WO2010148477A1 - Vaned filtering element - Google Patents
Vaned filtering element Download PDFInfo
- Publication number
- WO2010148477A1 WO2010148477A1 PCT/CA2010/000250 CA2010000250W WO2010148477A1 WO 2010148477 A1 WO2010148477 A1 WO 2010148477A1 CA 2010000250 W CA2010000250 W CA 2010000250W WO 2010148477 A1 WO2010148477 A1 WO 2010148477A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- fluid
- vaned
- fluid permeable
- permeable screens
- fin
- Prior art date
Links
- 238000001914 filtration Methods 0.000 title claims abstract description 51
- 239000012530 fluid Substances 0.000 claims description 63
- 239000002184 metal Substances 0.000 claims description 38
- 238000004891 communication Methods 0.000 claims description 10
- 239000011148 porous material Substances 0.000 claims description 6
- 125000006850 spacer group Chemical group 0.000 claims 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 16
- 238000001816 cooling Methods 0.000 abstract description 5
- 239000002826 coolant Substances 0.000 abstract description 2
- 238000009434 installation Methods 0.000 abstract description 2
- 239000000498 cooling water Substances 0.000 abstract 1
- 238000013461 design Methods 0.000 description 9
- 230000000694 effects Effects 0.000 description 9
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 230000037406 food intake Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003758 nuclear fuel Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D35/00—Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
- B01D35/28—Strainers not provided for elsewhere
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/01—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
- B01D29/05—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements supported
- B01D29/07—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements supported with corrugated, folded or wound filtering sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/39—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with hollow discs side by side on, or around, one or more tubes, e.g. of the leaf type
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/50—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition
- B01D29/52—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition in parallel connection
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D35/00—Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
- B01D35/02—Filters adapted for location in special places, e.g. pipe-lines, pumps, stop-cocks
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21C—NUCLEAR REACTORS
- G21C13/00—Pressure vessels; Containment vessels; Containment in general
- G21C13/02—Details
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21C—NUCLEAR REACTORS
- G21C19/00—Arrangements for treating, for handling, or for facilitating the handling of, fuel or other materials which are used within the reactor, e.g. within its pressure vessel
- G21C19/28—Arrangements for introducing fluent material into the reactor core; Arrangements for removing fluent material from the reactor core
- G21C19/30—Arrangements for introducing fluent material into the reactor core; Arrangements for removing fluent material from the reactor core with continuous purification of circulating fluent material, e.g. by extraction of fission products deterioration or corrosion products, impurities, e.g. by cold traps
- G21C19/307—Arrangements for introducing fluent material into the reactor core; Arrangements for removing fluent material from the reactor core with continuous purification of circulating fluent material, e.g. by extraction of fission products deterioration or corrosion products, impurities, e.g. by cold traps specially adapted for liquids
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21D—NUCLEAR POWER PLANT
- G21D1/00—Details of nuclear power plant
- G21D1/04—Pumping arrangements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2201/00—Details relating to filtering apparatus
- B01D2201/12—Pleated filters
- B01D2201/127—Pleated filters with means for keeping the spacing between the pleats
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E30/00—Energy generation of nuclear origin
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E30/00—Energy generation of nuclear origin
- Y02E30/30—Nuclear fission reactors
Definitions
- the present invention pertains generally to the field of fluid recirculation systems incorporating suction strainers More particularly, the present application pertains to strainers used to remove debris from water bemg sucked into a piping system, such as m nuclear power plants.
- a critical function of Emergency Core Cooling Systems (ECCS) and other recirculation systems of nuclear power plants is to move fluids quickly and in large volumes to critical areas of the nuclear power plant in the event of accidents and emergencies. Integral to this critical function is the ability of strainers, filters, screens and other such devices associated with the systems to remove solids from the moving fluids while at the same time maintaining a sufficiently large volume of fluid flow.
- ECCS Emergency Core Cooling Systems
- Nuclear plants have various safety systems to ensure that the nuclear fuel in the reactor core remains cooled in all credible accident scenarios.
