Patent Grant
10105726
The present disclosure relates to fluid flow devices, and more particular to a fluid flow sinker.
Fluid is typically extracted from a vessel by a tube. The tube can have a soft construction, allowing it to move within the vessel. Conversely, the tube can have a hard construction, such that it is adapted to remain rigid during fluid removal. A negative pressure can be applied within an internal bore of the tube, causing a fluid to flow through the tube at a desired flow rate. In the case of soft tubes, such as, for example, those typically used in the manufacturing of pharmaceuticals, application of a negative pressure within the tube can cause the tube to stick against a sidewall of the vessel. Once stuck, the negative pressure formed within the tube can generate a vacuum, preventing the tube from decoupling from the sidewall of the vessel and resulting in the termination, or halt, of fluid flow.
Any termination of fluid flow can increase the time required to evacuate the vessel and, especially in the case of pharmaceuticals where the fluid can be delicate and expensive, raise operating costs. In timed applications, where suction is applied to the tube for a predefined period of time, even a temporary termination or reduction in fluid flow can result in a larger portion of the fluid remaining in the vessel. Particularly in the pharmaceutical industry, even the smallest loss in fluid can render an operation unsustainable.
There continues to exist a need for a device that can permit unrestricted, or nearly unrestricted, fluid flow while simultaneously preventing a tube from forming a vacuum against a sidewall or a bottom surface of a vessel.
Embodiments are illustrated by way of example and are not limited in the accompanying figures.
The following description in combination with the figures is provided to assist in understanding the teachings disclosed herein. The following discussion will focus on specific implementations and embodiments of the teachings. This focus is provided to assist in describing the teachings and should not be interpreted as a limitation on the scope or applicability of the teachings. However, other embodiments can be used based on the teachings as disclosed in this application.
The terms “comprises,” “comprising,” “includes,” “including,” “has,” “having” or any other variation thereof, are intended to cover a non-exclusive inclusion. For example, a method, article, or apparatus that comprises a list of features is not necessarily limited only to those features but may include other features not expressly listed or inherent to such method, article, or apparatus. Further, unless expressly stated to the contrary, “or” refers to an inclusive- or and not to an exclusive- or. For example, a condition A or B is satisfied by any one of the following: A is true (or present) and B is false (or not present), A is false (or not present) and B is true (or present), and both A and B are true (or present).
Also, the use of “a” or “an” is employed to describe elements and components described herein. This is done merely for convenience and to give a general sense of the scope of the invention. This description should be read to include one, at least one, or the singular as also including the plural, or vice versa, unless it is clear that it is meant otherwise. For example, when a single item is described herein, more than one item may be used in place of a single item. Similarly, where more than one item is described herein, a single item may be substituted for that more than one item.
Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. The materials, methods, and examples are illustrative only and not intended to be limiting. To the extent not described herein, many details regarding specific materials and processing acts are conventional and may be found in textbooks and other sources within the fluid transportation arts.
A fluid flow sinker in accordance with one or more of the embodiments described herein can generally include a body having a generally cylindrical sidewall, a first end, a second end, and an aperture extending between the first and second ends. The second end of the body can be adapted to receive a tube in a manner such that the tube is in fluid communication with the aperture. The fluid flow sinker can further include a fluid passageway disposed on the first end of the body and extending from the generally cylindrical sidewall to the aperture. In this regard, a fluid can be drawn into the aperture at all times, including when the first end of the body is flush against, or parallel with, a surface of a vessel.
A fluid flow sinker assembly in accordance with one or more of the embodiments described herein can generally include a fluid flow sinker as described above and a tube in fluid communication with the aperture of the fluid flow sinker. The tube can extend from the second end of the fluid flow sinker to a second position, external to a vessel into which the fluid flow sinker can be positioned, where the tube can be coupled with a fluid urging device, such as, for example, a pump. In such a manner, the fluid flow sinker can cause the tube to remain submerged within a vessel while simultaneously preventing the tube from forming an air lock, e.g., a vacuum, with a wall of the vessel, thus enhancing fluid flow properties.
Referring initially to
In a further embodiment, when viewed from a side view, the generally cylindrical sidewall 104 can have a first diameter as measured at a first location, e.g., the first end 106, and a second diameter as measured at a second location, e.g., the second end 108, and the first and second diameters can differ by no greater than 5%. In such a manner, the generally cylindrical sidewall can be frustoconical, hour glass-shaped, or can have any other suitable configuration. As discussed in greater detail below, such a configuration may increase the volume of fluid that can be removed from a vessel.
