Hydrocyclone bundle

Information

  • Patent Grant
  • 6800208
  • Patent Number
    6,800,208
  • Date Filed
    Friday, January 10, 2003
    23 years ago
  • Date Issued
    Tuesday, October 5, 2004
    21 years ago
Abstract
A hydrocyclone bundle comprising a plurality of hydrocyclone liners and a plate assembly for use in liquid-liquid separation is disclosed. The hydrocyclone bundle may be used in new or existing separators. The hydrocyclone liners may be oppositely positioned within the hydrocyclone bundle. The plate assembly may collect and distribute overflow and underflow effluents from the hydrocyclone liners.
Description




BACKGROUND




1. Field of Invention




This invention relates generally to a hydrocyclone separator, and, more particularly, to a hydrocyclone bundle used in a hydrocyclone separator and methods of using same.




2. Description of Related Art




Hydrocyclone separators are know in the art for use in the separation of solids from liquid, solids from gas, gas from liquid, and in the separation of liquids from other liquids. In liquid-liquid separation, liquids are separated by density through the use of centrifugal force generated in a non-rotating chamber. Liquid-liquid separation is particularly useful in the oil and gas industries where large volumes of oil and water must be separated.




In liquid-liquid separation, fluid is generally introduced tangentially into an upper portion of a conic hydrocyclone liner at a relatively high velocity. As the fluid flows through a narrowing lower portion of the hydrocyclone liner, the angular velocity of the fluid accelerates in a spiral. As the fluid spirals, centrifugal forces drive the more dense components to the outer portion of the rotating column of the fluid and the less dense components of the fluid migrate to a central column area. The less dense components are passed upwardly through an overflow outlet in the upper portion of the hydrocyclone liner and the more dense components are discharged through an underflow outlet in the lower portion of the hydrocyclone liner.




Cyclone separators are disclose by Carroll et al. disclose, in U.S. Pat. No. 4,673,495. A plurality of cyclone separators are enclosed substantially within a partitioned housing such that a feed inlet of a first cyclone separator is in fluid communication on one side of a partition and a feed inlet of a second cyclone separator is in fluid communication with an underflow outlet of the first cyclone separator on the other side of the partition.




An oil recovery system is disclosed by Carroll discloses, in U.S. Pat. No. 4,698,152 wherein water contaminated with oil passes from a first separator bank to an inlet manifold of a second separator bank preferably consisting of one or more cyclone separators which separate the inlet mixture into water and oil components.




A hydrocyclone separation system is disclosed by Worrell et al, in U.S. Pat. No. 4,927,536 wherein a first and second hydrocyclone are oppositely disposed such that a curved flow direction conduit extends from an underflow outlet of a first hydrocyclone separator to a tangential fluid inlet of a second hydrocyclone separator.




A multiple hydrocyclone assembly is disclosed by Bouchillon et al. in U.S. Pat. No. 5,499,720, wherein the hydrocyclone assembly has a closed tubular vertical housing having an outer cylinder. Multiple hydrocyclones are mounted in axially extending rows and in corresponding radial positions from an outer surface of the outer cylinder.




SUMMARY




In one aspect, the present invention is directed to a hydrocyclone bundle comprising a plurality of hydrocyclone liners each having an overflow end and an underflow end, and a first plate fluidly connected to an outlet of one of the overflow end or the underflow end of at least one of the plurality of hydrocyclone liners. The first plate is constructed and arranged to collect fluid from the overflow end or the underflow end of the at least one of the plurality of hydrocyclone liners.




Another aspect of the invention is directed to a hydrocyclone bundle comprising a plurality of hydrocyclone liners, each having an overflow end and an underflow end, a first end plate assembly comprising an overflow plate and an underflow plate, and a second end plate assembly comprising an overflow plate and an underflow plate. The overflow plate of the first end plate assembly is in fluid communication with the overflow plate of the second end plate assembly.




In another aspect of the invention, a hydrocyclone separator comprises a plurality of hydrocyclone bundles and means for interrupting flow from at least one of the hydrocyclone bundles.




Another aspect of the invention is directed to a method of separating a fluid, comprising providing a fluid having a less dense component and a more dense component, feeding the fluid to an inlet of a hydrocyclone bundle thereby separating the less dense component and the more dense component. The less dense component is removed from an overflow outlet of the hydrocyclone bundle, and the more dense component is removed from an underflow outlet of the hydrocyclone bundle.




Another aspect of the invention relates to a method of facilitating separating a fluid having a less dense component and a more dense component, comprising providing a hydrocyclone bundle in a vessel, feeding the fluid to an inlet of the hydrocyclone bundle thereby separating the less dense component and the more dense component. The less dense component is removed from an overflow outlet of the hydrocyclone bundle, and the more dense component is removed from an underflow outlet of the hydrocyclone bundle.




Other advantages, novel features, and objects of the invention will become apparent from the following detailed description of non-limiting embodiments of the invention when considered in conjunction with the accompanying drawings, which are schematic and which are not intended to be drawn to scale. In the figures, each identical or nearly identical component that is illustrated in various figures typically is represented by a single numeral. For purposes of clarity, not every component is labeled in every figure, nor is every component of each embodiment of the invention shown where illustration is not necessary to allow those of ordinary skill in the art to understand the invention. In cases where the present specification and a document incorporated by reference include conflicting disclosure, the present specification shall control.











