FLUID FLOW CONDITIONER

Abstract: A fluid flow conditioning plate (10) for removing swirl, etc. from an enclosed water stream especially for a fire fighting nozzle. The plate has circular holes lying on concentric circles (11, 12, 13). Two cross-sectional shapes for the holes are suggested. They may have a short upstream end tapering inwardly in the direction of the flow then a substantially longer portion of constant cross section and finally a short downstream end tapering outwardly in the direction of the flow. In the alternative the portion of constant cross section is shortened to accommodate a longer downstream end portion, of conical or trumpet shape, which acts as a diffuser. Various examples of ratios of hole to plate diameters, etc. are given as are examples of fog nozzles incorporating flow conditioners.

Description: FLUID FLOW CONDITIONER FIELD OF THE INVENTION This invention relates to flow conditioners for fluid nozzles or for fluid measurement. For the sake of convenience, the invention will be described in relation to flow conditioners for jet type fire fighting water nozzles but it is to be understood that the invention is not limited thereto as it may be applied to other areas of fluid flow such as fluid jets for fountains or fluid measurement. BACKGROUND ART Prior art flow conditioners include the vane type and the tube bundle type both of which are located in the flui stream. A common use of such flow conditioners is to condition the water stream for jet type fire fighting streams. Although these prior art conditioners are very effective at removing swirl from the water, they are less successful in conditioning other fluid flow properties. Another kind of prior art flow conditioner is the single plate conditioner which consists of a circular plat having an array of 36 fluid passageways therethrough. Eac passageway is tapered inwardly in the direction of the fluid flow and around the downstream end of each passagewa is a tube which is typically 0.13 times the diameter of th plate. The thickness of the plate plus the tubes is also typically 0.13 times the diameter of the plate. SUMMARY OF THE INVENTION It is an object of the invention to provide improved plate type flow conditioners which are simpler to manufacture than prior art plate type flow conditioners and which provide better performance than those prior art flow conditioners. It is a further object of the invention to provide a modified single plate flow conditioner for use in an adjustable spray pattern nozzles such as fog nozzles of the kind used in fire fighting. According to one aspect of the invention there is provided a fluid flow conditioner comprising a plate having a plurality of fluid passageways therethrough, each fluid passageway having an upstream end that is tapered inwardly in the direction of fluid flow and a downstream end that is tapered outwardly in the direction of fluid flow. According to another aspect of the invention there is provided a fluid flow apparatus comprising a nozzle having a nozzle piece, a pipe or body portion and a coupling flange and a fluid flow conditioner according to the invention. BRIEF DESCRIPTION OF THE DRAWINGS In order that the invention may be more readily understood and put into practical effect, reference will now be made to the accompanying drawings in which:- Fig. 1 is a front elevational view of a plate-type flow conditioner according to one embodiment of the invention, Fig. 2 is a side elevational view of the flow conditioner shown in Fig. 1, Fig. 3 is a front elevational view of a plate-typ flow conditioner according to a second embodiment of the invention, Fig. 4 is a front elevational view of a plate-typ flow conditioner according to a third embodiment of the invention, Fig. 5 is an enlarged cross-sectional view of one kind of flow passageway of the plates show in Figs. 1 to 4, Fig. 6 is an enlarged cross-sectional view of a second kind of flow passageways for the plates shown in Figs. 1 to 4, Fig. 7 is a cross-sectional view of a jet-type water nozzle incorporating a plate-type flow conditioner according to the inventio in the body of the nozzle, Fig. 8 is a cross-sectional view of a jet type water nozzle incorporating a plate type flow conditioner according to the inventio with the conditioner located in the coupling of the nozzle, Fig. 9 is a cross-sectional view of a fog type water nozzle incorporating a plate type flow conditioner according to the invention, Fig. 10 is a plan view of the plate type flow conditioner of the fog type nozzle shown i Fig. 9, Fig. 11 is a front elevational view of a plate-type flow conditioner according to a fourth embodiment of the invention, Fig. 12 is a side elevational view of the flow conditioner shown in Fig. 11, and Fig. 13 is a cross-sectional view of a nozzle having co-axial proportioners incorporating a flow conditioner of the kind shown in Figs. 11 and 12. DESCRIPTION OF THE PREFERRED EMBODIMENT The single plate-type flow conditioner shown in Figs. 1 and 2 consists of a plate 10 that has a diameter D. There is a central fluid passageway 11, an inner array of six fluid passageways 12 and an outer array of twelve fluid passageways 13. The fluid passageway arrays 12 and 13 are located on circles which are concentric with the centre of the central fluid passageway 11. As shown in Fig. 2, each fluid passageway has a diameter d. The flow conditioner 16 shown in Fig. 3 is similar to that shown in Fig. 1 and 2 except that there is a further outer array of 18 fluid passageways 14 located on a circle which is also concentric with the centre of the passageway 11. The flow conditioner 17 shown in Fig. 4 is similar to that shown in Fig. 1 and 2 except that there is a further outer array of 24 fluid passageways 15 located on a circle which is also concentric with the centre of the passageway 11. The fluid passageways are spaced evenly over the area of the plate so as to allow for easy manufacture. The