The fluid flow sinker 100 can have a maximum diameter, DMAX, as measured by a maximum distance extending between diametrically opposite locations of the generally cylindrical sidewall 104, and a maximum length, LMAX, as measured by a maximum distance between the first and second ends 106 and 108. In particular embodiments LMAX/DMAX can be no less than 1.25, such as no less than 1.5, no less than 1.75, no less than 2.0, no less than 2.5, no less than 3.0, no less than 4.0, or even no less than 5.0. In further embodiments, LMAX/DMAX can be no greater than 10.0, such as no greater than 8.0, or even no greater than 6.0. Moreover, LMAX/DMAX can be within a range between and including any of the values described above, such as, for example, between 4.0 and 4.5.
In certain embodiments, a surface 116 of the first end 106 of the body 102 can be generally flat. As used herein, “generally flat” refers to a surface having all point locations along the surface deviate by no greater than 5%. In further embodiments, the surface 116 can be pitted, dimpled, or otherwise contoured. In other embodiments, the surface 116 can be flat. As used herein, the term “flat” refers to a surface having no greater than a nominal surface deviation (e.g., less than about 0.1%) as caused by acceptable tolerances exhibited during normal manufacturing processes, e.g., normal surface roughness.
In particular embodiments, the second end 108 can be at least partially outwardly rounded. In further embodiments, such as illustrated in
Referring now to
In a non-illustrated embodiment, the aperture can extend between one of the first and second ends and the generally cylindrical sidewall. In such a manner, the aperture can form a relative angle with the first end of the body. In such a manner, the aperture does not pass between opposing ends of the fluid flow sinker.
The aperture 110 can define an average diameter, DA, through which a fluid can pass. In particular embodiments, DMAX/DA can be at least 1.1, such as at least 1.2, at least 1.3, at least 1.4, at least 1.5, at least 1.75, or even at least 2.0. In further embodiments, DMAX/DA can be no greater than 4.0, such as no greater than 3.5, no greater than 3.0, no greater than 2.5, or even no greater than 2.25. Moreover, DMAX/DA can be within a range between and including any of the values described above, such as, for example, between 1.3 and 1.6. A person of ordinary skill will understand that as DMAX/DA increases, the relative weight of the fluid flow sinker 100 to the maximum fluid flow through the aperture 110 increases. Conversely, as DMAX/DA decreases, the generally cylindrical sidewall 104 of the body 102 can weaken such that the fluid flow sinker 100 collapses during operation. Therefore, in a particular embodiment, DMAX/DA is between 1.1 and 2.5, such as between 1.2 and 1.7, or even between 1.3 and 1.5.
In a particular embodiment, the diameter, DA, of the aperture 110 can be constant, as measured along a length of the aperture 110. In another embodiment, the diameter of the aperture 110 can vary along a length of the aperture 110. For example, as illustrated in
In a further embodiment, the aperture 110 can have a gradually increasing diameter. For example, as illustrated in
A person of ordinary skill will understand that an aperture having a constant, or nearly constant, diameter may cause a more laminar fluid flow which may reduce aspiration of the fluid being passed therethrough. Alternatively, an aperture having a varying diameter may cause a turbulent fluid flow which may result in increased aspiration of the fluid. Certain fluids, e.g., certain pharmaceuticals, are susceptible to damage upon subjection to turbulent fluid flow. Therefore, selection of the proper aperture diameter and shape may be dependent upon application.
In certain embodiments, the body 102 of the fluid flow sinker 100 can comprise a material having an average density, as measured at 39° F., of no less than 1.0 g/cm3, such as no less than 1.05 g/cm3, no less than 1.1 g/cm3, no less than 1.15 g/cm3, no less than 1.2 g/cm3, no less than 1.25 g/cm3, or even no less than 1.3 g/cm3. In further embodiments, the body 102 can comprise a material having an average density, as measured at 39° F., of no greater than 10.0 g/cm3, such as no greater than 8.0 g/cm3, no greater than 5.0 g/cm3, no greater than 3 g/cm3, or even no greater than 2.0 g/cm3. Moreover, the body 102 of the fluid flow sinker 100 can comprise a material having an average density within a range between and including any of the values described above, such as, for example, between 2.1 g/cm3 and 3.1 g/cm3.
In certain embodiments, the fluid flow sinker 100 can have a total mass of less than 500 grams, such as less than 400 grams, less than 300 grams, less than 200 grams, or even less than 100 grams. In further embodiments, the fluid flow sinker 100 can have a total mass of at least 5 grams, such as at least 20 grams, at least 40 grams, or even at least 75 grams. Moreover, the fluid flow sinker 100 can have a mass within a range between and including any of the values described above, such as, for example, between 90 grams and 150 grams. The density of the fluid flow sinker 100 may be important during fluid flow operations, e.g., filling or emptying of a vessel. Specifically, by having an average density greater than the density of water (or the fluid into which the fluid flow sinker is submerged), the fluid flow sinker 100 can sink, allowing for more complete fluid removal from the vessel.