- One such scenario is a "loss of coolant accident,” (LOCA) in which an external pipe is postulated to break, allowing a large amount of water to escape from the reactor cooling system
- LOCA loss of coolant accident
- This watei may dislodge solid debris from neighbouring pipes or other ieactoi structures
- the watei, along with some of the dislodged debris will flow to the lowest parts of the reactor building into a sump Plants aie equipped with safety systems that pump water from the sump back into various reactor cooling systems. Strainers on the pump intakes ensure that any debris large enough to clog equipment in these systems is prevented from entering
- the first layer to deposit on the strainer may form a mat of fibers and collect finer particles, which would otherwise pass through the strainer, resulting m a thin layer of low porosity deb ⁇ s with high hydraulic resistance.
- This behaviour is referred to as the "thm-bed effect" where the head loss per unit thickness of debris is relatively high as compared to that of full (or thick-bed) debris formation where relatively high porosity debris allows the passage of flow with lower head losses.
- Thm-bed debris can cause head losses high enough to threaten the functionality of emergency core cooling system (ECCS) sump recirculation pumps.
- ECCS emergency core cooling system
- Thin-bed debris has occurred operationally at nuclear power plants and has been created during head-loss testing.
- One way of alleviating the thin- bend effect is to increase the surface area of ECCS strainers.
- Strainers must have enough screen area that the debris layer on the strainer is not too thick to cause unacceptably high restriction to flow. Strainers must also be as small as possible to fit into the available space. Therefore compactness, i.e., accommodating the most screen area in the smallest volume, is important.
- Finned Strainer® which is described in International PCT publication number WO 06/50606.
- the Firmed Strainer performs the filtering function through modular hollow fins attached to a header that directs the filtered water to pump intake.
- the Finned Strainer includes two different fin designs (1) Flat-Surface Fins and (2)
- An object of the present invention is to provide a vaned filtering element.
- the present invention is an improvement to the Flat-Surface Fin design with the addition of vanes that result in a more compact design.
- the large increase in filtration surface area over a Flat- Surface fin is a significant advantage to reduce the thin-bed effect.
- the increased area reduces the restriction to flow entering the strainer by decreasing the water velocity through the screen and reducing the thickness of debris (because it is spread over a larger area). The resistance of this thin layer to flow entering the strainer is reduced with the larger screen area achieved by the vanes.
- a vaned filter element comprising one or more fluid permeable screens formed from at least one layer of porous material that is folded into a plurality of hollow vanes extending outwardly from the outer surface of the each of the one or more fluid permeable screens.
- a filtering element comprising: a perimeter frame having one or more openings along one side edge of said frame, a pair of fluid permeable screens fixed to the perimeter frame in opposed spaced relation to one another, and at least one fluid flow channel is formed between the fluid permeable screens for fluid communication with a header or tube via the one or more openings in the side edge of said frame, wherein each of said fluid permeable screens is formed from one or more perforated metal sheet, metal mesh or a combination thereof, and includes folds to form a plurality of outwardly extending hollow vanes.
- a strainer for filtering debris from a fluid comprising: (a) a header defining an enclosed volume and having an outlet in fluid communication with a suction source, said header having a plurality of inlet aperture slots formed therein, and (b) fin-like filter elements projecting outwardly from each aperture slot for filtering debris from said fluid, each said filter element comprising a perimeter frame and a pair of fluid permeable screens fixed thereto in opposed spaced relation, and at least one fluid flow channel therebetween in fluid communication with said enclosed volume through a marginal side edge of said frame and said aperture slot, wherein each of said fluid permeable screens is formed from one or more perforated metal sheet, metal mesh or a combination thereof, and includes folds to form a plurality of outwardly extending hollow vanes.
- Figure 1 depicts a vaned filter element (fin), according to one embodiment of the present invention, connected to a header (Isometric).
- Figure 2 depicts a modular use of a vaned filter element (fin) in a strainer assembly, according to one embodiment of the present invention.
- Figure 3 depicts a vaned fin according to one embodiment of the present invention, in which the fluid permeable screens are formed with perforated metal vanes.
