WO1986006311A1 - Abrasive fluid flow - Google Patents

Abrasive fluid flow Download PDF

Info

Publication number
WO1986006311A1
WO1986006311A1 PCT/GB1986/000224 GB8600224W WO8606311A1 WO 1986006311 A1 WO1986006311 A1 WO 1986006311A1 GB 8600224 W GB8600224 W GB 8600224W WO 8606311 A1 WO8606311 A1 WO 8606311A1
Authority
WO
WIPO (PCT)
Prior art keywords
flow channel
section
conduit
abrasive material
centre
Prior art date
Application number
PCT/GB1986/000224
Other languages
French (fr)
Inventor
Roger Artindale Heron
David Henry Saunders
Original Assignee
The British Hydromechanics Research Association
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by The British Hydromechanics Research Association filed Critical The British Hydromechanics Research Association
Priority to DE1986902854 priority Critical patent/DE258242T1/en
Priority to DE8686902854T priority patent/DE3665144D1/en
Priority to AT86902854T priority patent/ATE45693T1/en
Publication of WO1986006311A1 publication Critical patent/WO1986006311A1/en
Priority to NO865292A priority patent/NO172970C/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B24GRINDING; POLISHING
    • B24CABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
    • B24C5/00Devices or accessories for generating abrasive blasts
    • B24C5/02Blast guns, e.g. for generating high velocity abrasive fluid jets for cutting materials
    • B24C5/04Nozzles therefor

Definitions

  • An abrasive fluid that is a fluid with abrasive material entrained therein, causes wear on the surfaces of conduits through which it passes.
  • the object of the present invention is to reduce such interceptr.
  • nozzles in one or more grades of wear resistant materials such as ceramics (for example tungsten carbide, silicon carbide, aluminium oxide). These materials have been used in conventional nozzle shapes which are designed to accelerate the flow of fluid without undue loss of energy and without introducing disturbance which would cause the resulting > high velocity jet of fluid to break up.
  • ceramics for example tungsten carbide, silicon carbide, aluminium oxide.
  • the present invention has the object of directing the abrasive material in abrasive fluids away frcm the internal surfaces of the nozzle in order to reduce such i ⁇ pact.
  • a method of transporting an abrasive fluid comprising abrasive material and carrier fluid through a conduit comprising directing the abrasive material along the centre of the flow channel within the conduit, accelerating the carrier fluid and entraining the abrasive material within the accelerated carrier fluid.
  • a fluid flow conduit comprising a flow channel, means adjacent to the upstream section of the conduit for directing abrasive material along the centre of the flow channel, a section of reduced cross section for accelerating carrier fluid in the flow channel and a down-stream section for accelerating the abrasive material at the centre of the flow channel due to entrainment with the accelerated carrier fluid.
  • Figure 1 is a diametral cross-section through a nozzle assembly
  • Figures 2 to 4 are schematic diametral cross-sections through alternative nozzle assemblies
  • Figure 5 is a view on lines 5-5 in Figure 2
  • Figure 6 is a view on lines 6-6 on Figure 4.
  • abrasive fluid enters the up-stream section 1 of relatively large cross-section and abrasive material within * the fluid is deflected towards the centre of the flow channel by a tapered portion 4 between the upstream section 1 and the mid-stream section 2.