BRIEF DESCRIPTION OF THE DRAWINGS




Preferred non limiting embodiments of the present invention will be described by way of example with reference to the accompanying drawings, in which:





FIG. 1

is a hydrocyclone vessel of the prior art.





FIG. 2

is a hydrocyclone bundle having a plurality hydrocyclone liners.





FIG. 3

is an exploded view of a partial plate assembly.





FIG. 4

is a cut away view of the hydrocyclone bundle of FIG.


2


.





FIG. 5



a


is a perspective view of a first side of an underflow plate positioned near an overflow exit of a hydrocyclone bundle.

FIG. 5



b


is a perspective view of a second side of an underflow plate positioned near an end of a hydrocyclone bundle opposite to the overflow exit of the hydrocyclone bundle.





FIG. 6



a


is a top view of the underflow plate of

FIG. 5



a.







FIG. 6



b


is a top view of the underflow plate of

FIG. 5



b.







FIG. 7



a


is a perspective view of a first side of an overflow plate positioned near an overflow exit of a hydrocyclone bundle.





FIG. 7



b


is a perspective view of a second side of an overflow plate positioned near an end of a hydrocyclone bundle opposite to the overflow exit of the hydrocyclone bundle.





FIG. 8



a


is a top view of the overflow plate of

FIG. 7



a.







FIG. 8



b


is a top view of the overflow plate of

FIG. 7



b.







FIG. 9



a


is a top view of a first side of a backing plate.





FIG. 9



b


is a top view of a second side of the backing plate of

FIG. 9



a.







FIG. 10

is a top view of an endplate.





FIG. 11

is a top view of another endplate.





FIG. 12



a


is a perspective view of an overflow end of a hydrocyclone liner.





FIG. 12



b


is a side view of the overflow end of the hydrocyclone liner of

FIG. 12



a.







FIG. 12



c


is a side view of an underflow end of the hydrocyclone liner of

FIG. 12



a.







FIG. 13

is an end view of an overflow end of the hydrocyclone liner of

FIG. 12



a.







FIG. 14

is a perspective view of a hydrocyclone bundle having 16 hydrocyclone liners.





FIG. 15

is an end view of the hydrocyclone bundle of

FIG. 14

, showing another embodiment of an underflow plate.





FIG. 16

is a cross sectional view of the hydrocyclone bundle taken along section line


16





16


of

FIG. 15

with an endcap.





FIG. 17

is a cut away view of a hydrocyclone liner bundle having an overflow effluent and an underflow effluent positioned at one end.





FIG. 18



a


is an end view of a first side of an overflow plate of another embodiment.





FIG. 18



b


is a perspective view of the overflow plate of

FIG. 18



a.







FIG. 18



c


is an end view of a second side of an overflow plate of

FIG. 18



a.







FIG. 19



a


is an end view of a first side of an underflow plate shown in FIG.


15


.





FIG. 19



b


is a perspective view of the first side of the underflow plate of

FIG. 19



a.







FIG. 19



c


is a perspective view of a second side of the underflow plate of

FIG. 19



a.













DETAILED DESCRIPTION




The present invention relates to a bundle of hydrocyclone liners used to separate to a less dense component and a more dense component from a fluid. A plurality of hydrocyclone liners are arranged in a bundle which may be used in new or existing vessels or piping systems. The arrangement of hydrocyclone liners and plates may reduce the cost, size, weight, and complexity of hydrocyclone separators, as well as to segregate flow which may increase the operating range of the hydrocyclone separator by is expanding its turndown ratio.





FIG. 1

shows a conventional hydrocyclone separator. Hydrocyclone liners


12


are positioned in vessel


10


such that an overflow end


14


of each hydrocyclone liner


12


is located at or hear a first end


24


of the vessel


10


. Similarly, an underflow end


16


of each hydrocyclone liner


12


is located at or near a second end


26


of vessel


10


. Fluid enters inlet flow chamber


28


of vessel


10


through inlet


18


, and tangentially enters hydrocyclone liners


12


near an overflow end


14


of the hydrocyclone liner. Overflow plate


34


separates the inlet flow chamber


28


from an overflow collection space


36


. Underflow plate


30


separates inlet flow chamber


28


from an underflow collection space


32


. As the fluid flows through the hydrocyclone liner


12


, the less dense components are passed through an overflow outlet of the hydrocyclone liners and enter the overflow collection space


36


, while the more dense components are discharged through an underflow outlet of the hydrocyclone liners and enter the underflow collection space


32


. The underflow fluid exits vessel


10


through underflow exit


20


, and overflow fluid exits vessel


10


through overflow exit


22


. As is know in the art, in order to vary fluid flow through vessel


10


, the vessel must be opened so that one or more hydrocyclone liners


12


may be added or removed and replaced with a blank liner (not shown) which provides no flow.