- the vaned fin is depicted with the outer frame (a), and without the outer frame (b).
- Figure 4 is a photograph of a vaned fin according to one embodiment of the present invention, in which the fluid permeable screens are formed with perforated metal vanes.
- Figure 5 is an exploded view of the vaned fin shown in Figure 3.
- Figure 6 is a detail view of hollow vanes of the vaned fin shown in Figure 3.
- Figure 7 depicts a vaned fin according to one embodiment of the present invention, in which the fluid permeable screens are formed with layered metal mesh vanes.
- the vaned fin is depicted with the outer frame (a), and without the outer frame (b).
- Figure 8 is a photograph of a vaned fin according to one embodiment of the present invention, in which the fluid permeable screens are formed with layered metal mesh vanes.
- Figure 9 is an exploded view of the vaned fin shown in Figure 7.
- Figure 10 is a detail view of hollow vanes of the vaned fin shown in Figure 7.
- Figure 11 depicts a cylindrical vaned fin according to one embodiment of the present invention.
- Figure 12 depicts a vaned internal-fin filter element according to one embodiment of the present invention.
- Figure 13 depicts a planar vaned filter element according to one embodiment of the present invention.
- the present invention provides a vancd filter element comprising one or more fluid permeable screens formed from at least one layer of porous material that is folded into a plurality of hollow vanes extending outwardly from the outer surface of the each of the one or more fluid permeable screens.
- the vaned filtering element of the present invention is designed to reduce the space required for strainer installation by increasing strainer surface area per unit volume, while maximizing the quantity of debris that can be filtered from the water.
- the vaned filter element comprises two layers of porous material that are in the form of two fluid permeable screens in opposed spaced relation to one another.
- This vaned filter element has at least one fluid flow channel formed between the two fluid permeable screens.
- the vaned filter element is referred to as a "fin".
- the incorporation of the outwardly extending vanes in the fluid permeable screens of fins increases the filtering surface area of the fins in comparison to a similarly dimensioned Flat- Surface or Corrugated Surface fin and permits the use of small filter holes while minimizing the thin bed effect.
- the vaned filter element is configured as a cylinder having outwardly projecting vanes formed (see, for example, Figure 11).
- the vaned filter element is configured such that the vanes are inwardly projecting; this configuration is referred to as a vaned internal-fin filter element (see, for example, Figure 12).
- the vaned filter element is planar, such that the vanes extend outwardly from one side of the filter element (see, for example, Figure 13). The selection of the appropriate filter element will depend on the ultimate application.
- the present invention further provides a strainer system that includes one or more vaned filter elements.
- vaned filter elements that are configured as fins. However, it is understood that this description is not intended to limit the invention to vaned filter elements having a fin configuration.
- Figure 1 depicts a vaned filter element as a component of a strainer system according to one embodiment of the present invention.
- the strainer system depicted in Figure 1 includes four major components: one or more connection(s) 1 to the pump intake pipe 2; a duct, termed header 3, that collects incoming fluid and directs it to the pump intake, which may be in the floor or on a wall; and vaned filter element 4 with porous and hollow vanes 5.
- header 3 includes a plurality of slots 6 to accommodate multiple vaned filtering elements, or fins, and to allow the passage of fluid from each of the fins to the header.
- the vaned filter element, or fin, of the present invention can be designed as a modular attachment to larger structures that are connected to the pump intake, such as ducts and headers. As an alternate arrangement, the vaned filter element can be installed directly to an existing sump where the pump intake 2 is connected. Depending on the amount of debris, composition of debris, flow rate and pump suction head availability, additional fins are added in a modular manner to form a strainer system.
- the vaned filter element design incorporates spatial flexibility by customizing dimensions A, B and C of each fin as shown in Figure 1. This flexibility ensures that the available space, for example, in existing nuclear reactors, is used optimally and the strainer system can be built around existing structures.
- FIG. 2 depicts only part of a strainer assembly that includes multiple headers 3 that are connected to corresponding connections 1 to corresponding pump intake pipes 2. Each header 3 collects incoming fluid and directs it to the corresponding pump intake pipe 2. Further, as depicted in Figure 2, each header 3 includes a plurality of vaned filtering elements 4.