  • the carrier fluid tends to flow in stream-line manner in contact with the internal surfaces of the flow channels 1 and 2, whereas the abrasive material tends to be deflected by the tapered portion 4 towards the centre of the flow channel within the section 2.
  • Dcwn-strearr. of the mid-stream section 2 is a further tapered portion 5 which causes ' the carrier fluid to accelerate due to its decreasing cross-section, and as the abrasive fluid flows through the down-stream section 3 following the tapered section 5, there is an interchange of momentum between the carrier fluid and the abrasive material flowing in the centre of the flow channel, so that the abrasive material is accelerated and leaves the outlet 6 of the nozzle assembly at high velocity.
  • Typical dimensions of such a nozzle assembly include diameters of 17-0, 11.3 and 2.8mm for the up-stream section 1, mid-stream section 2 and down-stream section 3 > an entrance diameter of 9.5mm for the tapered section 5, a length of 27mm for the tapered section 4 and mid-stream section 2 together, and a length of 60mm for the tapered section 5 and down-stream section 3 together.
  • the outer diameter of the down-stream section 3 s 12mm.
  • the tapers of the sections 4 and 5 can be widely varied to achieve the desired effect of deflection of the abrasive material and acceleration of the carrier fluid, as will be seen from comparison of Figures 1 to 4-
  • the angle of taper of the section 4 is much greater, and the mid-stream section 2 and the tapered section 5 are combined into a single section of uniform taper and the down-stream section 3 is also tapered, to a smaller degree than the mid-stream section.
  • a central flow deflector 9 is mounted i the centre of the up-stream section 1, supported by radial vanes as shown in Figure 5 «
  • the flow defector 9 has a conical up-stream section, a cylindrical mid-stream section and a conical down-stream section of very large included angle.
  • the flow deflector serves to deflect particles towards the outside of the flow channel in section 1 , so tha the tapered section 5 which has an included angle of about 120° is able to deflect the particles to the centre of the flow channel in the mid-stream section 2.
  • the tapered section 4 has an included angle of more than l80°, in this case about 270°. This arrangement is particularly suitable when the abrasive material comprises large particles of high density.
  • the flow deflector 9 has a domed up-stream portion and the re-entrant domed down-stream portion.
  • the tapered portion 5 s in this case seperate from the mid-stream portion which is cylindrical and the taperd portion 5 is rounded and the down-stream portion 3 cylindrical.
  • Figure 4 the geometry of Figure 2 is followed, except that the flow deflector 9 is replaced by a centrifugal entry system 8, more clearly seen in the view in Figure 6, by which abrasive fluid enters the up-stream section tangentially so that abrasive material tends to flow around the outside of the up-stream section in a spiral flow before deflection by the tapered portion 4 *
  • a number of ribs 11 are provided in the tapered mid-stream section to prevent the spiral flow of fluid extending through that section ip order to prevent abrasive material which has been deflected to the centre of the flow channel by the tapered portion 4 being carried to the outside of that section by further centrifugal action.
  • the ribs 11 do not extend to the centre of the section 2 and consequently do not interfere with the abrasive particles which are concentrated at the centre of the flow channel.

