1. Field of the Invention
The present invention generally relates to apparatus and methods for transporting materials, which may include fluids, and more particularly to a method and system for efficiently transporting fluids over long distances.
2. Discussion of the Background
The transport of fluids, such as water or oil, over long distances may be accomplished by shipping or by transport through a dedicated fixed system of pipes or conduits. While the use of a conduits or pipe is effective, this technique has several problems. First, the fluid experiences drag on walls of the conduit, requiring a large amount of energy to overcome frictional losses. In addition, if the system relies on gravity to provide flow, then it is also necessary to provide a consistent slope to the system over long distances.
There is a need in the art for a method and apparatus that permits the more efficient transport of material over large distances. Such a method and apparatus should be simple to construct and operate, consume less power than conventional conduits or pipes, and be less affected by the slope of the ground on which the conduit or pipes rest.
The present invention overcomes the disadvantages of prior art by providing an apparatus and method wherein materials are transported with less frictional losses. Thus, for example, a transported fluid floats on a denser fluid. The denser fluid oscillates with no net motion, while a flow is induced in the transported fluid.
In one embodiment, an apparatus is provided to accept two or more fluids. The two or more fluids include a first fluid, less dense fluid, to be transported and a second, denser fluid that remains stationary. The apparatus includes: a channel to accept the two or more fluids; a first means to produce periodic standing waves one fluid; and a second means to induce a net motion of the less dense fluid in the flow direction.
In another embodiment, a method is provided to accept one or more fluids and transport a first fluid of the one or more accepted fluids in a flow direction. The method includes: accepting one or more fluids in a channel; imparting a periodic standing wave to the accepted fluids, where said standing wave is generally aligned with the flow direction; and providing means to inhibit the flow of the accepted first fluid in a direction counter to said flow direction.
These features together with the various ancillary provisions and features which will become apparent to those skilled in the art from the following detailed description, are attained by the fluid transporting method and device of the present invention, preferred embodiments thereof being shown with reference to the accompanying drawings, by way of example only, wherein:
Reference symbols are used in the Figures to indicate certain components, aspects or features shown therein, with reference symbols common to more than one Figure indicating like components, aspects or features shown therein.
In general, embodiments are presented of an apparatus and method for transporting material across long distances. The material may be, for example and without limitation, a fluid, such as a liquid, or may be a slurry or suspension that contains particles suspended or floating on the liquid, thereby enabling transport of solid particles as well. In general, such particles must have a density less than or equal to the transporting fluid. Solid particles themselves can consist of encapsulated third phases, for example, silica or polymer microballoons containing other fluids or particles.
Certain embodiments provide a channel or other conduit that induces longitudinal movement of at least one fluid along the length of the channel. In certain other embodiments, for example and without limitation, a transported fluid floats on a fluid within a channel. The fluid may be deformed by oscillatory motion as a standing wave, and means may be provided to induce longitudinal movement transported fluid perpendicular to the channel width.
In one embodiment, channel 100 has a rectangular cross-section of width W and a height H. Alternatively, channel 100 may some curvature along its length. Channel 100 is approximately horizontal.
Channel 100 may be used to transport a fluid, such as fluid 10, in a direction indicated by an arrow V. A second, denser fluid 20 is relatively stationary compared to fluid 10. Thus for example, a fluid 10 to be transported is shown as having a fluid upper surface 11 and a lower surface 12, which is also the upper surface of fluid 20.
Channel 100 may also be used to transport particles. Thus, for example and without limitation, the fluid 10 may include particles of neutral density in the first fluid, or of a density less than that of the first fluid, thereby enabling transport of particles with the net flow of the first fluid. The particles themselves may consist of encapsulated third phases such as other liquids or cargo of various materials and devices. For example, such particles may be silica or polymer microballoons containing other fluids or materials or devices.
In several embodiments, surface 11 has a wavelike structure about an average height A, and surface 12 has a wavelike structure about an average B. Average surfaces A and B are horizontal. The combined average depth of fluids 10 and 20 is shown as depth D, with fluid 10 having an average depth D1 and fluid 20 having an average depth D2 and may bound on the bottom by channel bottom 105. Fluid upper surface 11 may be a free surface, bound by air, or, alternatively, as shown optionally in
An average longitudinal motion (flow) of fluid 10 is induced in the x direction, at least in part, by the repeated up-and-down motion of the bottom, or lower surface 12, of the fluid. As one example,
While fluid 10 has a net flow in the x direction, fluid 20 has little or no net flow in the x direction. As described in several of the embodiments, fluid 20 executes a substantially stationary oscillatory motion which perturbs surface 12. Thus fluid 10 is transported over fluid 20.
Channel 400 includes a plurality of oscillatory devices 50. Each oscillatory device 50 extends along the width W, and is located at regular intervals l with fluid 20. Channel 400 is generally similar to channel 100, except as where explicitly noted. As illustrated in
Oscillatory device 50 may include, for example and without limitation, one or more vertical, oscillatory plates that extend upwards from the channel bottom.
