim 1 in which the outlet is in fluid communication with multiple output drive surfaces which are arranged to be impacted by the outgoing liquid to provide a rotational drive to the chamber.

17. A separator as claimed in claim 16 in which the output drive surfaces are provided in a sub-chamber located atop the chamber.

18. A separator as claimed in claim 1 which comprises multiple vane formations, arranged in use, to provide a rotational driving force to the chamber.

19. (canceled)

20. (canceled)

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0031] Various embodiments of the invention will now be described, by way of example only, with reference to the following drawings:

[0032] FIG. 1 is a longitudinal cross-sectional view of an oil separator,

[0033] FIG. 2 is a sectional downward plan view, inside the chamber of the separator of FIG. 1,

[0034] FIG. 3 is a perspective view of a vaned distributor of the oil separator,

[0035] FIG. 4 is a side elevation of a separator cone, a stack of which are present in the chamber of the separator of FIG. 1,

[0036] FIG. 5 is a plan view of the separator cone of FIG. 4,

[0037] FIG. 6 is a perspective view of the distributor disc provided with a cover,

[0038] FIG. 7 is an underside view of an uppermost portion of the separator of FIG. 1,

[0039] FIG. 8 is a longitudinal cross-sectional view of a second embodiment of an oil separator,

[0040] FIGS. 9A and 9B are perspective views of the uppermost sub-assemblies of the separator of FIG. 8,

[0041] FIG. 10A is a plan view of the distributor disc component and the lower assembly of the separator of FIG. 8, and

[0042] FIG. 10B is a perspective view of the distributor disc and lower separator sub-assembly.

DETAILED DESCRIPTION

[0043] There is now described an oil separator 1, as shown in FIG. 1. As will be described below, the separator 1 enables improved separation operational characteristics in relation to separating out contaminants in oil. The contaminants may include soot, dirt and metallic particulate, which need to be removed from an oil system to ensure optimum performance of the system.

[0044] The separator 1 comprises a generally cylindrical chamber 2, to which there is provided an inlet and an outlet. As will be described in detail below, the inlet is located at the base of the chamber, whereas the outlet is provided at the top of the chamber. In this way, all contaminated oil passes through maximum space in the generated centrifugal field before exiting. The chamber 2 is rotatably mounted about a spindle or shaft 5 by way of a top and a bottom bearing bush (referenced 8 and 9 in FIG. 1). A sleeve 15 encloses the spindle 5. Broadly, in use, the flow of oil in the chamber 2 through the inlet causes a driving force to be applied to the chamber, so as to rotate the chamber. The rotational motion of the chamber brings about a centrifugal effect to the liquid within the chamber, such that the contaminants are forced towards an inner surface 2a of the chamber 2. A ring or annulus of sludge forms on the inner surface.

[0045] Located within the chamber 2 there is provided a stack of cone or disk separators 10. The stack 10 is located centrally about the longitudinal axis of chamber 2, and each disk separator is maintained vertically spaced-apart from its neighbour. This spacing of adjacent disks results in allowing for contaminants to flow out radially (when viewed in plan) outwardly, towards the inner surface 2a of the chamber. This inter-stack spacing is achieved by way of integrally formed features (reference 10f, as shown in FIG. 4) on one side of each of the disks which bears on an adjacent disk, and serves to support and maintain adjacent disks spaced apart. FIGS. 4 and 5 show views of an individual separator disk 10a, which comprises a frusto-conical wall 10c, and multiple spaced-apart bridging members 10e which connect to an uppermost rim 10d. The apertures between the bridging members 10b serve, in use, to allow processed/clean oil to flow upwardly towards the outlet within the chamber. In more detail, the inter-stack spacing formations 10f are circumferentially distributed about the discs 10a. The radiused end portions of the formations 10f serve to assist in contributing to the centrifugal effect, by way of oil impacting on the formations 10f. The stack 10 of discs is held fast with respect to the inertial frame of reference of the chamber 2.

[0046] Details of the inlet portion of the separator are now described, referring in particular to FIGS. 1 and 2. A basal portion of the chamber comprises distributor 20 (which may be termed a distributor ring). Broadly, the distributor 20 serves to distribute incoming (unprocessed) liquid in the chamber, as well as providing drive surfaces which bring about rotation of the chamber. There is provided a hub portion 21 which defines therein multiple (feed) channels 21a, separate from each other. The channels 21a are substantially radially located. Liquid reaches the orifices by way of flowing through a conduit 13 which is provided in a lower portion of the spindle 5. An upper portion of the conduit 13 is provided with multiple ports 23. The ports 23 are fluidically connected to an annular space 24, which in turn is fluidically connected to the channels 21a. Each channel leads to a respective drive surface 22a, as best seen in FIG. 2. Each drive surface 22a, when viewed in plan, is of curved or multi-radiussed shape. Moreover, the shape may be viewed as part spiral. The shaping of the drive surfaces is such that when liquid impacts on the surface, it causes a turning moment to be applied to the chamber. The drive surfaces 22a may be considered in this way as serving as vanes similar to that of a turbine drive. Each drive surface 22a is a surface of a rib or vane formation 22. The formations 22 are equally angularly spaced from one another, and form channels therebetween. The formations 22 are provided on a basal surface of the chamber 2.

[0047] The shaping and configuration of the vane formations 22 also assists liquid to towards the inner wall 2a of the chamber, and thereby enhances the centrifugal effect. The formations 22 can more clearly be seen in FIG. 3. As can be seen, each vane formation 22 may be considered as providing a leading surface and a trailing surface. The drive surface 22a is the trailing surface. The surface 22b is similarly curved/(multi-) radiused as per the drive surface. In use the shape of the surface 22b serves to guide oil radially outwardly. It will be appreciated that oil is constrained within a space defined between adjacent vane formations 22.