Abstract

Abrasive fluid, which includes abrasive material and a carrier fluid, is transported through a conduit with minimum wear by directing the abrasive material along the centre of the flow channel within the conduit, accelerating the carrier fluid and entraining the abrasive material within the accelerated carrier fluid. A conduit for performing this method includes a flow channel, means (9) adjacent its upstream section (1) for directing abrasive material along the centre of the flow channel, a section (2) of reduced cross-section for accelerating carrier fluid in the flow channel and a down-stream section (3) for accelerating the abrasive material at the centre of the flow channel due to entrainment with the accelerated carrier fluid.

Description

ABRASIVE FLUID FLOW
An abrasive fluid, that is a fluid with abrasive material entrained therein, causes wear on the surfaces of conduits through which it passes. The object of the present invention is to reduce such vrear.
It is possible to construct nozzles in one or more grades of wear resistant materials such as ceramics (for example tungsten carbide, silicon carbide, aluminium oxide). These materials have been used in conventional nozzle shapes which are designed to accelerate the flow of fluid without undue loss of energy and without introducing disturbance which would cause the resulting > high velocity jet of fluid to break up.
When such nozzles are used with abrasive 'fluids, the abrasive material still causes some wear on contact with the internal surfaces of the nozzle and they will be slowed down by iπpact with the nozzle. The present invention has the object of directing the abrasive material in abrasive fluids away frcm the internal surfaces of the nozzle in order to reduce such iπpact.
According to one aspect of the invention there is provided a method of transporting an abrasive fluid comprising abrasive material and carrier fluid through a conduit comprising directing the abrasive material along the centre of the flow channel within the conduit, accelerating the carrier fluid and entraining the abrasive material within the accelerated carrier fluid.
According to another aspect of the invention there is provided a fluid flow conduit comprising a flow channel, means adjacent to the upstream section of the conduit for directing abrasive material along the centre of the flow channel, a section of reduced cross section for accelerating carrier fluid in the flow channel and a down-stream section for accelerating the abrasive material at the centre of the flow channel due to entrainment with the accelerated carrier fluid.
Examples of the invention will now be described as reference to the accαrpanying drawings in which:
Figure 1 is a diametral cross-section through a nozzle assembly, Figures 2 to 4 are schematic diametral cross-sections through alternative nozzle assemblies, Figure 5 is a view on lines 5-5 in Figure 2, and Figure 6 is a view on lines 6-6 on Figure 4.
In the nozzle assembly of Figure 1, abrasive fluid enters the up-stream section 1 of relatively large cross-section and abrasive material within*the fluid is deflected towards the centre of the flow channel by a tapered portion 4 between the upstream section 1 and the mid-stream section 2. The carrier fluid tends to flow in stream-line manner in contact with the internal surfaces of the flow channels 1 and 2, whereas the abrasive material tends to be deflected by the tapered portion 4 towards the centre of the flow channel within the section 2.
Dcwn-strearr. of the mid-stream section 2 is a further tapered portion 5 which causes' the carrier fluid to accelerate due to its decreasing cross-section, and as the abrasive fluid flows through the down-stream section 3 following the tapered section 5, there is an interchange of momentum between the carrier fluid and the abrasive material flowing in the centre of the flow channel, so that the abrasive material is accelerated and leaves the outlet 6 of the nozzle assembly at high velocity. It will be noted that there is a small shoulder between the mid-stream section 2 and the entrance to the tapered section 5 and the down-stream section 3 β enclosed within a cover whose outlet surface has a greater diameter than the down-stream section 3*
Typical dimensions of such a nozzle assembly include diameters of 17-0, 11.3 and 2.8mm for the up-stream section 1, mid-stream section 2 and down-stream section 3> an entrance diameter of 9.5mm for the tapered section 5, a length of 27mm for the tapered section 4 and mid-stream section 2 together, and a length of 60mm for the tapered section 5 and down-stream section 3 together. The outer diameter of the down-stream section 3 s 12mm.
The tapers of the sections 4 and 5 can be widely varied to achieve the desired effect of deflection of the abrasive material and acceleration of the carrier fluid, as will be seen from comparison of Figures 1 to 4- In Figure 2, the angle of taper of the section 4 is much greater, and the mid-stream section 2 and the tapered section 5 are combined into a single section of uniform taper and the down-stream section 3 is also tapered, to a smaller degree than the mid-stream section. A central flow deflector 9 is mounted i the centre of the up-stream section 1, supported by radial vanes as shown in Figure 5« The flow defector 9 has a conical up-stream section, a cylindrical mid-stream section and a conical down-stream section of very large included angle. The flow deflector serves to deflect particles towards the outside of the flow channel in section 1 , so tha the tapered section 5 which has an included angle of about 120° is able to deflect the particles to the centre of the flow channel in the mid-stream section 2. In the apparatus of Figure 3, the tapered section 4 has an included angle of more than l80°, in this case about 270°. This arrangement is particularly suitable when the abrasive material comprises large particles of high density. The flow deflector 9 has a domed up-stream portion and the re-entrant domed down-stream portion. The tapered portion 5 s in this case seperate from the mid-stream portion which is cylindrical and the taperd portion 5 is rounded and the down-stream portion 3 cylindrical.
In Figure 4, the geometry of Figure 2 is followed, except that the flow deflector 9 is replaced by a centrifugal entry system 8, more clearly seen in the view in Figure 6, by which abrasive fluid enters the up-stream section tangentially so that abrasive material tends to flow around the outside of the up-stream section in a spiral flow before deflection by the tapered portion 4* A number of ribs 11 are provided in the tapered mid-stream section to prevent the spiral flow of fluid extending through that section ip order to prevent abrasive material which has been deflected to the centre of the flow channel by the tapered portion 4 being carried to the outside of that section by further centrifugal action. The ribs 11 do not extend to the centre of the section 2 and consequently do not interfere with the abrasive particles which are concentrated at the centre of the flow channel.