number of holes per circle is only approximate and it appears not to be very important that a number of holes be left out in the outer circles thereby making manufacture slightly easier. The diameter d of the fluid passageways depend on the number of passageways used in the flow conditioner. For the 19 passageway flow conditioner 10 shown in Figs. 1 and 2, the passageway size should be in the range of 0.1 to 0.18 times the diameter of the plate D. For the 37 passageway conditioner 16 shown in Fig. 3, the passageway size should be in the range 0.08 to 0.13 times the diamete of the plate D. For the 61 passageway conditioner 17 show in Fig. 4, the passageway size should be in the range of 0.05 to 0.1 times the diameter of the plate D. It is not essential that all the passageways be of the same size but manufacture is simpler if all the passageways are of the same size. The thickness of the plate 10 will depend upon the diameter d of the passageways. The thickness of the plate 10 must be a minimum of 0.6 times the diameter d of the passageways with the ultimate being between 1.0 and 1.7 times the diameter d of the passageways. Structural considerations will influence the choice of plate thickness. The performance of a water jet nozzle depends on the number of fluid passageways. As the number of passageways increases, the quality of the water jet increases. The minimum requirement is 19 passageways to produce a water jet that is visibly superior to the vane or tube bundle type flow conditioners of the prior art. Increasing the number of holes beyond 19 to 37 and 61 has less effect on the quality of the water jet, however, the spacing between the flow conditioner must be reduced for optimum performance. The shortening of the nozzle/flow conditioner assembly is one of the principle advantages of the invention. The geometry of alternative fluid passageways is shown in Figs. 5 and 6. As can be seen in Fig. 5, the upstream end 20 of the fluid passageway 11 is tapered inwardly in the direction of fluid flow and the downstream end 21 of the passageway 11 is tapered outwardly in the direction of fluid flow. The central portion 22 of the passageway 11 is of constant cross-section and is substantially longer than either of the upstream end 20 or the downstream end 21. The upstream end 30 of the passageway 11 shown in Fig. 6 tapers inwardly in the direction of fluid flow. Adjacent to the inlet end 30 there is a smaller mid portion of the passageway 31 of constant cross-section and to the right of the mid portion 31 there is an outwardly tapering diffusion portion 32. The diffuser portion 32 is substantially longer than either the upstream portion 30 or the mid portion 31. In this instance, the diffuser portion is at least 0.3 times the thickness of the plate 10 and the mid portion 31 is from 0.2 to 0.5 times the diameter d of the passageway. In this instance, each upstream end 20 and downstream end 21 is 0.1 times the diameter d of the passageway. The geometry of the passageways has significant advantages including improved performance. For large diameter flow conditioners (100 mm and above), all passageways can be cast into the plate and the diffuser side of the passageway of the Fig. 6 embodiment requires n machining. For small diameter flow conditioners, the plat can be moulded or cast in a convenient plastics materia . The included angle for the diffuser portion 32 of the Fig. 6 embodiment should be in the range of 0 to 15 degrees wit 6 to 10 degrees being preferred. The diffuser could be trumpet shaped instead of conical. Figs. 7 and 8 show a fire fighting nozzle having a flo conditioner 10 of the invention positioned within a nozzle 40 having a nozzle piece 41, a pipe or body portion 42 and a coupling flange 43. With the 19-hole flow conditioner 10 of Figs. 1 and 2, the spacing S between the flow conditioner 10 and the nozzle piece 41 must be a minimum of seven pipe diameters. For the 37-passageway conditioner shown in Fig. 3, the spacing S must be between 4 and 7 pipe diameters. The use of shorter or longer spacing with the 37-passageway conditioner of Fig. 3 causes loss of performance. The flow conditioner 10 may be incorporated into other fire fighting nozzles such as an adjustable spray pattern nozzle or a fog nozzle 50 as shown in Fig. 9. The fog nozzle 50 has a coupling flange 51, a pipe or body portion 52, an adjustable nozzle piece 53 and a stem 54. In this instance, the flow conditioner 10 is used as a retaining plate for the stem 54 which has a threaded end which engages in a correspondingly threaded wall of the central passageway 11. A flow conditioner of the invention may be incorporated into many variations of the fog nozzle including those fitted with co-axial type proportioners. A flow conditioner used in this manner must have a minimum of six holes with the preferred number being 36. The use of six holes produces little or no improvement in performance unless the water entering the nozzle is very turbulent. A flow conditioner 60 suitable for use with a nozzle having co-axial proportioners is shown in Figs. 11 and 12. The flow conditioner 60 has a central bore 63 and two concentric arrays 61 and 62 of passageways. The inner array 61 has 18 passageways and the outer array 62 has 24 or 25 passageways. In this instance, the plate 60 is 18 mm thick and has a diameter of 152 mm and each passageway has a diameter of 16 mm and each upstream end and downstream end is 2 mm long. The co-axial type nozzle 70 shown in Fig. 13 incorporates a flow conditioner 60 of Figs. 11 and 12. The nozzle 70 includes a proportioner element 71, a coupling 72, a nozzle body 73, and a shaper 74. Within the shaper 74 there is a stem 75 having a steamhead 76 and stemplate 77. The conditioner 60 is located within nozzle body 73. Various modifications may be made in details of design and construction of the flow conditioner without departing from the scope and ambit of the invention.

