Patent Application
20140360587
This invention relates generally to the reduction of friction of a viscous fluid flow in a conduit by injection of a lubricating fluid between the viscous fluid and the wall of the conduit. The invention has particular application to the conveyance of thickened slurries in mining and mineral processing plants, but is also applicable in the transport of highly viscous fluids in a variety of other industries for example, the oil, cement, polymer, food and pharmaceutical industries.
Thickened slurries are favoured for the transport of particulate solid streams in mining and mineral processing. Benefits include reduced water consumption and reduced impact on the environment, and the greater ease of turn down and restart operations. Processes involving the conveyance of high viscosity materials are also found in a variety of other industries, for example the pumping of concrete in the construction industry, crude oil in the oil industry, fly ash in the power industry, and in food and pharmaceutical preparations. The viscous fluid may consist of a single phase or multiple phases.
The benefits however come with a cost since the increased friction loss arising with increasing viscosity elevates pressures and power requirements for conveying viscous materials. Sometimes the pressure required is so high that the capital cost for pumping equipment and the operating energy cost become unacceptably high.
To address these issues, there have been a number of proposals for reducing friction between viscous fluid flows and the conveying conduit, by injecting a lubricating fluid, often water, in an attempt to form a lubricating film between the viscous fluid flow and the wall of the conduit. For example, U.S. Pat. No. 5,361,797 discloses a system for injecting a lubricating fluid such as water, an oil or a polymer solution into the conduit interior from an annular reservoir via a thin circumferential slit that is inclined to direct the lubricating fluid in the direction of slurry flow. The lubricating fluid is delivered in turn to the reservoir through one or a number of feed ports. Tests have shown that the delivery of the lubricating fluid from the circumferential slit is significantly non-uniform resulting in uneven film distribution about the viscous flow and a circumferentially variable downstream effect of the lubrication. These difficulties are likely to be amplified in the arrangement of U.S. Pat. No. 5,605,174 in which lubricating fluid is delivered to the interior of a pipe section via drilled radial holes.
The peripheral unevenness of lubricant injection in these arrangements can be partially offset by increasing the volume of lubricant delivered at the injection station. In typical systems employing water as the lubricating fluid, the resulting proportionate total addition of water, especially where a number of devices are provided over a longer pipeline, may be unacceptable and detrimental to the process, or simply so high as to offset the potential advantages of employing the thickened slurry or viscous fluid as a means of transport.
The present applicant's international patent publication WO2011/050405 discloses a system for reducing friction of viscous fluid flowing in a conduit in which a lubricating fluid is passed under pressure through a porous conduit that defines a portion of the passage guiding the flow. While this configuration is initially effective in delivering lubricating fluid in a peripherally uniform manner, and is therefore suitable for many applications, some applications require the use of suitably treated water to avoid longer term clogging of the conduit pores by finer particles that are inevitably present in the available water supply.
It is an objection of this invention to achieve effective lubrication of a viscous fluid flow in a conduit in a manner that is peripherally substantially uniform but preferably does not entail a potential additional requirement for pre-treated lubricating fluid.
Reference to any prior art in the specification is not, and should not be taken as, an acknowledgment or any form of suggestion that this prior art forms part of the common general knowledge in Australia or any other jurisdiction or that this prior art could reasonably be expected to be ascertained, understood and regarded as relevant by a person skilled in the art.
The invention provides, a device for reducing friction of a, viscous fluid flow in a conduit, the device comprising:
The invention further provides a method of reducing friction of a viscous fluid flow in a conduit, comprising delivering lubricating fluid to the flow from a cavity via an outlet arrangement, wherein said fluid outlet arrangement comprises a substantially continuous opening or ring of close spaced openings about the flow, and said cavity comprises an array of passages in said body that includes a plurality of elongate passages that extend about said flow effective collectively to reduce the pressure variation and therefore velocity variation of the delivered lubricating fluid along said outlet arrangement.
In a preferred form, the cavity comprises an annular chamber about the flow path and the elongate passages include a plurality of grooves spaced apart between said at least one port and said fluid outlet arrangement on one or other of opposed faces of the annular chamber.
There are typically three to seven such grooves: it is found that the higher the number of spaced grooves, the less the variation in the velocity of the delivered lubricating fluid along the outlet arrangement. The grooves are conveniently arcuate or annular about the flow path.