Claims

C LA IMS
1. A method of transporting an abrasive fluid comprising abrasive material and carrier fluid through a conduit comprising directing the abrasive material along the centre of the flow channel within the conduit, accelerating the carrier fluid and entraining the abrasive material within the accelerated carrier fluid.
2. A method as claimed in Claim 1 wherein the directing step comprises deflecting abrasive material in the carrier fluid towards the centre of the flow channel within the conduit.
3. A fluid flow conduit comprising a flow channel, means adjacent to the upstream section (l) of the conduit for directing abrasive material along the centre of the flow channel, a section (2) of reduced cross section for accelerating carrier fluid in the flow channel and a down-stream section (3) for accelerating the abrasive material at the centre of the flow channel due to entrainment with the accelerated carrier fluid.
4- A conduit as claimed in Claim 3 wherein said directing means comprises deflecting means (4) adjacent the outside of the flow channel.
5. A conduit as claimed in Claim 4 wherein the deflecting means comprises a surface (4 in Figure 3) inclined at an angle greater than 90° to the downstream direction of the outside of the flow channel.
6. A conduit as claimed in anyone of Claims 3 to 5 comprising a central core (9) in the upstream section of the flow channel.
7* A conduit as claimed in Claim 6 when dependent on Claim 4 or Claim 5 wherein the downstream end. of the central core (9) is shaped to cooperate with the deflecting means to direct abrasive material along the centre of the fluid channel.
8. A conduit as claimed in anyone of Claims 3 to 7 comprising means (8) to introduce fluid into the upstream section with a tangential component.
PCT/GB1986/000224 1985-04-25 1986-04-24 Abrasive fluid flow WO1986006311A1 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
DE1986902854 DE258242T1 (en) 1985-04-25 1986-04-24 ABRASIVE FLOW.
DE8686902854T DE3665144D1 (en) 1985-04-25 1986-04-24 Abrasive fluid flow
AT86902854T ATE45693T1 (en) 1985-04-25 1986-04-24 ABRASIVE FLOW.
NO865292A NO172970C (en) 1985-04-25 1986-12-23 Nozzle device for an abrasive fluid

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB858510538A GB8510538D0 (en) 1985-04-25 1985-04-25 Nozzle
GB8510538 1985-04-25

Publications (1)

Publication Number Publication Date
WO1986006311A1 true WO1986006311A1 (en) 1986-11-06

Family

ID=10578179

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/GB1986/000224 WO1986006311A1 (en) 1985-04-25 1986-04-24 Abrasive fluid flow

Country Status (9)

Country Link
US (1) US4878785A (en)
EP (1) EP0258242B1 (en)
JP (1) JPS62502957A (en)
AU (1) AU581991B2 (en)
CA (1) CA1298707C (en)
DE (1) DE3665144D1 (en)
GB (1) GB8510538D0 (en)
WO (1) WO1986006311A1 (en)
ZA (1) ZA863056B (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5263504A (en) * 1990-12-28 1993-11-23 Carolina Equipment And Supply Company, Inc. Apparatus and method for cleaning with a focused fluid stream
US5220935A (en) * 1990-12-28 1993-06-22 Carolina Equipment & Supply Co., Inc. Apparatus and method for cleaning with a focused fluid stream
US5494381A (en) * 1991-04-11 1996-02-27 The Young Industries, Inc. Apparatus and method for pneumatically conveying bulk materials
US5931392A (en) * 1997-03-07 1999-08-03 Adams; Robert J. High-pressure cleaning spray nozzle
US5855321A (en) * 1997-08-05 1999-01-05 Hayes; John W Die lubricant nozzle assembly
USD657242S1 (en) 2010-01-14 2012-04-10 S.C. Johnson & Son, Inc. Container with nozzle
USD648216S1 (en) 2010-01-14 2011-11-08 S.C. Johnson & Son, Inc. Actuator nozzle for a diffusion device
DE102010051227A1 (en) 2010-11-12 2012-05-16 Dental Care Innovation Gmbh Nozzle for the emission of liquid cleaning agents with abrasive particles dispersed therein
US9678016B2 (en) * 2015-01-23 2017-06-13 J.M. Canty Inc Flow analyzer for harsh environments
USD825741S1 (en) 2016-12-15 2018-08-14 Water Pik, Inc. Oral irrigator handle