In one embodiment of the invention, a plurality of hydrocyclone liners may be arranged in any manner to provide efficient use of space within a new or existing hydrocyclone separator. The hydrocyclone liners may be arranged in an opposing configuration in such a way that an overflow end of one hydrocyclone liner and an underflow end of another hydrocyclone liner are positioned at one end of a vessel. The hydrocyclone liners may, but need not be, positioned in a single alternating pattern wherein each hydrocyclone liner is oppositely positioned in an alternating arrangement so that the overflow end of each hydrocyclone liner is positioned near the underflow end of an adjacent hydrocyclone liner. In another embodiment, the hydrocyclone liners may be positioned in a multiple alternating pattern, wherein a set of two or more hydrocyclone liners are oppositely positioned near another set of two or more hydrocyclone liners, and the overflow ends of each of the hydrocyclone liners within the set are similarly positioned at one end of a hydrocyclone vessel.




In another embodiment, a plurality of hydrocyclone liners may be grouped together in a hydrocyclone bundle. In one embodiment, a plurality of hydrocyclone liners may be arranged in an opposing configuration in such a way that an overflow end of one hydrocyclone liner and an underflow end of another hydrocyclone liner are positioned at one end of the bundle. In another embodiment, a plurality of hydrocyclone liners are bundled such that the overflow end of each of the liners is positioned at one end of the hydrocyclone bundle. Multiple hydrocyclones may be bundled in any shape or pattern to efficiently utilize available space in a new or existing pipe or vessel. The bundle of hydrocyclone liners may have any overall cross sectional area and comprise any number of hydrocyclone liners useful for a particular purpose. The cross sectional area of the bundle may vary depending on the diameter of the hydrocyclone liners used. The cross sectional area of the bundle may be configured to maximize the number of bundles which may be used in a new or existing hydrocyclone separator. The cross sectional areas of the bundles may be configured to be close packed.




The hydrocyclone bundle may, but need not, comprise an even number of hydrocyclones for close packing. The hydrocyclone liners may be similarly positioned within the bundle so that the over flow ends of each hydrocyclone liner are positioned at one end of the hydrocyclone bundle. Alternatively, the hydrocyclone liners within the bundle may be arranged in a variety of opposing configurations. As used herein, the phrase “opposing configuration” is used to define a configuration of hydrocyclone liners in which an overflow end of at least one hydrocyclone liner and the underflow end of at least another hydrocyclone liner are positioned at one end of a hydrocyclone separator. A variety of configurations may be imagined, such as the single alternating pattern or multiple alternating pattern mentioned above. In a preferred embodiment, a plurality of hydrocyclone liners are oppositely positioned in a bundle to increase the number of hydrocyclone liners per a given area.




Any hydrocyclone liner may be bundled in an opposite configuration to increase the number of hydrocyclone liners per a given area. The hydrocyclone liner may have a continuous or jointed taper between a wide overflow end and a narrow underflow end. In one embodiment a hydrocyclone liner having a separating section with a cross sectional area that gradually and continuously decreases toward the underflow end may be used. One example of a liner is disclosed by Schubert in U.S. Pat. No. 5,667,686, incorporated herein by referenced for all purposes.




The hydrocyclone bundle may comprise a plate or plate assembly positioned at one or both ends of the bundled hydrocyclones. The plate may be constructed and arranged to hold each hydrocyclone liner in place. The plate may also be constructed and arranged to collect effluent from the overflow end and/or underflow end of the hydrocyclone liners. The plate may have any cross sectional area useful for a particular purpose, and may correspond to the cross sectional area of the bundled hydrocyclones. Multiple plates may form a plate assembly constructed an arranged to support each hydrocyclone liner as well as to collect and distribute overflow and underflow effluents from the hydrocyclone liners.




One or more hydrocyclone bundles may be positioned in a variety of separators, such as in piping, a new vessel, and/or a retrofitted vessel. In one embodiment, two or more bundles may be packed one after another in series, such that effluent of one bundle may be directed to an inlet of another bundle. In another embodiment, the two or more bundles may be packed in parallel and fluidly connected in series such that the effluent of one bundle may be directed to an inlet of another bundle. In a preferred embodiment, the bundles may be close packed in parallel so that a fluid to be separated into a less dense component and a more dense component may be simultaneously directed to all bundles. Each bundle in a multiple bundle separator may, but need not, be identical in number, size and position of liners within each bundle.




One or more hydrocyclone liner bundles may be individually fluidly connected to an outlet of the hydrocyclone separator, such that fluid flow may be interrupted at one or any number of the hydrocyclone bundles. For example, the hydrocyclone separator may include a valve fluidly connected to a pair of valves corresponding to the overflow and underflow outlets from a single hydrocyclone bundle or a set of hydrocyclone bundles to be interrupted. Alternatively, all or any number of hydrocyclone bundles may be valved so that flow to a specific hydrocyclone bundle may be interrupted. Because the number of hydrocyclone liners per bundle may be varied, the number and size of bundles used in a separator may be varied, and flow to the bundles may be interrupted individually or as a set, a separator having an almost unlimited turn down ratio may be designed, so that one separator may handle a wide range of fluid flow.




