GB2202506A - Pneumatic transfer of particulate material - Google Patents

Pneumatic transfer of particulate material Download PDF

Info

Publication number
GB2202506A
GB2202506A GB08804971A GB8804971A GB2202506A GB 2202506 A GB2202506 A GB 2202506A GB 08804971 A GB08804971 A GB 08804971A GB 8804971 A GB8804971 A GB 8804971A GB 2202506 A GB2202506 A GB 2202506A
Authority
GB
United Kingdom
Prior art keywords
sand
particulate material
ejector
barrel
air
Prior art date
Legal status (The legal status 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 status listed.)
Pending
Application number
GB08804971A
Other versions
GB8804971D0 (en
Inventor
Weston Crescent Paul Wi Mosley
David Charles Beresford
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
British Railways Board
Original Assignee
British Railways Board
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
Priority claimed from GB878705392A external-priority patent/GB8705392D0/en
Priority claimed from GB878718550A external-priority patent/GB8718550D0/en
Application filed by British Railways Board filed Critical British Railways Board
Publication of GB8804971D0 publication Critical patent/GB8804971D0/en
Publication of GB2202506A publication Critical patent/GB2202506A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/04Conveying materials in bulk pneumatically through pipes or tubes; Air slides
    • B65G53/24Gas suction systems
    • B65G53/26Gas suction systems operating with fluidisation of the materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B61RAILWAYS
    • B61CLOCOMOTIVES; MOTOR RAILCARS
    • B61C15/00Maintaining or augmenting the starting or braking power by auxiliary devices and measures; Preventing wheel slippage; Controlling distribution of tractive effort between driving wheels
    • B61C15/08Preventing wheel slippage
    • B61C15/10Preventing wheel slippage by depositing sand or like friction increasing materials
    • B61C15/102Preventing wheel slippage by depositing sand or like friction increasing materials with sanding equipment of mechanical or fluid type, e.g. by means of steam
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/04Conveying materials in bulk pneumatically through pipes or tubes; Air slides
    • B65G53/28Systems utilising a combination of gas pressure and suction
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/34Details
    • B65G53/40Feeding or discharging devices
    • B65G53/42Nozzles

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Transportation (AREA)
  • Jet Pumps And Other Pumps (AREA)

Abstract

A method of pneumatically transferring particulate material from a bulk comprises disposing a tubular device (2) in the bulk (3), the tubular device (2) having a longitudinal opening (7) for the ingress of the particulate material, an air and particulate material outlet (4b) at or towards one end and an air inlet (4a) at or towards its other end, applying suction to the outlet (4b) to draw air from the inlet (4a) and so entrain particulate material from the bulk (3) and simultaneously applying fluid pressure from a pressurised source to the inlet (4a). The method has been found to have particularly advantageous application in sand box and ejector equipment for railway locomotives in which the tubular device (2) is disposed in the sand box (1) for transferring sand from the sand box (1) to the ejector.