- Fins can be mounted on one side (as shown in Figure 1), two sides (as shown in Figure 1), two sides (as shown in Figure 1), two sides (as shown in Figure 1), two sides (as shown in Figure 1), two sides (as shown in Figure 1), two sides (as shown in Figure 1), two sides (as shown in Figure 1), two sides (as shown in Figure 1), two sides (as shown in Figure 1), two sides (as shown in Figure 1), two sides (as shown in Figure 1), two sides (as shown in Figure 1)
- FIG 2 top, bottom, or a combination of sides, top and/or bottom of the header.
- Fins can have differing dimensions, and uniform or variable spacing, depending on the particular spatial and filtering requirements of the application.
- the vaned filter element, or fin, of the present invention is a variation of the Flat Surface Fin of the Finned Strainer technology described in International PCT publication number WO 06/50606. Two configurations of the vaned filter element of the present invention are detailed in the next sections.
- Figure 3 (a) and (b) depicts a vaned filtering element, or fin, 4 according to one embodiment of the present invention, in which the vaned fin 4 is easily installed or removed using one or more connection means, such as a pin and a bolt inserted in opening 10.
- connection means such as a pin and a bolt inserted in opening 10.
- the vaned filtering element of the present invention can be permanently attached to a header so as to form a permanent component of a strainer system (not shown).
- KECTIFIED SHEET (RULE 91 .1) As shown in Figure 3(a), water enters the fin 4 (shown as inflow 19) through a porous filtration screen, leaving debris on the screen, and exits fin 4 through side opening 18 (shown as outflow 20). hi Figure 3(b) the structure of the porous filtration surface of fin 4 is shown to include a filtration surface formed in the shape of vanes 5, to increase the surface area. Two types of vanes can be used based on the design requirements:
- the vanes of the porous filtration screen are formed from a single perforated sheet metal ( Figure 5 and Figure 6).
- Figure 3(b) depicts the interior of a vaned fin 4, without an outer frame.
- vaned fin 4 will include outer frame 7 in order to provide mechanical stability and to define part of the at least one fluid flow channel within the vaned fin 4.
- the frame itself can include perforations or be formed from a rigid porous material to provide additional filtering.
- the frame can be made from a rigid material that is impermeable to fluid.
- the frame includes an elongated opening 18, or a series of smaller openings (not shown) along one side, which corresponds with a slot or opening in the header to which it is, or is to be, attached. It is through this opening that fluid flows from the main flow channel 13 within vaned fin 4, into the header.
- Figure 4 is a photograph of a vaned fin as depicted in Figure 3 (a), and which includes perforated metal vanes.
- the outer frame of the vaned fin can include an end cap 17 at the header end of vaned fin 4.
- End cap 17 is formed from a plate that is welded over one end of corrugated plate 15.
- End cap 17 includes a large opening 18 through which flow exits fin 4 and enters the header. End cap is also attached to C-shaped mounting frame
- Figure 5 shows an exploded view of vaned filter element 4 according to one embodiment of the present invention, which includes fluid permeable screens made from vaned perforated metal, hi this configuration the porous vaned surfaces are formed from a single perforated metal plate.
- the perforated metal plate vane surface is simple to manufacture and adds significantly to the strength of the fin.
- the two vaned surfaces 14 on each side of the fin are separated by a corrugated plate 15 that provides stiffness and strength, and forms flow channels for fluid communication with the collection header.
- Edges of the vaned fin are covered by a mounting frame 16 around all sides except the edge that fits into the header. This edge includes one or more openings to facilitate fluid communication between the flow channels and the interior of the header. This frame also adds to the structural strength of the fin.
- the mounting frame 16 can be fully or partially perforated if extra screen area is needed.
- FIG. 7(a) water enters the fin 4 (shown as inflow 19) through a porous filtration screen, leaving debris on the screen, and exits fin 4 through side opening 18 (shown as outflow 20).
- Li Figure 7(b) the structure of the porous filtration surface of fin 4 is shown to include a filtration surface formed in the shape of vanes 5, to increase the surface area.