In a particular embodiment, the fluid flow sinker 100 can at least partially comprise a polymer. Exemplary polymers can include, for example, a polyketone, a polyaramid, a polyimide, a polytherimide, a polyphenylene sulfide, a polyethersulfone, a polysulfone, a polyphenylene sulfone, a polyamideimide, ultra high molecular weight polyethylene, a fluoropolymer, a polyamide, a polybenzimidazole, or any combination thereof.
An example fluoropolymer can include a fluorinated ethylene propylene (FEP), a polytetrafluoroethylene (PTFE), a polyvinylidene fluoride (PVDF), a perfluoroalkoxy (PFA), a terpolymer of tetrafluoroethylene, a hexafluoropropylene, and a vinylidene fluoride (THV), a polychlorotrifluoroethylene (PCTFE), an ethylene tetrafluoroethylene copolymer (ETFE), an ethylene chlorotrifluoroethylene copolymer (ECTFE), or any combination thereof.
In another embodiment, the fluid flow sinker 100 can at least partially comprise a metal. In yet a further embodiment, the fluid flow sinker 100 can at least partially comprise an alloy. It may be desirable in certain applications for the fluid flow sinker 100 to comprise a polymer/metal combination. In particular, a polymer body can be overmolded or otherwise attached to a metal component, thereby increasing the average density of the fluid flow sinker. In certain embodiments, the fluid flow sinker can include an outer layer adapted to prevent caustic or otherwise damaging chemical reactions between the body of the fluid flow sinker and the fluid into which the fluid flow sinker is positioned.
Referring again to
As illustrated in
Referring again to
When viewed in cross section, the recess 114 can define a cross-sectional area, AR. In particular embodiments, the cross-sectional area of the recess 114 can be greater than 0.1 in2, such as greater than 0.2 in2, greater than 0.3 in2, greater than 0.4 in2, or even greater than 0.5 in2. In further embodiments, the recess can have a cross-sectional area of less than 2.0 in2, such as less than 1.0 in2, less than 0.75 in2, or even less than 0.6 in2. Moreover, the cross-sectional area of the recess 114 can be within a range between and including any of the values above, such as, for example, between 0.15 in2 and 0.50 in2.
As illustrated in
As illustrated in
In particular embodiments, when viewed from the first end, each of the recesses can lie along a straight line. In other embodiments, when viewed from the first end, each of the recesses can lie along an at least partially ellipsoidal line. In yet further embodiments, when viewed from the first end, each of the recesses can have a plurality of segments disposed at relative angles with respect to each other.
As illustrated in
In particular, the fluid passageway 112 can define a volumetric area, AFPA, as measured by the volume the fluid passage area 112 excluding the projections 122 located within the dashed lines. The total area, as measured between the surface 116 of the first end 106, a plane formed by the generally cylindrical sidewall 104, and a plane formed at a distal surface of the plurality of projections 122, can define a volumetric area, AT. In particular embodiments, AFPA can be no less than 0.05 AT, such as no less than 0.1 AT, no less than 0.25 AT, no less than 0.5 AT, no less than 0.75 AT, or even no less than 0.9 AT. In further embodiments, AFPA can be less than 1 AT, such as less than 0.98 AT, less than 0.96 AT, less than 0.94 AT, less than 0.92 AT, or even less than 0.90 AT. Moreover, AFPA can be within a range between and including any of the values described above, such as, for example, between 0.80 AT and 0.90 AT. A person of ordinary skill will understand that as AFPA increases relative to AT, the volumetric flow rate of a fluid through the passageway 112 can increase. However, this increase can reduce structural integrity of the projections 122 by reducing the size thereof. Hence, in a more particular embodiment, AFPA can be no greater than 0.90 AT.
As contemplated herein, and as illustrated in
In particular embodiments, the tube 200 can be threaded to the body 102 of the fluid flow sinker 100. In other embodiments, the tube 200 can form an interference fit with the body 102 of the fluid flow sinker 100. In yet further embodiments, the tube 200 can be overmolded to the body 102 of the fluid flow sinker 100. In alternate embodiments, the tube 200 can be secured to the body 102 by a fastener or an adhesive.