[0048] Located atop the formations 22 there is provided a cover 25. The cover is of substantially frusto-conical form, and comprises a central aperture arranged to receive the sleeve 15. The cover 25 serves in part to support the stack 10, and in part to provide and dictate a required outlet orifice (referenced 23) size and position for oil leaving the drive surfaces 24 into the chamber. The cover is best seen in FIG. 6.

[0049] In use, oil fed into the chamber 2 is forced towards the inner wall 2a. As the chamber progressively fills with oil it is forced upwardly through the separator discs 10a. The discs 10a provide an enhanced centrifugal separation by causing particulate to be directed radially outwardly within the spacings between adjacent discs 10a. That particulate accumulates with the sludge cake on the inner surface 2a. The oil which reaches the uppermost part of the chamber 2 reaches the chamber outlet, which is provided by a substantially annular opening. It is to be noted that the this opening occupies a smaller radial position as compared to the outlet regions adjacent the drive surfaces 24 at which oil enters the chamber. This advantageously ensures that the oil travels through the region of the chamber at which the centrifugal force is at its greatest, and thus ensuring optimal separation. In particular, the greater surface area created by the separator discs that the contaminated liquid is exposed to, causes quicker separation.

[0050] As the separation process continues, an annular sludge cake 30 accumulates on the inner wall 2a. The radial thickness of this sludge increases during an operational cycle. As it does so, the inertia of the chamber gradually increases, which, for the same flow rate of oil into the chamber results in a decrease in rotational speed of the chamber 2. This decrease in speed is roughly inversely proportional to the increase in thickness of the sludge cake 30. A sensor 50a is provided which is in a stationary frame of reference as compared to the chamber 2. A magnet 50b is provided attached to the chamber, and the passing proximity of the magnet is detectable by the sensor. In use, a measure of the rotational speed of the chamber can be determined. A data processor and a memory, or equivalent electronic circuitry and/or sub-assemblies, are also provided which is configured to determine from an output of the sensor 50a when the speed of the chamber reaches, or falls below a predetermined (stored) threshold value. This value is selected to correspond to a thickness of sludge which necessitates a service operation of the separator in which the separator is partially dissembled to allow the sludge to be removed. The data processor is connected to a visual and/or audio signalling device, which is arranged to issue an alert signal when the threshold criteria is met. For example, this may comprise a green light, amber light and a red light. The amber light is activated when the separator requires servicing due to sludge build up. A red light indicates power on.

[0051] With reference to FIG. 8 there is shown a further embodiment of the invention. The separator 100 is substantially functionally identical to the separator 1, save for some structural changes. Like reference numerals are used to denote substantially the same, or identical features. One such structural change is that of the inclusion of a mesh component 110, arranged in a ring shape, located between the outlet from the chamber, and the nozzles which output cleansed oil therefrom. More generally, the mesh is located in the fluid pathway 28 between the orifice 33 from the chamber and the nozzles 35. The mesh may comprise a component of expanded or perforated metal of plastic, which comprises an array apertures/openings defined by the network-like structure of the material.

[0052] A rotational speed sensor (such as 50a and 50b) would be provided with the separator 100 (but is not shown in FIG. 8).

[0053] It will be appreciated that the separator 1 could be modified to include a similar mesh material with the pathway 28.

[0054] In use, the mesh component 110 allows liquid from the separation chamber therethrough and towards being output at the nozzles. However, over time, the apertures will gradually block with small particulate, and so progressively reducing the flow area available for fluid to flow through. This in turn has the effect of slowing the flow of fluid through the separator, and the reduction in speed can be sensed by the speed sensor. Therefore, the mesh component provides an enhancement to providing an indicator that the separator is saturated with sludge cake, and needs to be cleaned. The mesh component, may advantageously be detachable such that it can be removed from the assembly, cleaned and replaced, or alternatively, replaced with a fresh/unused mesh. The saturation level indication is thereby made more accurate.

[0055] In FIGS. 9A and 9B, and FIGS. 10A and 10B, the respective upper and lower subassemblies are shown. As can be seen, they are largely identical to those of the separator 1. In FIG. 9B, the reference numeral 50 denotes the top cover 50, which incorporates the nozzles 35.

[0056] When the (processed) oil exits the chamber it enters into a sub-chamber 28, provided in an uppermost part 27 of the separator. An annular orifice 33 fluidically connects the chamber 2 to the sub-chamber 28. Provided within the sub-chamber 28 there are provided multi-radiused drive fins/vanes 29 which upon impingement by the oil with a respective drive surface 29a provide a rotational motive force to the chamber. On flowing through the sub-chamber 28, the oil is directed to one of multiple exit nozzles 35 by virtue of the oil being constrained and compartmentalised between neighbouring vanes 29, as best seen in FIG. 4. The oil is then delivered back to the host system through nozzles 35, such as an oil sump in a diesel engine. The uppermost part 27 further comprises vane formations 26 which are generally curved profile and located intermediate of the vanes 29.

[0057] Advantageously, the separator 1 is capable of being driven at high rotation speeds. This results in highly effective separation of contaminants. This results from the position of the nozzles 35 at a larger diameter than the chamber inner wall 2a. Increased momentum also results from the design and configuration of the distributor 20 as well as the top turbine 27. The rotational sensor and alert signal advantageously means that the separator can be timely serviced only when as required. It will be appreciated that continued growth of the sludge cake would result in partial or total occlusion of the oil inlet to the chamber, resulting in restricted oil flow therethrough.