For example, a separator having nine hydrocyclone bundles may have a first pair of valves (pair A) capable of interrupting flow to one hydrocyclone bundle, a second pair of valves (pair B) capable of interrupting flow to two hydrocyclone bundles, a third and fourth pair of valves (pair C and D, respectively) capable of interrupting flow to three hydrocyclone bundles each. As inlet flow increases for the hydrocyclone separator, valve pair A may be opened with all other valves closed, providing one ninth of the total flow capacity of the hydrocyclone separator. As inlet flow increases for the hydrocyclone separator, valve pair A may be closed and valve pair B may be opened with all other valves closed providing two ninths of the total flow capacity of the hydrocyclone separator. As inlet flow increases still further for the hydrocyclone separator, valve pair B may be closed and valve pair C (or D) may be opened with all other valves closed providing one third of the total flow capacity of the hydrocyclone separator. As inlet flow continues to increase for the hydrocyclone separator, valve pair A may be opened and valve pair C (or D) may remain open with all other valves closed providing four ninths of the total flow capacity of the hydrocyclone separator. In response to further increases in flow for the hydrocyclone separator, valve pair A may be closed, valve pair B may be opened and valve pair C (or D) may remain open with all other valves closed providing five ninths of the total flow capacity of the hydrocyclone separator. In response to further increases in flow for the hydrocyclone separator, valve pair A may be opened and valve pair B and valve pair C (or D) may remain open with all other valves closed providing two thirds of the total flow capacity of the hydrocyclone separator. In response to still further increases in flow for the hydrocyclone, all valves except valve pair B may be opened providing seven ninths of the total flow capacity of the hydrocyclone separator. In response to still further increases in flow for the hydrocyclone all valves except valve pair A may be opened providing eight ninths of the total flow capacity of the hydrocyclone separator. Lastly, with all valves opened 100% of the hydrocyclone separator capacity may be provided. This combination of flow control valves maintains the flow rate through, and associated pressure drop across each hydrocyclone bundle and or liner.




One or more valves may be manually or automatically controlled. In one embodiment, as an example, the valves may automatically respond to a signal originating from a sensor which may detect pressure, flow rate, or another characteristic, The signal may be any suitable signal, such as, a pneumatic signal, a mechanical signal, an electrical signal, or the like. The sensor may be located in any appropriate position for a particular purpose, such as, upstream of the separator. The valve(s) may be a check valve, a gate valve, a diaphragm valve, a glove valve, a butterfly valve, or the like. In response to the signal, the valve may respond by fully opening and closing in some embodiments, or by partially opening and closing in other embodiments. Other methods for regulating the flow to the bundles may also be envisioned.





FIG. 2

shows one embodiment of a hydrocyclone bundle


40


comprising hydrocyclone liners


12


positioned longitudinally in a substantially circular pattern. Although this embodiment is configure to accommodate


12


hydrocyclone liners, as mentioned above, any number of hydrocyclone liners may be used for a particular purpose. In this embodiment, adjacent hydrocyclone liners


12


are oppositely positioned in an alternating arrangement, such that an overflow end


14


of one hydrocyclone liner


12


is positioned near an underflow end


16


of an adjacent hydrocyclone liner


12


. Because hydrocyclone liners typically have a wide overflow end


14


and taper to a narrow underflow end


16


, the opposing positions of the hydrocyclone liners


12


allow more hydrocyclone liners


12


to be positioned in an area than would be capable if all hydrocyclone liners


12


were uniformly positioned in an identical area with each overflow end


14


located at one end of the vessel


10


. In this embodiment, a plurality of overflow ends


14


, each having an overflow exit, and a plurality of underflow ends


16


, each having an underflow exit, are located at each end of the hydrocyclone bundle. Plate assembly


42


collects and separates the overflow and underflow effluents.




As shown in

FIG. 3

, in one embodiment, plate assembly


42


may comprise a plurality of plates


44


,


46


, and


48


positioned at each end of the hydrocyclone bundle


40


. The plates may be constructed an arranged to collect and direct overflow and/or underflow effluents. Overflow and underflow effluents may exit hydrocyclone bundle


40


at the same or opposite ends of hydrocyclone bundle


40


.

FIG. 17

shows an embodiment of a hydrocyclone bundle having an overflow exit


126


and underflow exit


124


. The plurality of plates may be flush mounted together, welded, bolted or otherwise compressed with or without a gasket material to prevent leakage of one process stream into another. The plates may, but need not, be attached to a separator vessel. The plurality of plates when assembled in any fashion described herein, or evident to one skilled in the art, may maintain a pressure differential over their outer surfaces and their inner void surfaces. Conventional overflow plate


34


and underflow plate


30


shown in

FIG. 1

are typically metal plates designed to resist the forces generated by the pressure differential acting on the area of the plates. Because hydrocyclone separators utilize pressure differential to affect separation, the pressures present in the inlet area


28


of the hydrocyclone separator can be several hundred pounds per square inch greater than the pressures present in the overflow collection volume


36


and underflow collection volume


32


. By replacing the overflow plate


34


and underflow plate


30


with a plurality of, smaller plate assemblies which are themselves not required to maintain a pressure differential, the cost and weight of the plates required to maintain a given pressure drop may significantly be reduced. By exposing all outer surfaces of the plate assembly to the same inlet pressure, the forces acting on the plate assembly may be balanced. The forces acting on the individual plates as they retain the differential pressures found in the higher pressure inlet volume and the lower pressure overflow and underflow collection volumes are compressive in nature and may place less mechanical loading on the plates. This compressive load may require much less mechanical strength than the shear forces encountered by the typically much larger conventional flat plate required to resist several hundred pounds of pressure distributed across the plate's area while displaying only negligible deflection across the plate's diameter.