Description

Pneumatic Transfer of Particulate Material This invention relates to the pneumatic transfer of particulate material from a bulk at one location to a second location. Such transfer has appplication in large size installations for the transfer of, for example, sand, cement, fly ash, sugar, grain to and from railway vehicles, down to small installations such as coffee dispensing machines. It also has application in sand box and ejection equipment of railway locomotives.
One object of the invention is to provide a pneumatic transfer system in which particulate material can be transferred even though it may contain a relatively high degree of dampness.
According to one aspect of the invention a method of pneumatically transferring particulate material from a bulk comprises disposing a tubular device in the bulk, the tubular device having a longitudinal opening for the ingress of the particulate material and a fluid particulate material outlet at or towards one end and a fluid inlet at or towards its other end, applying suction to said outlet to entrain particulate material from the bulk and simultaneously applying fluid pressure from a pressurised source to said inlet. In many applications the fluid will be air.
According to a second aspect of the invention, there is provided an apparatus for transferring particulate material from a bulk at a first location to a second location comprising a tubular device adapted to be disposed in the bulk and having a longitudinal opening for the ingress of particulate material, an outlet at or towards one end for particulate material, a fluid inlet at or towards the other end, means for applying suction to said outlet and a pressurised fluid source for applying a fluid pressure to said fluid inlet.
The invention has been found to have particularly advantageous application in sand box and ejector equipment for railway locomotives. Such equipment must be capable of operating for short periods at a controlled rate and be reliable despite variations in the condition of the sand. The invention will now be further described in this context.
In order to improve traction under certain railway track conditions (under wet or greasy conditions), a small quantity of sand or other grit is placed between the rail and the driving wheel of the locomotive. The sand is stored in boxes on the locomotive from which it is carried to a sand ejector and directed towards the wheel and rail.
Various methods have been used to deliver the sand from its box. The early methods worked largely by a gravity feed from the bottom of the box. Later methods operate on a suction principle and all have devices suspended in the sand with an opening through which the sand can be collected from the box. In each of these devices one end, i.e. the inlet end, is open to the atmosphere and the other is connected to the sand ejector which has a venturi to create a suction pressure.
When the ejector operates it therefore causes a fall in air pressure which draws air through the device picking up grains of sand and carrying them to the ejector. All of these devices have difficulty in removing from the box, sand that will not flow due to damp or compaction, and some are prone to blockages.
In applying the invention to a sand box and ejector equipment for a railway locomotive, the aforesaid tubular device is disposed in the sand box for transferring sand from the sand box to the ejector.
It has been found, very surprisingly, that applying a positive pressure, i.e. an above atmospheric pressure, to the inlet of the device is very effective in providing a very consistent sand delivery to the ejector irrespective of whether the sand is dry or damp.
Existing designs of ejector contain a nozzle through which pressurised air is allowed to escape at high velocity into and along the barrel of the ejector. This causes a partial vacuum within the barrel, in the vicinity of the nozzle, which is used to draw in sand at an angle to the ejector barrel and hence into the stream of escaping air as shown in Figure 1 of the accompanying drawings. After several hours of continual use the case hardened barrel opposite the sand inlet is worn to the extent that replacement becomes necessary. Furthermore the changes in section and direction of the sand path make this type of ejector prone to blockage.
In further development of the invention and in order to overcome these problems a new design of ejector has been produced which allows the sand to travel in a straight path.
Thus the reliability of the ejector and the useful life of the barrel are thereby increased. In this new design of ejector the sand passes along a straight duct to an inlet port on the axis of the barrel, the said duct and the barrel being co-axial. The barrel is of slightly larger diameter than the inlet port and high pressure air is arranged to enter the barrel around the outside of the sand inlet, to produce a partial vacuum that draws the sand into the high velocity air blast.