Preferably, the tube 200 can be selected to have an internal opening that is equal, or almost equal, in diameter to the diameter of the aperture 110. As used herein, the phrase “almost equal” refers to a deviation between two objects of no greater than approximately 5%. For example, the tube 200 can have an internal diameter of approximately 1.0 inch and the aperture 110 can have an inner diameter of between approximately 0.95 inches and approximately 1.05 inches. In such a manner, a fluid can pass through the aperture 110 of the fluid flow sinker 100 and the tube 200 with a more laminar flow. This can reduce aspiration and damage to sensitive fluids being passed therethrough. In other embodiments, an internal diameter of the tube 200 can be larger or smaller than an internal diameter of the aperture 110.
A fluid flow sinker 100 or fluid flow sinker assembly 300 as contemplated herein is not intended to be limited to particular applications or assemblies. By way of non-limiting examples, the fluid flow sinker or fluid flow sinker assembly as contemplated in embodiments herein can be utilized in vessels for household fluids, the manufacturing of pharmaceutical components, or even industrial equipment.
As used herein, the phrase “flow effectiveness ratio” compares the fluid flow rate of a fluid through the fluid flow sinker in an ideal fluid flow situation, e.g., when the fluid flow sinker is positioned furthest from a surface of a vessel, and the fluid flow rate of the fluid through the fluid flow sinker in a worst fluid flow situation, e.g., when the aperture of the fluid flow sinker is disposed at a location adjacent a surface of the vessel. In other words, the flow effectiveness ratio is the ratio of the worst flow rate to the best flow rate of the fluid flow sinker. The fluid flow sinker 100 in accordance with embodiments herein can have a flow effectiveness ratio of no less than 25%, such as no less than 50%, no less than 75%, or even no less than 90%.
As used herein, the phrase “fluid removal percentage” is a measure of the percentage of fluid that can be removed from a vessel. For example, in a vessel which can hold 1 Liter of fluid, removal of 0.95 Liters results in a fluid removal percentage of 95%. The fluid flow sinker 100 in accordance with embodiments herein can have a fluid removal percentage of no less than 90%, such as no less than 95%, no less than 98%, no less than 99%, no less than 99.5%, or even no less than 99.9%. A person of ordinary skill will recognize that the fluid removal percentage from a vessel can be a critical value when the fluid to be removed from the vessel is costly per unit volume. Therefore, a high fluid removal percentage is preferred. A fluid flow sinker 100 having a generally cylindrical sidewall, rather than a rounded, or spherical, sidewall may permit the fluid flow sinker 100 to have an increased fluid removal percentage, especially in non-flat bottomed vessels, as the aperture 110 can reach otherwise unreachable locations, e.g., a corner formed between a sidewall and a bottom surface of a vessel. For example, as illustrated in
As used herein, the phrase “flow/size ratio” is a ratio of the maximum attainable volumetric flow as compared to the volumetric size of the fluid flow sinker. A high flow/size ratio indicates a high fluid flow rate relative to the volumetric size of the body of the fluid flow sinker, e.g., the body of the fluid flow sinker is small as compared to the aperture extending therethrough. A low flow/size ratio indicates a thick body or a small aperture. As contemplated herein, the fluid flow sinker 100 can have a flow/size ratio of no less than 1 in3/sec:1.2 in3.
As used herein, the term “cavitation” refers to the lateral movement, e.g., the X-Y plane movement, of the fluid flow sinker 100 while a fluid passes through the aperture thereof while the fluid flow sinker 100 is separated from a surface of the vessel. “Cavitation” can be measured by movement of the fluid flow sinker in a lateral direction as compared to the maximum diameter, DMAX, of the body. In particular embodiments, the fluid flow sinker 100 can cavitate during a maximum fluid flow by a distance of no greater than 5.0 DMAX, such as no greater than 4.0 DMAX, no greater than 3.0 DMAX, no greater than 2.0 DMAX, or even no greater than 1.0 DMAX. A person of ordinary skill will recognize that reduced cavitation of the fluid flow sinker during filling and unfilling of a vessel may reduce any damage to delicate fluids passing therethrough.
Many different aspects and embodiments are possible. Some of those aspects and embodiments are described below. After reading this specification, skilled artisans will appreciate that those aspects and embodiments are only illustrative and do not limit the scope of the present invention. Embodiments may be in accordance with any one or more of the items as listed below.
Item 1. A fluid flow sinker comprising:
Item 2. A fluid flow sinker comprising:
Item 3. A fluid flow sinker assembly comprising:
Item 4. A fluid flow sinker adapted for use in the production of pharmaceuticals, the fluid flow sinker comprising a body having an aperture adapted to permit a fluid flow, wherein the fluid flow sinker has a fluid removal rate according to the Fluid Removal Test of no less than 95%, such as no less than 98%, no less than 99%, or even no less than 99.5%.