Referring again to

FIG. 3

, backing plate


44


comprises a body


50


having a first surface


52


, a second surface


54


, and a plurality of passageways extending through the body


50


from the first surface


52


to the second surface


54


. Underflow passageway


56


may be constructed and arranged to receive the underflow end


16


of hydrocyclone liner


12


. As used herein, the term “receive” is defined as to bear the weight or force of an element being received. The receipt of an element by a passageway extending through a body may, but need not, provide a fluid tight seal to prevent the passage of fluids which may be present at either or both surfaces of the body. In another embodiment, passageway


56


may be fluidly connected to the underflow exit of hydrocyclone liner


12


. Overflow passageway


58


may be constructed and arranged to receive an overflow exit of hydrocyclone liner


12


. In another embodiment, passageway


58


may be fluidly connected to the overflow exit of hydrocyclone liner


12


. Passageway


90


may be constructed and arranged to receive an overflow conduit (not shown). In another embodiment, passageway


90


may be fluidly connected to passageway


70


of overflow plate


46


.




Overflow plate


46


comprises a body


60


having a first surface


62


, a second surface


64


, and a plurality of underflow passageways


66


extending though the body


60


from the first surface


62


to the second surface


64


. Underflow passageway


66


may be constructed and arranged to receive the underflow end


16


of hydrocyclone liner


12


. In another embodiment, underflow passageway


66


may be fluidly connected to underflow passageway


56


of backing plate


44


. Overflow plate


46


may also comprise a recess


68


in the second surface


64


constructed and arranged to collect overflow effluent from the overflow end


14


of hydrocyclone liner


12


. Recess


68


may also be constructed and arranged to receive an overflow exit of hydrocyclone liner


12


. Recess


68


may have any shape and depth suitable for a particular purpose. Overflow plate


46


may, but need not, comprise passageway


70


extending from recess


68


through body


60


to the first surface


62


. Passageway


70


may be constructed and arranged to receive an overflow conduit (not shown). In another embodiment, passageway


70


may be fluidly connected to passageway


90


of backing plate


44


, and/or fluidly connected to passageway


38


of underflow plate


48


.




Underflow plate


48


comprises a body


72


having a first surface


74


, a second surface


76


having a recess


78


. Recess


78


may be constructed and arranged to collect underflow effluent from the underflow end


16


of hydrocyclone


12


. Recess


78


may also be constructed and arranged to receive the underflow end


16


of hydrocyclone liner


12


. Recess


78


may have any shape and depth suitable for a particular purpose. Underflow passageway


80


extends through the body


72


from the recess


78


in the second surface


74


to the first surface. Passageway


80


may be constructed and arranged to receive the underflow end


16


of hydrocyclone liner


12


. Alternatively, passageway


80


may be fluidly connected to the underflow exit of hydrocyclone liner


12


. Underflow plate


48


may, but need not, have passageway


38


, constructed and arranged to receive underflow conduit


88


, as shown in FIG.


4


. In another embodiment, passageway


38


may be fluidly connected to underflow passageways


66


of overflow plate


46


.





FIG. 4

shows a cut away section of the bundle of

FIG. 2

illustrating underflow conduit


88


extending between each plate assembly. Underflow conduit


88


may be constructed and arranged to be received by passageways


82


,


84


and


86


of plates


48


,


46


, and


44


, respectively. In another embodiment, an inlet or outlet of underflow conduit


86


may be in fluid communication with passageways


82


,


84


, and


86


. Underflow conduit


88


is in fluid communication with recess


78


of plate


48


allowing the underflow effluent to flow from the underflow end


16


of hydrocyclone liners


12


to the underflow end


16


of oppositely positioned hydrocyclone liners


12


.




The hydrocyclone bundle


40


may also comprise an overflow conduit (not shown) extending between each plate assembly. The overflow conduit may be constructed and arranged to be received by passageway


38


of underflow plate


48


, passageway


70


of overflow plate


46


, and/or passageway


90


of backing plate


44


. In another embodiment, the overflow conduit may be in fluid communication with passageways


38


,


70


, and/or


90


.




Two embodiments of an underflow plate are shown in

FIGS. 5



a


,


5




b


,


6




a


and


6




b.







FIGS. 5



a


and


6




a


show an underflow plate


92


which may be positioned near an overflow outlet of the hydrocyclone bundle.

FIG. 5



b


represents an underflow plate


94


which may be positioned near an opposite end of the hydrocyclone bundle. Underflow plate


94


comprises a recess in a first surface (not shown) which collects underflow effluent of the hydrocyclone liners when the surface is sealingly positioned adjacent solid endplate


96


. As used herein, the phrase “sealingly positioned adjacent” is defined as contact which provides a fluid tight seal between and among corresponding passageways. A fluid tight seal may include a gasket positioned between adjacent plates, sealing groves on a surface of one or both plates to accept a gasket, or a boss portion on one or both plates. A void resulting from a seal between endplate


94


of FIG.


