ABRASIVE FLUID JET APPARATUS

Abstract: A carrier fluid with entrained particulate solid material (14), for abrasive purposes, is fed through an inlet (12) in a housing (3) so as to follow a spiral path, thereby preventing the particulate solid material (14) from settling under the influence of gravity. The housing (3) defines a transfer space (5) which is bounded, in part, by a first end (18) and a second end (20) of the housing (3). The fluid with the entrained particulate solid material (14) is deflected inwardly by the inner surfaces (15 and 16) of the first and second ends (18 and 20) of the housing (3) into a liquid jet (11) issuing from a jetting nozzle (9) in the first end (18) of the housing (3). The particulate solid material (14) is thereby entrained in the outer layer of the jet (11) issuing from an outlet aperture (8) in the second end (20) of the housing (3), thus enabling the jet (11) to be used for cutting or cleaning purposes.

Description: " ** - - Abrasive Fluid Jet Apparatus Technical Field The invention relates to an abrasive fluid jet apparatus in whic particulate solid material is entrained in a fluid jet for th purpose of improving the cutting and/or cleaning ability of the jet. Background Art One known form of dispenser for a jet of fluid bearing particulate abrasive material, disclosed in UK Patent Specification No. 1569 736, comprises housing means defining a transfer space; outlet means defining an outlet aperture extending from the transfer space; and jetting nozzle means for directing a fluid through the transfer space and the outlet aperture in a jet. However, in this known form of apparatus, the particulate solid material is fed into the transfer space in a dry condition along passages extending convergently with the axis of the je , the dry particulate solid material being drawn into the transfer space as a result of suction caused by the jet passing through the transfer space. Thus, even where great care is taken in the design and manufacture of apparatus such as this, there is a tendency for the dry particulate solid material to clog and thereby cause variations in the amount of particulate solid material entrained in the jet. Disclosure of the Invention The purpose of the present invention is to provide an abrasive fluid jet apparatus which is less difficult to design and manufacture and in which particulate solid material is entrained in the fluid jet at a more uniform rate than in known apparatus. This is achieved by providing inlet means for directing a carrier fluid, in which the particulate solid material is entrained, along a spiral path within the transfer space and guide means for conducting OM the carrier fluid with the entrained particulate solid material through the transfer space towards the jet for entraining the particulate solid material in the outer layer of the jet. The invention therefore provides an abrasive fluid jet apparatus comprising housing means defining a transfer space; inlet means for directing a carrier fluid with entrained particulate solid material along a spiral path within the transfer space; outlet means defining an outlet aperture extending from the transfer space; jetting nozzle means for directing a fluid through the transfer space and through the outlet aperture in a jet; guide means for conducting the carrier fluid with the entrained particulate solid material through the transfer space towards the jet for entraining the particulate solid material in the outer layer of the jet. Thus, by entraining the particulate solid material in a carrier fluid and providing means for directing this carrier fluid along a spiral path, it is possible to maintain a constant concentration of solid particulate material in the carrier fluid entrained in the outer layer of the jet. Conveniently, a housing encloses the transfer space and has first and second ends respectively surrounding the jetting nozzle means and the outlet means and a connecting wall extending between Hie first and the second ends; and the guide means comprise inner surfaces of the transfer space which deflect the carrier fluid with the entrained particulate solid material in the transfer space radially inwards towards the axis of the jet. Thus, in one eπibcidiment according to the invention, the transfer space is bounded by the first and second ends and the connecting wall. I a preferred form of the invention, for use with a particulate solid material which is denser than the carrier fluid, the outlet means comprise a tubular member extending from within the housing; and the transfer space is bounded, in part, by the tubular member the connecting wall and the second end of the housing. The inne surface of the first end may be shaped so as to facilitate th movement of the particulate solid material towards the jet and j- 5 preferably frusto-conical in shape. With this form of apparatus, particulate solid material i concentrated towards the outer portion of the transfer space, as result of centrifugal force, whereas the carrier fluid i concentrated towards the central portion of the transfer space. 10However, as a result of secondary flow within the converging portio of the transfer space which is bounded, in part, by the frusto- conical inner surface of the first end of the housing, the particulate solid material is concentrated around the jet to facilitate entrainment of the particulate solid material in the outer 15layer of the jet and the carrier fluid is discharged from the transfer space in the form of a curtain which surrounds the fluid jet and its entrained particulate solid material, thus providing a protective barrier between the particulate solid material and the outlet means to prevent or reduce abrasive wear of the outlet means. 0 Alternatively, the carrier fluid can be vented directly to atmosphere through vents in the second end of the housing. The momentum of the carrier luid with the entrained particulate solid material flowing in the spiral path is very low compared with that of the fluid in the jet (typically less than 0.5^) so that the 5 swirl it produces is dissipated within the outlet means. Brief description of the drawings Figure 1 is • a schematic half-sectional side elevation of a first abrasive fluid jet apparatus embodying the invention; Figures 2 is a sectional side elevation of a second abrasive fluid ϋ jet apparatus embodying the invention; and Figure 3 is a sectional end elevation across the Section III - III in Figure 2. Modes for Carrying Out the Invention In the first embodiment 1 of the invention, illustrated in Figure 1, jetting nozzle means, in the form of a single jetting nozzle 9 direct a jet of fluid 11 through an outlet aperture 8. Inlet means 12 extend tangentially into a transfer space 5 within the housing 3- Carrier fluid, such as water, with entrained particulate solid material, such as particles of sand, is therefore directed into the transfer space 5 so as to flow along a spiral path. Clearly, it is not necessary for the inlet 12 to extend perfectly tangentially; all that is necessary is that the inlet 12 extends along an axis which has at least a component extending tangentially of the transfer space 5» Similarly, although it is preferred that the transfer space 5 should be of circular cross-section, the cross- section may be non-circular. Carrier fluid with entrained ^ particulate solid material 1 is directed towards the central axis of the transfer space 5 where it is entrained in the outer layer of a jet extending from the jetting nozzle 9 and through the transfer space 5 and the outlet aperture 8. The apparatus 1 thus ensures that the concentration of particulate solid material 14 in the carrier fluid fed to the jet 11 remains constant and is uniformly entrained in the outer layer of the jet 11. In this eiribodiment of the invention, the transfer space 5 is enclosed by a housing 3 having a first end 18 surrounding jetting nozzle means in the form of a jetting nozzle 9, and a second end 20 surrounding outlet means in the form of an outlet nozzle 6. Carrier fluid with entrained particulate solid material 14 is fed into the housing 3 through inlet means 12 adjacent a connecting wall 22 extending between the first end 18 and the second end 20 so as to direct the carrier fluid with the entrained particulate solid material 14 along a spiral path within the transfer space 5- Guide means, in the form of the inner surfaces 15 and 16 of the first end 18 and the second end 20 conduct the carrier fluid with the entrained particulate solid material 14 radially inwards into contact with the jet 11 issuing from the jetting nozzle 9 so that the. particulate material 14 is entrained in the outer layer of the jet 11 which issues from the outlet nozzle 6. In the second embodiment 2, illustrated in Figures 2 and 3 of the drawings, the transfer space 5 is again enclosed within a housing 4 having a first end 19 surrounding jetting nozzle means in the form of a jetting nozzle 10 and a second end 21 surrounding outlet means in the form of an outlet tube 7 extending frcβn the transfer space 5 to beyond the second end 21 of the housing 4- connecting wall 23 extends between the first end 19 and the second end 21 of the housing 4. The outlet tube 7 defines an outlet aperture " 8 having a cross- section larger than that of a fluid jet 11 issuing f om the jetting nozzle 10. However, in this case, the inlet means 13 are disposed adjacent the second end 21 of the housing 4 so as to direct a carrier fluid with entrained particulate solid material 14 along a spiral path in the transfer space-5 which is bounded, in part, by the second end 21 of the housing 4> The carrier fluid with the entrained particulate solid material 14 is conducted by guide means in the form of a frusto-conical inner surface 17 of the first end 19 of the housing 4 which direct the carrier fluid and the entrained particulate solid material 14 radially inwards into a fluid jet 11 issuing from the jetting nozzle 10. However, where the particulate solid material 14 is more dense than the carrier fluid, centrifugal separation causes an increase in the concentration of the particulate solid material 14 in the carrier fluid fed into the upstream portion of the jet 11 and a decrease in the concentration of the particulate solid material 14 in the carrier fluid fed into the downstream portion of the jet 11 passing through the transfer space 5- As a result, the carrier fluid forms a protective screen between the inner surface of the outlet tube 7 and the outer layer of the jet 11 in which the particulate solid material 14 is entrained. O WIP ■