Preferably, the annular chamber exhibits an elongated cross-section that is relatively substantially wider in one direction and relatively substantially narrower in another direction orthogonal to said one direction, whereby said elongated cross-section defines a first annular and a second annular end of said chamber. Conveniently, the fluid outlet arrangement comprises an open end of the annular chamber at the first end. At least one port may typically be at the second end of the annular chamber.
In a first embodiment, the annular chamber is relatively wide in a radial direction relative to an axis of the viscous fluid flow and relatively narrow in the axial direction, and the grooves are spaced radially.
In another, second, embodiment, the annular chamber extends co-axially about the flow path and the arcuate or annular grooves are spaced axially.
The body may comprise a plurality of parts that when assembled together define the cavity and the fluid outlet arrangement. For example, in the case of the abovementioned first embodiment, the body may comprise a pair of flanges, and the cavity is defined by a recess in one or preferably both of the opposed faces of the flanges. In the case of the second embodiment, one of the body parts may be internally relieved or counterbored to receive a spigot portion of another of the body parts so that said cavity is defined between the spigot portion and the relief or counterbore.
Means, for example, suitable through-holes in the flanges and matching bolts, are provided for clamping the flanges together, and a circumferential seal is provided to prevent escape of lubricating fluid from the cavity.
Advantageously, there can be one, two or more ports in the body for delivering lubricating fluid to the cavity. When two ports are used, they are preferably disposed substantially diametrically opposite and opening into the cavity at or radially outwardly of the outermost of the aforementioned arcuate or annular grooves.
The flanges may be integral with or fitted to respective segments of a conduit for confining the viscous fluid flow.
In an embodiment, means may be provided to selectively deliver and withhold delivery of the lubricating fluid at said outlet arrangements for respective defined periods.
As used herein, except where the context requires otherwise, the term “comprise” and variations of the term, such as “comprising”, “comprises” and “comprised”, are not intended to exclude further additives, components, integers or steps.
The invention will now be further described, by way of example only, with reference to the accompanying drawings, in which:
The device 10 illustrated in
The device 10 thus constitutes a body positionable to define at least a segment of a flow path 15 for viscous fluid in a conduit. The device may provide the whole conduit or more typically a section of the conduit. This body is formed by a pair of solid annular flanges 20, 21 each contiguous with a respective cylindrical conduit section 22, 23. The flanges have respective rings of complementary through-holes 25, 26 adjacent their outer peripheries for receiving, respective bolts 28 to clamp the flanges together to form the assembled body. The then opposed faces 32, 33 of flanges 20, 21 have respective shallow annular recesses 50, 51 that cooperate to define a cavity 40 in the body for retaining lubricating fluid when the flanges are assembled together. The lubricating fluid is delivered to the cavity 40 by a pair of diametrically opposite ports 42, 43 in flange 20. These ports extend parallel to the central axis 11 of the device and are fitted for coupling (not shown) to a supply of lubricating fluid, which, for example, in a mineral processing application would typically be water under pressure.
Cavity 40 is an annular chamber that exhibits an elongated cross-section that is relatively substantially wider in one direction (in this case the radial direction) and relatively substantially narrower in another direction orthogonal to the one direction (in this case the axial direction). The elongated cross-section thus defines a first annular and a second annular end of the cavity/chamber. The outer periphery or annular end of this cavity is sealed against fluid egress by an O ring seal or other type of seal 45 while the inner periphery or annular end is wholly open and thereby provides a peripherally continuous fluid outlet arrangement 48 from cavity 40 for delivering lubricating fluid to flow path 15 as a film 9 at conduit surface 13.
As mentioned, cavity 40 is defined by matching shallow recesses 50, 51 in opposed flange faces 32, 33. Recess 50 differs from recess 51 in that it has a plurality of continuous annular grooves 55 at radially spaced intervals, typically equal intervals. There are typically three to seven such grooves 55. The grooves comprise passages of cavity 40. Indeed, the radially extending main part of the cavity and the grooves 55 form an array of passages in body 10 of which grooves 55 are elongate passages extending about the flow path. Fluid inlet ports 42, 43 open into cavity 40 in the outermost of grooves 55 that is adjacent the outer annular end of the cavity 40. Grooves 55 are spaced apart between fluid inlet ports 42, 43 and outlet arrangement 48.