This design of ejector produces a more uniform pattern of wear on the barrel than is achieved with the previous type of ejector shown in Figure 1.
The invention will now be further described by way of example as applied to sand box and ejector equipment on a railway locomotive and with reference to Figures 2 to 4 of the accompanying diagrammatic drawings in which: Figure 2 illustrates the equipment with the sand box shown in section, Figure 3 shows a preferred form of ejector in accordance with the invention, and Figure 4 shows a cross-section through a preferred form of tubular device for collecting sand from the sand box.
Referring to Figures 2 to 4 of the drawings, sand box 1 contains a sand collecting device 2 embedded in the sand 3.
The device 2 comprises a horizontal sand collecting tube extending substantially horizontally and linearly between opposite sides of the sand box adjacent the bottom of the sand box 1 and connecting with ports in these sides. At these ports inlet tube 5 and outlet tube 6 are sealed into the inlet and outlet ends 4a and 4b of the collecting tube 2. Along its lower side the tube is provided with a slit 7 through which the sand is drawn from the box 1 into the tube 2. The slit may, for example, extend over 1200 of arc about the centre of the tube 2. However, this angle may vary to suit the desired characteristics of the material being delivered.
The inlet tube 5 tees into a line 8 which leat from a source of air pressure. The outlet -tube 6 leads to a sand ejector 9 which also connects via the line 8 to the source of air pressure. Chokes 11 and 12 are fitted in the inlet tu 5 and in the line 8 adjacent the ejector 9. The choke 11 controls the air flow to the device 2 via the inlet tube 5 and the choke 12 controls the air flow to the ejector 9 which creates a suction pressure in outlet tube 6 to draw air and sand from the sand box I through the device 2.
In this particular example the pressure applied by the air source is between 50 and 100 p.s.i. (345 - 690 kN/m2). The range of the chokes 11 and 12 is 1 to 2 mm. The vacuum produced by the ejector is 2"-6" of mercury. The flow of sand through the outlet tube 6 and out of the ejector is between 300 and 700 grams per minute.
In operation, as the sand. ejector 9 applies suction to the outlet tube 6 a positive air pressure is simultaneously applied to the inlet tube 5 from the source of air pressure.
The air movement caused within the sand box 1 is rapid and turbulent and may extend beyond the confines of the collecting tube 2. A slight positive pressure is thus produced which helps to prevent the ingress of atmospheric air into the box 6 and reduces compaction of the sand.
It was observed that the speed and turbulence of the air through the device 2 is very effective in dislodging sand grains from around it and the slight positive pressure bursts any cavities so formed. By control of air pressures and tube and choke sizes the rate of delivery is reliably controlled.
It is ts be noted that this method will work for other material than sand and with other fluid media than air.
As seen in Figure 3, the ejector 9 comprises straight air and sand duct 21 extending co-axially with the ejector barrel 22. The duct 21 is of smaller diameter than the barrel 22 and connects with the barrel 22 via annular shoulder 23.
Surrounding the duct 21 is an annular air duct 24 which connects via supply duct 25 to the high pressure air supply line 8. Leading from the duct 24 are a series of ducts 27 which have orifices in the shoulder 23 opening into the barrel 22. The ducts 27 are regularly spaced about the axis of the duct 21 and are inclined towards the axis of the barrel 22 so that the air issuing from the orifices makes an angle if of about 150 with the axis of the barrel 22 to create areas of vacuum 28 in the barrel 22 as shown in dotted line adjacent the shoulder 23 to cause sand and air to be drawn along duct 21 and into the barrel 22. Since the sand is not drawn in at a significant angle with respect to the barrel axis, there is no significant short term wear on the barrel by the direct impingement of sand.
Figure 4 shows a cross-section of a particular form of tubular device 2 for collecting sand from the sand box 1. In the device 2 of Figure 4 the inlet for the sand instead of being a slit is a throat 31 formed by shaping the material of the device 2 and through which the sand must pass in order to enter the device 2. This throat 31 providing that its width is appropriately sized in relation to the particulate material can act as a valve to prevent back feed of the material. Thus if the pressures are removed, and the weight of the material tends to push the material back, the throat 31 becomes blocked with the material.