Claims: CLAIMS 1. A fluid flow conditioner comprising a plate having a plurality of fluid passageways therethrough, each fluid passageway having an upstream end that is tapered inwardly in the direction of fluid flow and a downstream end that is tapered outwardly in the direction of fluid flow. 2. A fluid flow conditioner according to claim 1 wherein each fluid passageway has a portion of constant cross- section between the upstream end and the downstream end. 3. A fluid flow conditioner according to claim 2 wherein the constant cross-section portion is substantially longer than the tapered upstream end or the tapered downstream end. 4. A fluid flow conditioner according to claim 2 wherein the tapered downstream end is substantially longer than the tapered upstream end or the portion of constant cross- section. 5. A fluid flow conditioner according to claim 4 wherein the tapered downstream end is a diffuser. 6. A fluid flow conditioner according to claim 5 wherein the diffuser is of conical shape. 7. A fluid flow conditioner according to claim 6 wherein the included angle of the conical shaped diffuser is in the range of 0 to 15 degrees. 8. A fluid flow conditioner according to claim 6 wherein the included angle of the conical shaped diffuser is in the range of 6 to 10 degrees. 9. A fluid flow conditioner according to claim 6 wherein the diffuser is trumpet shaped. 10. A fluid flow conditioner according to any one of the preceding claims having a central fluid passageway, an inner array of six fluid passageways and an outer array of 12 fluid passageways, the inner and outer arrays being located on circles which are concentric with the centre of the central passageway. 11. A fluid flow conditioner according to claim 10 and further including another array of passageways located on a circle which is concentric with the centre of the passageways and which is located radially outwardly from the outer array. 12. A fluid flow conditioner according to claim 11 and further including another array of passageways located on a circle which is concentric with the centre of the passageways and which is located radially outwardly from the outer array. 13. A fluid flow conditioner according to any one of claims 1 to 9 having a central bore and inner and outer concentric arrays of passageways. 14. A fluid flow conditioner according to any one of claims 1 to 13 wherein the diameter of each fluid passageway is in the range of 0.1 to 0.18 times the diameter of the plate. 15. A fluid flow conditioner according to any one of claims 1 to 13 wherein the diameter of each fluid passageway is in the range of 0.8 to 0.13 times the diameter of the plate. 16. A fluid flow conditioner according to any one of claims 1 to 12 wherein the diameter of each fluid passageway is in the range of 0.05 to 0.1 times the diameter of the plate. 17. A fluid flow conditioner according to any one of the preceding claims wherein the thickness of the plate is within the range of 0.6 to 1.7 times the diameter of each passageway. 18. A fluid flow conditioner according to claim 2 wherein the upstream end and downstream end of each passageway is 0.1 times the diameter of the passageway. 19. A fluid flow conditioner according to claim 5 wherein the diffuser is 0.3 times the thickness of the plate. 20. A fluid flow conditioner according to claim 19 wherein the portion of constant cross-section is from 0.2 to 0.5 times the diameter of the passageway. 21. A fluid flow apparatus comprising a nozzle having a nozzle piece, a pipe or body portion and a coupling flange and a fluid flow conditioner according to any one of claim 1 to 20. 22. A fluid flow apparatus according to claim 21 wherein the fluid flow conditioner is located in the pipe or body portion of the nozzle. 23. A fluid flow apparatus according to claim 22 wherein the fluid flow conditioner is located in the coupling flange. 24. According to any one of claims 21, 22 or 23 and furthe including a stem portion connected to the central passageway of the fluid flow diffuser whereby the fluid flow apparatus constitutes a fog nozzle.

Inventors: MEYER DAVID JEFFREY, MEYER, DAVID, JEFFREY
Applicants: MEYER DAVID JEFFREY, ORION SAFETY IND PTY LTD, MEYER, DAVID, JEFFREY, ORION SAFETY INDUSTRIES PTY. LIMITED
Application year: 1995
Main classification: F15D1
IPC codes: A62C31, B05B1, F15D1