Item 5. A fluid flow sinker comprising a body having an aperture, wherein the fluid flow sinker comprises at least one of the following:
Item 6. The fluid flow sinker or fluid flow sinker assembly according to any one of the preceding items, wherein the fluid flow sinker is adapted to permit a continuous fluid flow for a minimum duration of no less than 5 seconds, no less than 10 seconds, no less than 30 seconds, no less than 60 seconds, no less than 90 seconds, no less than 120 seconds, no less than 180 seconds, or no less than 300 seconds.
Item 7. The fluid flow sinker or fluid flow sinker assembly according to any one of the preceding items, wherein the fluid flow sinker is adapted to permit a continuous fluid flow for a maximum duration of no greater than 1000 seconds, no greater than 600 seconds, no greater than 420 seconds, or no greater than 360 seconds.
Item 8. The fluid flow sinker or fluid flow sinker assembly according to any one of the preceding items, wherein the fluid flow sinker comprises an average density, as measured at 39° F., of no less than 1.0 g/cm3, no less than 1.05 g/cm3, no less than 1.1 g/cm3, no less than 1.15 g/cm3, no less than 1.2 g/cm3, no less than 1.25 g/cm3, or no less than 1.3 g/cm3.
Item 9. The fluid flow sinker or fluid flow sinker assembly according to any one of the preceding items, wherein the fluid flow sinker comprises an average density, as measured at 39° F., of no greater than 10.0 g/cm3, no greater than 8.0 g/cm3, no greater than 5.0 g/cm3, no greater than 3 g/cm3, or no greater than 2.0 g/cm3.
Item 10. The fluid flow sinker or fluid flow sinker assembly according to any one of the preceding items, wherein the fluid flow sinker comprises a total mass of less than 500 g, less than 400 g, less than 300 g, less than 200 g, or less than 100 g.
Item 11. The fluid flow sinker or fluid flow sinker assembly according to any one of the preceding items, wherein the fluid flow sinker comprises a total mass of at least 5 g, at least 20 g, at least 40 g, at least 75 g.
Item 12. The fluid flow sinker or fluid flow sinker assembly according to any one of the preceding items, wherein the fluid flow sinker comprises an average density greater than the density of pure water.
Item 13. The fluid flow sinker or fluid flow sinker assembly according to any one of the preceding items, wherein the fluid flow sinker comprises a polymer.
Item 14. The fluid flow sinker or fluid flow sinker assembly according to any one of the preceding items, wherein the fluid flow sinker comprises a metal.
Item 15. The fluid flow sinker or fluid flow sinker assembly according to any one of the preceding items, wherein the fluid flow sinker has a maximum diameter, DMAX, as measured across the generally cylindrical sidewall, and a maximum length, LMAX, as measured between the first end and the second end, and wherein LMAX/DMAX is no less than 1.25, no less than 1.5, no less than 1.75, no less than 2.0, no less than 2.5, no less than 3.0, no less than 4.0, or no less than 5.0.
Item 16. The fluid flow sinker or fluid flow sinker assembly according to item 13, wherein LMAX/DMAX is no greater than 10.0, no greater than 8.0, or no greater than 6.0.
Item 17. The fluid flow sinker or fluid flow sinker assembly according to any one of the preceding items, wherein, when viewed in cross section, the generally cylindrical wall comprises a cylindrical wall.
Item 18. The fluid flow sinker or fluid flow sinker assembly according to any one of items 15-17, wherein the aperture has an average diameter, DA, and wherein DMAX/DA is at least 1.1, at least 1.2, at least 1.3, at least 1.4, at least 1.5, at least 1.75, or at least 2.0.
Item 19. The fluid flow sinker or fluid flow sinker assembly according to item 18, wherein DMAX/DA is no greater than 4.0, no greater than 3.5, no greater than 3.0, no greater than 2.5, or no greater than 2.25.
Item 20. The fluid flow sinker or fluid flow sinker assembly according to any one of items 18 or 19, wherein the DA is constant, as measured along a length of the aperture.
Item 21. The fluid flow sinker or fluid flow sinker assembly according to any one of items 18 or 19, wherein DA varies along a length of the aperture.
Item 22. The fluid flow sinker or fluid flow sinker assembly according to item 21, wherein the aperture has a maximum diameter, DAMAX, a minimum diameter, DAMIN, and wherein DAMAX is no greater than 1.5 DA, and DAMIN is no less than 0.5 DA.
Item 23. The fluid flow sinker or fluid flow sinker assembly according to item 22, wherein DAMAX is no greater than 1.4 DA, no greater than 1.3 DA, no greater than 1.2 DA, or no greater than 1.1 DA.