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1736768A (en) * 1926-07-03 1929-11-26 Carle D Boynton Gun for blowing asphalt and the like
US3522659A (en) * 1968-05-14 1970-08-04 Ralph A Welch Method and apparatus for treating solid material in particulate or fibrous form
US4080762A (en) * 1976-08-26 1978-03-28 Watson John D Fluid-abrasive nozzle device
FR2369008A1 (en) * 1976-10-26 1978-05-26 Myers Europ Gmbh FLAT SPOTLIGHT FOR A MIX OF A PRESSURIZED LIQUID AND SOLID PARTICLES
DE2928698A1 (en) * 1979-07-16 1981-02-19 Nat Res Dev Dispenser for liq. bearing particulate abrasive material - has fluid fed through nozzle to mixing chamber to pick up abrasive material in suspension
US4339406A (en) * 1979-02-26 1982-07-13 3U Partners Process of forming a nozzle
EP0110529A2 (en) * 1982-10-22 1984-06-13 Flow Industries Inc. High velocity fluid abrasive jet
US4478368A (en) * 1982-06-11 1984-10-23 Fluidyne Corporation High velocity particulate containing fluid jet apparatus and process

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US3212217A (en) * 1963-05-28 1965-10-19 Tex Tube Inc Cleaning device
US3276821A (en) * 1964-02-28 1966-10-04 Howard C Edwards Materials handling draft eductor
DE2030241A1 (en) * 1970-06-19 1971-12-23 Schaubstahl-Werke, 5910 Kreuztal Mixing nozzle for mixing in the conveyed material with conveying air in a pneumatic conveying system
JPS5537152B2 (en) * 1972-10-05 1980-09-26
DE2437856A1 (en) * 1974-08-06 1976-02-19 Lutz Tilo Kayser PROCESS AND DEVICE FOR CONTINUOUS PRESSURE TRANSFER OF FINE-PIECE BULK GOODS
US4161280A (en) * 1977-10-13 1979-07-17 State Of Connecticut Method and apparatus for dispensing a deicer liquid
SU964384A1 (en) * 1980-12-26 1982-10-07 Всесоюзный Научно-Исследовательский Биотехнический Институт Injection nozzle for spray drier
JPS60197370A (en) * 1984-03-15 1985-10-05 Mitsui Eng & Shipbuild Co Ltd Nozzle for sand blasting

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1736768A (en) * 1926-07-03 1929-11-26 Carle D Boynton Gun for blowing asphalt and the like
US3522659A (en) * 1968-05-14 1970-08-04 Ralph A Welch Method and apparatus for treating solid material in particulate or fibrous form
US4080762A (en) * 1976-08-26 1978-03-28 Watson John D Fluid-abrasive nozzle device
FR2369008A1 (en) * 1976-10-26 1978-05-26 Myers Europ Gmbh FLAT SPOTLIGHT FOR A MIX OF A PRESSURIZED LIQUID AND SOLID PARTICLES
US4339406A (en) * 1979-02-26 1982-07-13 3U Partners Process of forming a nozzle
DE2928698A1 (en) * 1979-07-16 1981-02-19 Nat Res Dev Dispenser for liq. bearing particulate abrasive material - has fluid fed through nozzle to mixing chamber to pick up abrasive material in suspension
US4478368A (en) * 1982-06-11 1984-10-23 Fluidyne Corporation High velocity particulate containing fluid jet apparatus and process
EP0110529A2 (en) * 1982-10-22 1984-06-13 Flow Industries Inc. High velocity fluid abrasive jet

Also Published As

Publication number Publication date
AU581991B2 (en) 1989-03-09
ZA863056B (en) 1986-12-30
DE3665144D1 (en) 1989-09-28
EP0258242B1 (en) 1989-08-23
EP0258242A1 (en) 1988-03-09
CA1298707C (en) 1992-04-14
AU5815086A (en) 1986-11-18
GB8510538D0 (en) 1985-05-30
US4878785A (en) 1989-11-07
JPS62502957A (en) 1987-11-26

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