Claims: Claims 1. An abrasive fluid jet apparatus (1 or 2) comprising: housing means ! {3 or 4) defining a transfer space (5); outlet means (6 or 7) defining an outlet aperture (8) extending from the transfer space (5); and jetting nozzle means (9 or 10) for directing a fluid through the transfer space (5) and the outlet aperture (8) in a jet (11); characterised in that: inlet means (12 or 13) are provided for directing a carrier fluid, in which the particulate solid material (14) is entrained, along a spiral path within the transfer space (5); and guide means (15 and 16, or 17) are provided for conducting, the carrier fluid with the particulate solid material (14) through the transfer space (5) towards the jet (11) for entraining the particulate solid material (14) in the outer layer of the jet (11). 2. Apparatus (1 or 2), according to Claim 1, in which: a housing (3 or 4) encloses the transfer space (5 ) and has a first end (l8 or 19) a second end (20 or 21) respectively surrounding the jetting nozzle means (9 or 10) and the outlet means (6 or 7) , and a connecting wall (22 or 23) extending between the first end (18 or 19) and the second end (20 or 21); and the guide means comprise inner surfaces (15 and 16, or 17) of the transfer space (5) which deflect the carrier fluid with the entrained particulate solid material (14) in the transfer space (5) radially inwards towards the axis of the jet (11). 3- Apparatus (1), according to Claim 2, in which the transfer space (5) is bounded by the first and second ends (18 and ~ 20) and the connecting wall (22). 4. Apparatus (2), according to Claim 2, for use with a particulate solid material (14) which is denser than the carrier fluid, in which: the outlet means comprise a tubular member (7) extending from within the housing (4); and the transfer space (5) is bounded, in part, by the tubular member (7), "the connecting wall (23) and the second end (21) of the housing (4). 5- Apparatus (2), according to Claim 4, in which the inner surface (17) of the first end (19) is shaped so as to facilitate the " movement of the particulate solid material (14) towards the jet (11). 6. Apparatus according to Claim 5, in which the inner surface (17) of the first end (19) is frusto-conical in shape. 7. An abrasive fluid jet apparatus (1 or 2) substantially as hereinbefore described with reference to and as illustrated in Figure 1 or Figures 2 and 3»

Inventors: SAUNDERS DAVID HENRY, SAUNDERS, DAVID, HENRY
Applicants: FLUID ENG PROD, FLUID ENGINEERING PRODUCTS LIMITED
Application year: 1983
Main classification: B05B7
IPC codes: B05B7, B24C5, B24C7, B26F3