11


and underflow plate


94


allows the underflow effluent to be collected and directed through passageway


82


and conduit


88


to the opposite end of the hydrocyclone bundle. The underflow effluent then passes through passageway


82


of underflow plate


92


of

FIGS. 5



a


and


6




a


mixing with underflow effluent entering recess


78


of underflow plate


92


from the underflow end of the hydrocyclone liners positioned in passageways


80


, or directly from passageways


80


which are fluidly connected to the underflow end of the hydrocyclone liners. The first surface


74


of underflow plate


92


is sealingly positioned adjacent endplate


98


of

FIG. 10

forming a collection void. Underflow effluent passes through underflow passageway


108


of endplate


98


exiting the hydrocyclone bundle. Underflow plate


92


comprises passageway


38


that accommodates an overflow conduit allowing the overflow effluent collected at the opposite end of the hydrocyclone bundle to pass through underflow plate


92


.




Two embodiments of an overflow plate are illustrated in

FIGS. 7



a


,


7




b


,


8




a


, and


8




b.







FIGS. 7



a


and


8




a


illustrate a first side of an overflow plate


100


positioned near an overflow exit of a hydrocyclone bundle.

FIGS. 7



b


and


8




b


illustrate a second side of an overflow plate


102


positioned at an opposite side of the hydrocyclone bundle. Overflow plate


102


comprises a recess


68


in a second surface


64


which collects overflow effluent from the overflow end of the hydrocyclone liners when the second surface


64


is sealingly positioned adjacent a backing plate


104


. A void resulting from a seal between backing plate


104


and the overflow plate


102


allows the overflow effluent to be collected and directed through the overflow conduit fluidly connected to the recess


68


by passageway


90


of the backing plate


104


. Overflow effluent passes through overflow conduit, to the opposite end of the hydrocyclone bundle, through passageway


90


of a second backing plate


104


which is sealingly positioned adjacent a second surface of overflow plate


100


of

FIGS. 7



a


and


7




b


. A recess in the second surface of overflow plate


100


(not shown) provides a collection void when sealingly positioned adjacent to the second backing plate


104


. Overflow effluent from the overflow conduit, as well as from the overflow ends of hydrocyclone liners fluidly connected to the recess


68


and passageway


70


in overflow plate


100


are collected and passed through passageway


38


of underflow plate


92


to an exit of the hydrocyclone liner bundle.




An embodiment of a backing plate


104


is shown in

FIGS. 9



a


and


9




b


depicting a first and second side, respectively. As previously mentioned, when baking plate


104


is sealingly positioned adjacent overflow plate


100


or


102


, an overflow collection void is formed to collect overflow effluent for further distribution. Overflow effluent enters the void through an overflow exit of the hydrocyclone liner positioned in passageway


58


. Passageway


90


of backing plates


104


positioned at opposing ends of the hydrocyclone bundle receive an overflow conduit allowing overflow effluent from a first overflow collection void to flow to a second overflow collection void at the opposing end of the hydrocyclone bundle. Passageway


86


of backing plates


104


positioned at opposing ends of the hydrocyclone bundle receive an underflow conduit for passing underflow effluent from a first underflow collection void located at one end of the hydrocyclone bundle to a second underflow collection void located at an opposing end of the hydrocyclone bundle.




Additional plates


98


and


94


shown respectively in

FIGS. 10 and 11

may be included in a plate assembly. End plate


94


comprises a solid surface that when sealingly positioned adjacent a first surface


74


of underflow plate


106


forms an overflow collection void, collecting underflow effluent from the underflow end of one set of hydrocyclone liners. The underflow effluent passes through the underflow conduit to an underflow collection void formed when the first surface of underflow plate


92


is sealingly positioned adjacent end plate


108


at the other end of the hydrocyclone bundle. End plate


108


comprises passageways


108


and


110


each constructed and arranged to receive an underflow exit and an overflow exit of the hydrocyclone bundle.





FIGS. 12



a


and


12




b


show one embodiment of a hydrocyclone liner having a nipple


112


located at the overflow end


114


of the hydrocyclone liner that may be used with a plate assembly. Nipple


112


may be inserted through overflow passageway


58


of backing plate


104


and into recess


68


of overflow plates


100


or


102


. The recess


68


, may be constructed and arranged to receive nipple


112


. For example, recess


68


may comprise groove


116


to support the nipple


112


of the hydrocyclone liner, and allow overflow effluent to be collected in the recess.

FIG. 13

shows a side view of the hydrocyclone liner having nipple


112


and overflow exit


116


. Nipple


112


may be fluidly sealed to backing plate


104


. For example, nipple


112


may comprise an o-ring and or a groove that sealingly contacts an inner wall of passageway


58


. In another embodiment, overflow end may comprise an o-ring gland and/or a groove that sealingly contacts one of the surfaces of backing plate


104


.

FIG. 12



c


shows an underflow end of a hydrocyclone liner having an outer surface


118


. The underflow end may be inserted into one or more plates, and may be constructed and arranged to provide a fluid tight seal with one or more plates. In one embodiment, the underflow end may comprise a groove (not shown) on outer surface


118


. The groove may receive a seal, such as a gasket or o-ring. The groove may be constructed and arranged to receive a corresponding boss on the inner surface of any of passageways


56


,


66


, and


80


of plates


44


,


46


, and


48


respectively. The outer surface of the underflow end may be threaded to mate with corresponding threads in passageways


55


,


66


, and/or


80


.