Item 24. The fluid flow sinker or fluid flow sinker assembly according to any one of items 22 or 23, wherein DAMIN is no less than 0.6 DA, no less than 0.7 DA, no less than 0.8 DA, or no less than 0.9 DA.
Item 25. The fluid flow sinker or fluid flow sinker assembly according to any one of the preceding items, wherein the aperture has a length, LA, wherein a first portion of the aperture has a diameter, DA1, wherein a second portion of the aperture has a diameter DA2, and wherein DA2 is greater than DA1.
Item 26. The fluid flow sinker or fluid flow sinker assembly according to item 25, wherein DA2 is at least 1.05 DA1, at least 1.1 DA1, or at least 1.2 DA1.
Item 27. The fluid flow sinker or fluid flow sinker assembly according to any one of items 25 or 26, wherein DA2 is no greater than 1.5 DA1, no greater than 1.4 DA1, or no greater than 1.3 DA1.
Item 28. The fluid flow sinker or fluid flow sinker assembly according to any one of items 25-27, wherein the first portion of the aperture is adjacent the first end of the body, and wherein the second portion of the aperture is adjacent the second end of the body.
Item 29. The fluid flow sinker or fluid flow sinker assembly according to any one of the preceding items, wherein the fluid flow sinker comprises a fluid passageway disposed on the first end and extending from the generally cylindrical sidewall to the aperture.
Item 30. The fluid flow sinker or fluid flow sinker assembly according to item 29, wherein the fluid passageway comprises a recess extending from the first end into the body.
Item 31. The fluid flow sinker or fluid flow sinker assembly according to item 30, wherein, when viewed in cross section, the recess has a polygonal profile.
Item 32. The fluid flow sinker or fluid flow sinker assembly according to any one of items 30 or 31, wherein, when viewed in cross section, the recess has a rectangular profile.
Item 33. The fluid flow sinker or fluid flow sinker assembly according to item 30, wherein, when viewed in cross section, the recess has an ellipsoidal profile.
Item 34. The fluid flow sinker or fluid flow sinker assembly according to any one of items 30-33, wherein the recess has a maximum height, HRMAX, as measured from the first end, wherein the body comprises a maximum length, LMAX, and wherein LMAX/HRMAX is at least 2.0, at least 3.0, at least 4.0, at least 5.0, at least 6.0, at least 7.0, at least 8.0, at least 9.0, at least 10.0, at least 15.0, at least 20.0, at least 25.0, at least 30.0, or at least 50.0.
Item 35. The fluid flow sinker or fluid flow sinker assembly according to item 34, wherein LMAX/HRMAX is no greater than 500, no greater than 400, no greater than 300, no greater than 200, no greater than 100, or no greater than 75.
Item 36. The fluid flow sinker or fluid flow sinker assembly according to any one of items 30-35, wherein, when viewed in cross section, the recess has a cross-sectional area greater than 0.1 in2, greater than 0.2 in2, greater than 0.3 in2, greater than 0.4 in2, or greater than 0.5 in2.
Item 37. The fluid flow sinker or fluid flow sinker assembly according to any one of items 30-36, wherein, when viewed in cross section, the recess has a cross-sectional area of less than 2.0 in2, less than 1.0 in2, less than 0.75 in2, or less than 0.6 in2.
Item 38. The fluid flow sinker or fluid flow sinker assembly according to item 29, wherein the fluid passageway comprises a plurality of recesses extending from the first end into the body.
Item 39. The fluid flow sinker or fluid flow sinker assembly according to item 38, wherein, when viewed in cross section, each of the plurality of recesses has a polygonal profile.
Item 40. The fluid flow sinker or fluid flow sinker assembly according to any one of items 38 or 39, wherein, when viewed in cross section, each of the plurality of recesses has a rectangular profile.
Item 41. The fluid flow sinker or fluid flow sinker assembly according to item 38, wherein, when viewed in cross section, each of the plurality of recesses has an ellipsoidal profile.
Item 42. The fluid flow sinker or fluid flow sinker assembly according to any one of items 38-41, wherein, when viewed in cross section, each of the plurality of recesses has a different geometric profile.
Item 43. The fluid flow sinker or fluid flow sinker assembly according to any one of items 38-42, wherein each of the plurality of recesses has a maximum height, HRMAX, as measured from the first end, wherein the body comprises a maximum length, LMAX, and wherein LMAX/HRMAX is at least 2.0, at least 3.0, at least 4.0, at least 5.0, at least 6.0, at least 7.0, at least 8.0, at least 9.0, at least 10.0, at least 15.0, at least 20.0, at least 25.0, at least 30.0, or at least 50.0.