- the vaned surfaces are formed from a layered metal mesh. The two vaned surfaces are attached to the flat perforated plate 23.
- FIG. 7(b) depicts the interior of a vaned fin 4, without an outer frame.
- vaned fin 4 will include outer frame 7 in order to provide mechanical stability and to define part of the at least one fluid flow channel within the vaned fin 4.
- the frame itself can include perforations or be formed from a rigid porous material to provide additional filtering.
- the frame can be made from a rigid material that is impermeable to fluid.
- the frame includes an elongated opening 18, or a series of smaller openings (not shown) along one side, which corresponds with a slot or opening in the header to which it is, or is to be, attached. It is through this opening that fluid flows (identified as outflow 20) from the main flow channel 13 within vaned fin 4, into the header.
- Figure 8 is a photograph of a vaned fin as depicted in Figure 7(a), and which includes layered metal mesh vanes.
- Figure 9 shows an exploded view of the vaned filter element according to one embodiment of the present invention, which incorporates layered metal mesh. Using this configuration, filtration of debris smaller than 200 ⁇ m is possible. After the initial accumulation of a thin fibre mat, much smaller size debris (nominal size of 10 ⁇ m) are filtered. The mesh size can be changed depending on the requirements of the specific application.
- the two vaned surfaces on each side of the fin are composed of two layers of woven metal mesh surfaces 24 and 25 as shown in Figure 9.
- the outer mesh surface 25 provides the fine-particle filtering capability. This mesh is very flexible on its own and requires structural enhancement for consistent vane forming.
- the inner mesh surface 24 is selected to increase the stiffness and strength of the layered surface.
- the combined fine-mesh surface 25 and the course-mesh surface 24 provide fine filtering capability with sufficient structural strength.
- the two mesh layers are attached prior to forming the vanes at multiple locations such that they behave as one surface.
- This layered mesh surface is used to manufacture the two faces of the fin with formed hollow vanes. The details of the vanes are shown in Figure 10.
- the two vaned surfaces are attached to the flat perforated plate 23.
- the combined vaned face is structurally strong.
- the corrugated plate 15 adds significant additional stiffness and strength, and forms flow channels for fluid communication with the collection header. Edges of the vaned fin are covered by a mounting frame 16 around all sides except the edge that fits into the header. This edge includes one or more openings to facilitate fluid communication
- KECTIFIED SHEET (RULE 91 .1) between the flow channels and the interior of the header. This frame also adds to the structural strength of the fin.
- the mounting frame 16 can be fully or partially perforated if extra screen area is needed.
- FIG. 10 The details of the layered metal mesh vane is shown in Figure 10. As illustrated in this figure, after entering the vanes, water flows through the hollow core 12 of the vanes towards the main flow channel 13 of the fin. With the optimal use of vane spacing, the thin- bed effect is minimized.
- the standard vane dimensions are selected based on the typical debris composition expected in nuclear power plants following a LOCA.
- the spacing between vanes is determined with the consideration of maximizing the filtering surface area without any loss of filtering capability. If the vane spacing is too large, the surface area of the fin will be non- optimal, resulting in a non-compact strainer design. If the vane spacing if too small, deposited debris on the vane surfaces will bridge across the vanes resulting in a reduction in the effective filtering area and, hence, a reduction in filtering efficiency. For this reason, the proper selection of vane spacing is important for optimal design.
- the typical thin bed debris thickness is about 3 mm.
- a vane pitch of approximately 14 mm with 10 mm space between two adjacent vanes could be appropriate in order to allow the formation of the thin bed without bridging between vanes.
- vane height is also determined by consideration of maximizing filtering surface area while maintaining filtering efficiency.
- the fin surface area can be increased indefinitely by increasing filtration area, there is a limit beyond which additional vane height will not provide any benefit for debris filtration.
- the increased vane height provides no further improvement in filtering capability. This is because the thick-bed debris fills the space between vanes and the thick-bed head loss becomes a function of the projected area (e.g., fin surface area without the vanes) that is independent of the vane height.