As examples, which are not meant to limit the scope of the present invention, the average depth of fluid 20, D2, may be 8 feet, the height D1 may be 2 feet, the distance between each plate 517, 527 is, on average, 12 feet, with S1=8 feet and S2=16 feet, resulting in a length l of 40 feet.
Channel 410 includes devices 54 that are placed at regular intervals l along the channel. Devices 54, each having a bottom surface 55 may be fixed or may move up and down, as indicated by the vertical double arrows, to coincide with the rising surface 11 to urge fluid 10 downstream. Alternatively, devices 54 could descend onto the top surface of the fluid 10 at ⅛ of each cycle before nearby peaks of fluid 20 forms.
More specifically,
Channel 600 includes a plurality of barriers 601, several of which are individually labeled 601a-f. Each barrier 601 extends the width W of channel 600 and may be support at sides 101, 103. Each barrier 601 extends down to the same location C in the channel. The location C is above the average position B of surface 12, and thus protrudes fully into fluid 10 at certain portions of a standing wave cycle and does not protrude fully into fluid 10 at other times.
Individual barriers 601 are located at half-wave locations, spaced by l/2, for example. Further, barriers 601 are located at positions slightly “upstream” of the peak/trough location by a distance δ, i.e. just before each crest.
As fluid 10 oscillates between curved and flat, as indicated in
As surface 12 recedes, as in
As one illustration of the dimensions of fluid in channel 600,
Channel 700 contains a plurality of identical barriers 701, several of which are individually labeled 701a-f. Each barrier 701 floats on surface 12 of fluid 10. Thus, for example, each barrier 701 includes a float 703 and a gate 705 that extends along width W and into fluid 10. Barriers 701 may be tethered to channel 700 or ride on rails attached to the conduit to permit them to move longitudinally in an oscillatory motion. Alternatively, barriers 701 may ride on rails attached to the conduit to permit them to move vertically.
With the height of gate 705 chosen to be within the range of the depth of fluid 10, the gate alternatively protrudes into fluid 20 and withdraws from the fluid, permitting fluid 10 to move generally in the flow direction, but having hindered backflow.
Individual barriers 701 are located at half-wave locations, spaced by l/2, for example. Further, barriers 701 are located at positions slightly “upstream” of the peak/trough location by a distance δ.
The operation of channel 700 is similar to that of channel 600. As fluid 10 oscillates between curved and flat, as indicated in
As surface 12 recedes, as in
In channel 700 a plurality of identical barriers 710, several of which are individually labeled 710a-f. Each barrier 710 floats on surface 12 of fluid 10 and is generally similar to barrier 710, and also includes a hinge 706, a hinged bottom portion 707 extending below gate 705. Portion 707 is affected by forces of fluid 10, but is hinged to gate 705 to swing in one direction only, thus permitting flow only in a downstream direction. As an example, portions 710a, 710c, and 710e illustrate portion 707 as aligned with gate 705, and portions 710b, 710d, and 710f illustrate portion 707 pointed downstream. Portions 707 faceplate the flow in the downstream direction.
Gates 910, 920, 930, and 940 may move independently in a vertical direction, with corresponding bottoms 913, 923, 933, and 943 shown as being near the average level of surface 12. As surface 12 oscillates, gates 910, 920, 930, and 940 move up and down. The width of the gate is one half a wavelength λ, such that adjacent gates move up and down past each other, as indicated in
The top of each gate 910, 920, 930, and 940 is slopped downwards in the direction of flow, as indicated by top 911, 921, 931, and 941. As gates 910, 920, 930, and 940 rises and fall, fluid 10 is collected on tops 911, 921, 931, and 941 and urged in the flow direction. Thus, for example,
It should be appreciated that in the above description of exemplary embodiments of the invention, various features of the invention are sometimes grouped together in a single embodiment, figure, or description thereof for the purpose of streamlining the disclosure and aiding in the understanding of one or more of the various inventive aspects. This method of disclosure, however, is not to be interpreted as reflecting an intention that the claimed invention requires more features than are expressly recited in each claim. Rather, as the following claims reflect, inventive aspects lie in less than all features of a single foregoing disclosed embodiment. Thus, the claims following the Detailed Description are hereby expressly incorporated into this Detailed Description, with each claim standing on its own as a separate embodiment of this invention.
Thus, while there has been described what is believed to be the preferred embodiments of the invention, those skilled in the art will recognize that other and further modifications may be made thereto without departing from the spirit of the invention, and it is intended to claim all such changes and modifications as fall within the scope of the invention.
Number | Name | Date | Kind |
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6412354 | Birchak et al. | Jul 2002 | B1 |
7326001 | McFarland | Feb 2008 | B2 |
Number | Date | Country | |
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20120312376 A1 | Dec 2012 | US |