Item 44. The fluid flow sinker or fluid flow sinker assembly according to item 43, wherein LMAX/HRMAX is no greater than 500, no greater than 400, no greater than 300, no greater than 200, no greater than 100, or no greater than 75.
Item 45. The fluid flow sinker or fluid flow sinker assembly according to any one of items 38-44, wherein, when viewed in cross section, each of the plurality of recesses has a cross-sectional area greater than 0.1 in2, greater than 0.2 in2, greater than 0.3 in2, greater than 0.4 in2, or greater than 0.5 in2.
Item 46. The fluid flow sinker or fluid flow sinker assembly according to any one of items 38-45, wherein, when viewed in cross section, each of the plurality of recesses has a cross-sectional area of less than 2.0 in2, less than 1.0 in2, less than 0.75 in2, or less than 0.6 in2.
Item 47. The fluid flow sinker or fluid flow sinker assembly according to any one of items 38-46, wherein, when viewed in cross section, each of the plurality of recesses has a different cross-sectional area.
Item 48. The fluid flow sinker or fluid flow sinker assembly according to any one of items 38-47, wherein each of the plurality of recesses is disposed at a relative angle, A, with respect to the adjacent recess, and wherein A is equal between each adjacent recess.
Item 49. The fluid flow sinker or fluid flow sinker assembly according to any one of items 38-48, wherein each of the plurality of recesses is disposed at a relative angle, A, with respect to the adjacent recess, and wherein A is different between each adjacent recess.
Item 50. The fluid flow sinker or fluid flow sinker assembly according to any one of items 38-49, wherein, when viewed from the first end, the plurality of recesses forms a starburst pattern.
Item 51. The fluid flow sinker or fluid flow sinker assembly according to item 29, wherein the first end comprises a plurality of projections extending therefrom, and wherein the fluid passageway comprises a fluid passage area free of projections, as defined within a total area as measured between the first end, the generally cylindrical sidewall, and a plane formed at a distal surface of the plurality of projections.
Item 52. The fluid flow sinker or fluid flow sinker assembly according to item 51, wherein the fluid passage area has a volumetric area, AFPA, wherein the total area has a volumetric area, AT, and wherein AFPA is no less than 0.05 AT, no less than 0.1 AT, no less than 0.25 AT, no less than 0.5 AT, no less than 0.75 AT, or no less than 0.9 AT.
Item 53. The fluid flow sinker or fluid flow sinker assembly according to item 52, wherein AFPA is less than 1 AT, less than 0.98 AT, less than 0.96 AT, less than 0.94 AT, less than 0.92 AT, or less than 0.90 AT.
Item 54. The fluid flow sinker or fluid flow sinker assembly according to any one of the preceding items, wherein the fluid flow sinker has a fluid removal rate as measured according to the Fluid Removal Test of no less than 95%, such as no less than 98%, no less than 99%, or even no less than 99.5%.
Item 55. The fluid flow sinker or fluid flow sinker assembly according to any one of the preceding items, wherein the fluid flow sinker has a flow effectiveness ratio of no less than 25%, such as no less than 50%, no less than 75%, or even no less than 90%.
Item 56. The fluid flow sinker or fluid flow sinker assembly according to any one of the preceding items, wherein the fluid flow sinker is adapted to remove a fluid from a vessel upon application of a negative pressure in the aperture.
Item 57. The fluid flow sinker or fluid flow sinker assembly according to any one of the preceding items, wherein the second end of the fluid flow sinker is adapted such that the aperture remains in fluid communication with a fluid disposed in a vessel when a surface of the second end is oriented in a direction coplanar with a portion of a sidewall of a vessel.
The above-disclosed subject matter is to be considered illustrative, and not restrictive, and the claims are intended to cover all such modifications, enhancements, and other embodiments, which fall within the true scope of the present invention. Thus, to the maximum extent allowed by law, the scope of the present invention is to be determined by the broadest permissible interpretation of the following claims and their equivalents, and shall not be restricted or limited by the foregoing detailed description.
In addition, in the foregoing detailed description, various features can be grouped together or described in a single embodiment for the purpose of streamlining the disclosure. This disclosure is not to be interpreted as reflecting an intention that the claimed embodiments require more features than are expressly recited in each claim. Rather, as the following claims reflect, inventive subject matter can be directed to less than all features of any of the disclosed embodiments. Thus, the following claims are incorporated into the detailed description, with each claim standing on its own as defining separately claimed subject matter.