FIG. 14

is a perspective view of another hydrocyclone bundle having a plurality of hydrocyclone liners


12


. Although this embodiment accommodates


16


hydrocyclone liners, as noted above, any number of liners may be used. In this embodiment, each of the sixteen hydrocyclone liners is oppositely positioned in an alternating pattern, such that the overflow end of each hydrocyclone liner is positioned adjacent the underflow end of an adjacent hydrocyclone liner. In

FIG. 15

, one embodiment of an underflow plate


122


is constructed and arranged to receive the underflow ends of eight hydrocyclone liners. Passageways


80


receive the underflow end of the individual hydrocyclone liners. As seen in

FIGS. 19A

,


19


B and


19


C, underflow plate


122


has a first surface


74


having a protruded periphery portion


132


extending outward from the first surface defining a collection recess. The protruded periphery portion is constructed and arranged to provide a collection space for underflow effluent. In one embodiment illustrated in

FIGS. 19A

,


19


B and


19


C, the protruded periphery portion


132


is positioned adjacent an outer perimeter of underflow plate


122


to collect effluent from conduit


88


, illustrated in

FIG. 16

, via passageway


82


and from the underflow end of individual hydrocyclone liners positioned in passageways


80


. In another embodiment, the protruded periphery portion may be positioned adjacent passageway


82


so that effluent from the underflow and the individual hydrocyclone liners positioned in passageways


80


, may be collected and passed to conduit


88


. In another embodiment, conduit


88


may extend through passageway


80


and may further define a collection space. Underflow effluent exits the underflow end of the hydrocyclone liners and enters underflow collection space


128


, illustrated in

FIG. 16

, formed between endcap


130


, first surface


74


, and protruded periphery portion


132


. Underflow effluent may then pass through conduit


88


to the opposing side of the bundle for collection with the underflow effluent from the remaining 8 hydrocyclone liners. Underflow plate


122


may comprise overflow passageways


38


to pass overflow effluent to an opposing side of the hydrocyclone bundle or out of the hydrocyclone bundle. Underflow plate


122


may be used in conjunction with an overflow plate and/or a backing plate. In another embodiment, underflow plate


122


may comprise an overflow recess in an opposing surface such that overflow effluent from 8 of the hydrocyclone liners is redirected to the opposing side of the hydrocyclone bundle while underflow effluent passes into underflow collection space


128


.





FIGS. 18A

,


18


B and


18


C illustrate another embodiment of an overflow plate constructed and arranged to be used without a backing plate. Overflow plate


136


comprises a body


60


having a first surface


62


, a second surface


64


and a plurality of underflow passageways


66


extending through the body


60


from the first surface


62


to the second surface


64


. Underflow passageways


66


may be constructed and arranged to receive the underflow end


16


of hydrocyclone liner


12


. Overflow plate


136


may also comprise a recess


68


in the second surface


64


constructed and arranged to collect overflow effluent from the overflow end


14


of hydrocyclone liner


12


. Recess


68


may also be constructed and arranged to receive an overflow exit of hydrocyclone liner


12


. Recess


68


may have any shape and depth suitable for a particular purpose.




The hydrocyclone bundle of

FIG. 14

may be used in parallel or in series with other hydrocyclone bundles. Endcap


130


allows the underflow effluent to be redirected to on side of the hydrocyclone bundle. By removing endcap


130


, a plurality of hydrocyclone bundles may be fluidly connected in series, such that the underflow effluent may be directed from a final hydrocyclone bundle in the series having a cap. The underflow effluent then passes through conduits


88


of each hydrocyclone bundle fluidly connected to each other.




It is to be appreciated that a wide variety of individual plate configurations and plate assemblies may be designed for a particular purpose. For example, as shown in

FIGS. 18A-18C

, an overflow plate and an underflow plate may be combined into one plate. Similarly, an overflow plate and an underflow plate may be combined into one plate.




Those skilled in the art will readily appreciate that all parameters listed herein are meant to be exemplary and actual parameters depend upon the specific application for which the methods and materials of the present invention are used. It is, therefore, to be understood that the foregoing embodiments are presented by way of example only and that, within the scope of the appended claims and equivalents thereto, the invention can be practiced otherwise than as specifically described.




While several embodiments of the invention have been described and illustrated herein, those of ordinary skill in the art will readily envision a variety of other means and structures for performing the functions and/or obtaining the resuits or advantages described herein, and each of such variations or modifications is deemed to be within the scope of the present invention. More generally, those skilled in the art would readily appreciate that all parameters, dimensions, materials, and configurations described herein are meant to be exemplary and that actual parameters, dimensions, materials, and configurations will depend upon specific applications for which the teachings of the present invention are used. Those skilled in the art will recognize, or be able to ascertain using no more than routine experimentation, many equivalents to the specific embodiments of the invention described herein. It is, therefore, to be understood that the foregoing embodiments are presented by way of example only and that, within the scope of the appended claims and equivalents thereto, the invention may be practiced otherwise than as specifically described. The present invention is directed to each individual feature, system, material and/or method described herein. In addition, any combination of two or more such features, systems, materials and/or methods, if such features, systems, materials and/or methods are not mutually inconsistent, is included within the scope of the present invention.