It is found that grooves 55 are effective collectively to reduce the pressure variation and therefore velocity variation of the delivered lubricating fluid along outlet arrangement 48. This is thought to be because the lubricating fluid seeps successively into the grooves 55, which might be described as together constituting a labyrinth of grooves, to emerge at the inner conduit surface 13 uniformly, i.e. with no or minimal variation of the pressure and therefore velocity of the delivered lubricating fluid along outlet 48. The arrangement should ideally be such that the pressure of the injected lubricating fluid at ports 42, 43 results in a pressure at outlet 48 that is sufficiently above the radial pressure exerted by the slurry for the lubricating fluid to emerge and form a lubricating film 9 on the conduit wall surface 13 downstream of the outlet, thereby lubricating and improving the flow of the slurry or other viscous flow. Device 10 may therefore be viewed as an effective drag reduction device.
A brief analysis of the arrangement illustrated in
V(x)∝P=pi−p(x) (1)
Therefore the feed velocity variation can be reduced by increasing the back pressure across the medium by way of grooves 55.
It is thus shown that the feed velocity variation along the circumferential outlet 48 is inversely proportional to the back pressure across the medium and therefore to the number of grooves. The higher the number of grooves, the more uniform the flow becomes annularly. For example, a design with five grooves will produce ⅕th of flow variation compared to a single groove, and a design with 10 grooves will produce 1/10th of that variation. Preferably, the pressure variation and velocity variation along outlet arrangement 48 is less than 2:1, more preferably less than 1.3:1, most preferably less than 1.1:1.
Grooves 155 are formed on the outer face of spigot portion 123a and therefore on the “inner” face of cavity 140. In this case there are four grooves, and the single lubricating fluid injection port 142 extends radially through conduit segment 122 opposite the rearmost of grooves 155 relative to outlet 148.
An advantage of the “in line” embodiment of
Another useful advantage of the alternative arrangement is its compactness: its radial dimension is significantly less at the flange periphery. Indeed, the flanges can be kept as standard flanges in mineral processing plants, whereas the configuration of
The incidence of clogging by inadvertent particles within the lubricating fluid is further reduced in the embodiment of
In the “in line” embodiment of
If desired, and as illustrated in
It will be understood that, in typical applications, the lubricating fluid will be a liquid, most often water, but it may also be a non-aqueous liquid such as an oil. The lubricating fluid may alternatively be a gas or a gas within a liquid and may include additives such as a viscosity modifier. It is envisaged that the illustrated device may be beneficial for dosing chemicals into a pipeline, for example for protecting pipe internals against scaling and corrosion, with the desire to minimise the required chemical volume rates. Another potential application of the device is to deliver other reagents to a flowing viscous fluid, for example reagents that would reduce the impact of acid mine drainage from mineral tailings.
More than one device 10,110 may be provided in line in a fluid transport system, for example spaced at intervals along the length of the transport conduit and/or positioned at the inlet and/or outlet sides of a pump.
It may be useful for the internal surface of the circumferential outlet 48,148 to be machined with very rough finishing to widen the jet spread; this will minimise the diffusion of the injection flow into the bulk slurry.
A particular benefit of the uniform film achievable with a device according to the invention is the ability to minimise the proportion of lubricating fluid added to the viscous fluid. Where, as would be common, the lubricating fluid is water, the proportionate addition of water relative to the water already present in the viscous flow can be as low as 1%. This is particularly beneficial where alteration of the water proportion may be undesirable or detrimental and has the further beneficial consequence that a number of the devices may be able to be used in a single conduit without excessive addition of water to the viscous fluid, for example a mineral slurry, carried by the conduit.
Tests at high viscosities (30-40 Pa yield stress) lead to an estimation that for the drag reduction performance achieved at an injection ratio of 1% of the pipe flow using the embodiment of
In general, the pressure and rate of flow of the lubricating fluid are arranged so that the lubricating fluid constitutes between about 0.05% and about 10% of fluid flowing through the flow path downstream of the device. More particularly, the lubricating fluid may constitute between about 0.05% and about 5% of fluid through the downstream passage. More particularly still, the lubricating fluid may constitute between about 0.1% and about 2% of fluid through the downstream passage, for example between about 1.0% and about 1.5% or between about 0.1% and about 1.0%.
It has been found that after the injection is turned off, the “drag reduction” performance typically continues for a while before dissipating. It may therefore be beneficial to pulse the injection flow, i.e. switch on and off, say 10 seconds on and 10 seconds off. Such pulsation would save 50% water used in the injection.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2012900442 | Feb 2012 | AU | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/AU2013/000109 | 2/7/2013 | WO | 00 | 6/23/2014 |