This application claims priority under 35 U.S.C. § 119(e) to U.S. Patent Application No. 61/984,150 entitled “FLUID FLOW SINKER,” by Mitchell L. Snyder, et al., filed Apr. 25, 2014, which is assigned to the current assignee hereof and incorporated herein by reference in its entirety.
| Number | Name | Date | Kind |
|---|---|---|---|
| 1581508 | Bomhard | Apr 1926 | A |
| 2344005 | Sundholm | Mar 1944 | A |
| RE26470 | Deuschle et al. | Oct 1968 | E |
| 3541583 | Deuschle | Nov 1970 | A |
| 4245760 | Stevenson | Jan 1981 | A |
| 4273272 | Blanc | Jun 1981 | A |
| 4537334 | Spengler et al. | Aug 1985 | A |
| 4630759 | Dawn | Dec 1986 | A |
| 5114342 | Young et al. | May 1992 | A |
| 5195664 | Rhea | Mar 1993 | A |
| 5215227 | Farner | Jun 1993 | A |
| 5217044 | Schulte | Jun 1993 | A |
| D379854 | Hirsch et al. | Jun 1997 | S |
| 5690487 | Whitehouse et al. | Nov 1997 | A |
| 5743736 | Folko et al. | Apr 1998 | A |
| 5769284 | Vargas | Jun 1998 | A |
| 5839620 | Battegazzore | Nov 1998 | A |
| 5931670 | Davis | Aug 1999 | A |
| 6027041 | Evans | Feb 2000 | A |
| 6156004 | Tremaine et al. | Dec 2000 | A |
| 6183254 | Cohen | Feb 2001 | B1 |
| 6193101 | Murphy et al. | Feb 2001 | B1 |
| 6227412 | Sweeton | May 2001 | B1 |
| 6290265 | Warburton-Pitt et al. | Sep 2001 | B1 |
| 6375092 | Banach | Apr 2002 | B1 |
| 6602072 | Burney | Aug 2003 | B2 |
| 6695179 | Mandile | Feb 2004 | B2 |
| 6779693 | Sweeton | Aug 2004 | B2 |
| 6821118 | Schlussel | Nov 2004 | B2 |
| 6969046 | Streutker et al. | Nov 2005 | B2 |
| 7240810 | Harrity et al. | Jul 2007 | B2 |
| 7335023 | Mahlmann | Feb 2008 | B2 |
| 7377780 | White et al. | May 2008 | B2 |
| 7500584 | Schutz | Mar 2009 | B2 |
| 7648083 | Hornsby et al. | Jan 2010 | B2 |
| 7942873 | Kwan et al. | May 2011 | B2 |
| 8191740 | Hoss et al. | Jun 2012 | B2 |
| D692143 | Shahidi Bonjar | Oct 2013 | S |
| 8545401 | Hajarian et al. | Oct 2013 | B2 |
| 8603049 | Morris et al. | Dec 2013 | B2 |
| 8870568 | Ream | Oct 2014 | B1 |
| 9138109 | Leon | Sep 2015 | B1 |
| D741495 | Snyder et al. | Oct 2015 | S |
| D749749 | Snyder et al. | Feb 2016 | S |
| 9248463 | Anzalone et al. | Feb 2016 | B2 |
| 20030134254 | Filho | Jul 2003 | A1 |
| 20030218030 | Torres et al. | Nov 2003 | A1 |
| 20060088800 | Neff et al. | Apr 2006 | A1 |
| 20060259014 | Yarger | Nov 2006 | A1 |
| 20080145815 | Hershey et al. | Jun 2008 | A1 |
| 20120001112 | Alkemade et al. | Jan 2012 | A1 |
| 20140072744 | Sitcoske | Mar 2014 | A1 |
| 20150306619 | Snyder et al. | Oct 2015 | A1 |
| Number | Date | Country |
|---|---|---|
| 1477194 | Nov 2004 | EP |
| 1253863 | Sep 2007 | EP |
| H08299863 | Nov 1996 | JP |
| H11180481 | Jul 1999 | JP |
| 2002019862 | Jan 2002 | JP |
| 2005145457 | Jun 2005 | JP |
| 2009066501 | Apr 2009 | JP |
| 2013063457 | May 2013 | WO |
| 2015164729 | Oct 2015 | WO |
| Entry |
|---|
| International Search Report from PCT/US2015/027499 dated Aug. 7, 2015, 1 pg. |
| Supplementary European Search Report for EP15782262 dated Dec. 22, 2017, 9 pages. |
| Number | Date | Country | |
|---|---|---|---|
| 20150306619 A1 | Oct 2015 | US |
| Number | Date | Country | |
|---|---|---|---|
| 61984150 | Apr 2014 | US |