In the claims (as well as in the specification above), all transitional phrases such as “comprising,” “including,” “carrying,” “having,” “containing,” “involving,” and the like are to be understood to be open-ended, i.e. to mean including but not limited to. Only the transitional phrases “consisting of” and “consisting essentially of” shall be closed or semi-closed transitional phrases, respectively, as set forth in the United States Patent Office Manual of Patent Examining Procedures, section 2111.03.



Claims
  • 1. A method of separating a fluid, comprising:providing a fluid having a less dense component and a more dense component; feeding the fluid to inlets of a plurality of hydrocyclone liners thereby separating the less dense component and the more dense component; collecting the less dense component from a portion of the hydrocyclone liners in a first plate assembly; passing the less dense component to a second plate assembly; removing the less dense component from the second plate assembly; and removing the more dense component from one of the first plate assembly and the second plate assembly.
  • 2. The method of claim 1, further comprising:collecting the more dense component from a portion of the hydrocyclone liners in the first plate assembly; passing the more dense component to a second plate assembly; and removing the more dense component from the second plate assembly.
  • 3. The method of claim 1, further comprising:collecting the more dense component from a portion of the hydrocyclone liners in the second plate assembly; passing the more dense component to the first plate assembly; and removing the more dense component from the first plate assembly.
  • 4. A method of facilitating separating a fluid having a less dense component and a more dense component, comprising:providing a hydrocyclone bundle having a plurality of hydrocyclone liners, a first plate assembly, and a second plate assembly in a vessel; feeding the fluid to inlet of the hydrocyclone liners thereby separating the less dense component and the more dense component; collecting the less dense component from a portion of the hydrocyclone liners in a first plate assembly; passing the less dense component to a second plate assembly; collecting the more dense component from a portion of the hydrocyclone liners in the first plate assembly; passing the more dense component from the first plate assembly to the second plate assembly; and removing the less dense component and the more dense component from the second plate assembly.
  • 5. The method of claim 4, wherein the vessel is a tank.
  • 6. The method of claim 4, wherein the vessel is a pipe.
US Referenced Citations (35)
Number Name Date Kind
4208270 Grieve et al. Jun 1980 A
4389307 Boadway Jun 1983 A
4622150 Carroll Nov 1986 A
4650584 Macierewicz Mar 1987 A
4673495 Carroll et al. Jun 1987 A
4698152 Carroll Oct 1987 A
4711720 Young Dec 1987 A
4816165 Carroll et al. Mar 1989 A
4857197 Young et al. Aug 1989 A
4927536 Worrell et al. May 1990 A
4960525 Dalby et al. Oct 1990 A
4995989 Carroll et al. Feb 1991 A
5009785 Webb Apr 1991 A
5071556 Kalnins et al. Dec 1991 A
5071557 Schubert et al. Dec 1991 A
5154826 Prendergast et al. Oct 1992 A
5194150 O'Brien et al. Mar 1993 A
5336410 O'Brien et al. Aug 1994 A
5401411 Andersson Mar 1995 A
5499720 Bouchillon et al. Mar 1996 A
5667686 Schubert Sep 1997 A
5667687 Lange Sep 1997 A
5858237 Hashmi et al. Jan 1999 A
5965021 Hesse et al. Oct 1999 A
5980639 Trickey et al. Nov 1999 A
6129217 Trickey et al. Oct 2000 A
6209641 Stevenson Apr 2001 B1
6214220 Favret, Jr. Apr 2001 B1
6238579 Paxton et al. May 2001 B1
6312594 Conrad et al. Nov 2001 B1
6315837 Barclay Nov 2001 B1
6378608 Nilsen et al. Apr 2002 B1
6464884 Gadgil Oct 2002 B1
6627081 Hilditch et al. Sep 2003 B1
20010002009 Gil et al. May 2001 A1
Non-Patent Literature Citations (7)
Entry
Colman, D.A. and Thew, M.T., “Correlation of Separation Results from Light Dispersion Hydrocyclones,” Chem Eng. Res. Des., vol. 61, Jul. 1983, pp. 233-240.
Smyth, I.C. and Thew, M.T., “The Use of Hydrocyclones in the Treatment of Oil Contaminated Water Systems,” 1st International Symposium on Oil and Gas Exploration and Production Management Practices, New Orleans, USA, 1990, pp. 1001-1012.
Wolbert, B. MA, B.-F., and Aurelle, Y., “Efficiency Estimation of Liquid-Liquid Hydrocyclones Using Trajectory Analysis,” AlChE Journal, Jun., 1995, vol. 41, No. 6, pp. 1395-1402.
Axsia - Total Solutions -Produced Water Treatment Systems -Liquid/Liquid Hydrocyclones, 9 pages from http://www.axsia.com on Jul. 17, 2001.
Baker-Baker Process, 7 pages from http://www.bakerhughes.com on Jul. 17, 2001.
Cyclotech-Separation technologies for the petroleum industry, 3 pages from http://www.cyclotech.co.uk.
U.S. Filter, High Efficiency Liquid/Liquid Hydrocyclone, 1 page from http://www.usfilter.com ,on Jul. 2001.