- the standard vane height used for nuclear ECCS strainer applications is roughly 25 mm, but this dimension has
- KECTIFIED SHEET (RULE 91 .1) to be optimized with lab testing to include the effects of debris composition and debris quantity per unit area.
- the present Vaned Fin invention Compared to the Flat-Surface Fin and Corrugated Surface Fin of the Finned Strainer technology, the present Vaned Fin invention provides about 4.5 and 2.5 times the surface area per unit volume, respectively. The significant increase in the surface area minimizes the "thin-bed effect" by distributing the thin bed debris deposition over a larger surface area.
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- Physics & Mathematics (AREA)
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Plasma & Fusion (AREA)
- General Engineering & Computer Science (AREA)
- High Energy & Nuclear Physics (AREA)
- Filtering Materials (AREA)
- Structure Of Emergency Protection For Nuclear Reactors (AREA)
Abstract
Description
Claims
Priority Applications (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA2766105A CA2766105C (en) | 2009-06-23 | 2010-02-26 | Vaned filtering element |
EP10791085.3A EP2445606B1 (en) | 2009-06-23 | 2010-02-26 | Vaned filtering element |
US13/379,915 US9770680B2 (en) | 2009-06-23 | 2010-02-26 | Vaned filtering element |
CN201080034643.8A CN102802758B (en) | 2009-06-23 | 2010-02-26 | Tab style filter element |
KR1020177026684A KR101910001B1 (en) | 2009-06-23 | 2010-02-26 | Vaned filtering element |
JOP/2010/0177A JO3307B1 (en) | 2009-06-23 | 2010-05-27 | Vaned filtering element |
TW099117620A TWI587905B (en) | 2009-06-23 | 2010-06-01 | Vaned filtering element |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US21965909P | 2009-06-23 | 2009-06-23 | |
US61/219,659 | 2009-06-23 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2010148477A1 true WO2010148477A1 (en) | 2010-12-29 |
Family
ID=43385817
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/CA2010/000250 WO2010148477A1 (en) | 2009-06-23 | 2010-02-26 | Vaned filtering element |
Country Status (8)
Country | Link |
---|---|
US (1) | US9770680B2 (en) |
EP (1) | EP2445606B1 (en) |
KR (2) | KR20120107453A (en) |
CN (1) | CN102802758B (en) |
AR (1) | AR078217A1 (en) |
CA (1) | CA2766105C (en) |
JO (1) | JO3307B1 (en) |
WO (1) | WO2010148477A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012177692A (en) * | 2011-02-14 | 2012-09-13 | Global Nuclear Fuel Americas Llc | Debris exclusion and retention device for fuel assembly |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
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US9672947B2 (en) | 2004-11-15 | 2017-06-06 | Atomic Energy Of Canada Limited | Finned strainer |
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- 2010-02-26 KR KR1020127001791A patent/KR20120107453A/en active Application Filing
- 2010-02-26 US US13/379,915 patent/US9770680B2/en active Active
- 2010-02-26 CN CN201080034643.8A patent/CN102802758B/en active Active
- 2010-02-26 KR KR1020177026684A patent/KR101910001B1/en active IP Right Grant
- 2010-02-26 WO PCT/CA2010/000250 patent/WO2010148477A1/en active Application Filing
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Also Published As
Publication number | Publication date |
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KR101910001B1 (en) | 2018-10-22 |
CA2766105C (en) | 2019-04-02 |
CN102802758B (en) | 2018-02-16 |
EP2445606B1 (en) | 2016-08-31 |
EP2445606A4 (en) | 2014-01-22 |
EP2445606A1 (en) | 2012-05-02 |
US9770680B2 (en) | 2017-09-26 |
CN102802758A (en) | 2012-11-28 |
KR20120107453A (en) | 2012-10-02 |
US20120273407A1 (en) | 2012-11-01 |
JO3307B1 (en) | 2018-09-16 |
AR078217A1 (en) | 2011-10-26 |
KR20170113680A (en) | 2017-10-12 |
CA2766105A1 (en) | 2010-12-29 |
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