Claims (1)

1. A method of transferring particulate material from a bulk at a first location to a second location comprising disposing a tubular device in the bulk, the tubular device having a longitudinal opening for the ingress of the particulate material, a fluid and particulate material outlet at or towards one end and a fluid inlet at or towards its other end, applying suction to said outlet to entrain particulate material from the bulk and simultaneously applying fluid pressure from a pressurised source to said inlet.
2. A method according to claim 1, wherein said fluid is air.
3. An apparatus for transferring particulate material from a bulk at a first location to a second location comprising a tubular device adapted to be disposed in the bulk and having a longitudinal opening for the ingress of particulate material, an outlet at or towards one end for particulate material, a fluid inlet at or towards the other end, means for applying suction to said outlet and a pressurised fluid source for applying a fluid pressure to said fluid inlet.
4. A sand box and ejector equipment for a railway locomotive and comprising an apparatus according to claim 3 disposed in the sand box for transferring sand from the sand box to the ejector.
5. An equipment according to claim 4, wherein said tubular device extends substantially horizontally and linearly adjacent the bottom of the sand box.
6. An equipment according to claim 4 or 5, wherein said pressurised fluid source also connects with said ejector to create the suction at the outlet of said tubular device.
7. An equipment according to any of claims 3 to 6, wherein the longitudinal opening in said tubular device comprises a throat through which the sand has to pass in order to enter the device.
8. An equipment according to any of claims 3 to 7, wherein the ejector comprises an ejector barrel and an air and sand duct extending coaxially with the ejector barrel, the duct being of smaller diameter than the barrel and connecting with the barrel via an annular shoulder, and a plurality of air ducts connecting with the pressurised source and having orifices in the shoulder, which orifices are spaced from one another around the shoulder whereby air flowing through said orifices from the pressurised source creates suction in the barrel to cause air and sand to be drawn along said air and sand duct.
10. An equipment according to claim 9, wherein said air ducts are inclined towards the axis of said barrel.
Amendments to the claims have been filed as follows CLAIMS 1. A method of transferring particulate material from a bulk at a first location to a second location comprising disposing a tubular device in the bulk, the tubular device having a laterally or downwardly directed longitudinal opening for the ingress of the particulate material, a fluid and particulate material outlet at or towards one end and a fluid inlet at or towards its other end, applying suction to said outlet to entrain particulate material from the bulk and simultaneously applying fluid pressure from a pressurised source to said inlet.
2. A method according to claim 1, wherein said fluid is air.
3. An apparatus for transferring particulate material from a bulk at a first location to a second location comprising a tubular device adapted to be disposed in the bulk and having a longitudinal opening for the ingress of particulate material, an outlet at or towards one end for particulate material, a fluid inlet at or towards the other end, means for applying suction to said outlet and a pressurised fluid source for applying a fluid pressure to said fluid inlet.
4. A sand box and ejector equipment for a railway locomotive and comprising an apparatus according to claim 3 disposed in the sand box with the longitudinal opening laterally or downwardly directed for transferring sand from the sand box to the ejector.
5. An equipment according to claim 4, wherein said tubular device extends substantially horizontally and linearly adjacent the bottom of the sand box.
6. An equipment according to claim 4 or 5, wherein said pressurised fluid source also connects with said ejector to create the suction at the outlet of said tubular device.
7. An equipment according to any of claims 3 to 6, wherein the longitudinal opening in said tubular device comprises a throat through which the sand has to pass in order to enter the device.
8. An equipment according to any of claims 3 to 7, wherein the ejector comprises an ejector barrel and an air and sand duct extending coaxially with the ejector barrel, the duct being of smaller diameter than the barrel and connecting with the barrel via an annular shoulder, and a plurality of air ducts connecting with the pressurised source and having orifices in the shoulder, which orifices are spaced from one another around the shoulder whereby air flowing through said orifices from the pressurised source creates suction in the barrel to cause air and sand to be drawn along said air and sand duct.
10. An equipment according to claim 9, wherein said air ducts are inclined towards the axis of said barrel.
GB08804971A 1987-03-07 1988-03-02 Pneumatic transfer of particulate material Pending GB2202506A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
GB878705392A GB8705392D0 (en) 1987-03-07 1987-03-07 Sand boxes
GB878710938A GB8710938D0 (en) 1987-03-07 1987-05-08 Sand box & ejector equipment
GB878718550A GB8718550D0 (en) 1987-03-07 1987-08-05 Pneumatic transfer of particulate material

Publications (2)

Publication Number Publication Date
GB8804971D0 GB8804971D0 (en) 1988-03-30
GB2202506A true GB2202506A (en) 1988-09-28

Family

ID=27263340

Family Applications (1)

Application Number Title Priority Date Filing Date
GB08804971A Pending GB2202506A (en) 1987-03-07 1988-03-02 Pneumatic transfer of particulate material

Country Status (3)

Country Link
AU (1) AU1349488A (en)
GB (1) GB2202506A (en)
WO (1) WO1988007017A1 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2259911A (en) * 1991-09-03 1993-03-31 Ingersoll Rand Co Flow reduced feed collector and transporter apparatus.
FR2796004A1 (en) * 1999-07-06 2001-01-12 Monique Bassaler Device adapted to long distance lorries to provide better driving wheel adherence on slippery ground uses dry heated sand contained in tank withdrawn by compressed air and ejected in front of wheel
EP1182109A1 (en) * 2000-03-17 2002-02-27 Railway Technical Research Institute Slip prevention particle injection device
FR2879578A1 (en) * 2004-12-22 2006-06-23 Cms Automatisme Sarl Filling device for fluid products e.g. granulates has input line having one end exposed to ambient air while other end is inserted into storage vessel
CN100434317C (en) * 2002-10-11 2008-11-19 财团法人铁道总合技术研究所 Antiskid material sprinkling apparatus
EP2775142A1 (en) * 2013-03-07 2014-09-10 Forges de Belles Ondes Device for ejecting granular material by venturi effect
CN104554298A (en) * 2015-02-05 2015-04-29 南车株洲电力机车有限公司 Locomotive and sanding device thereof
WO2022043546A1 (en) * 2020-08-31 2022-03-03 Knorr-Bremse Gesellschaft Mit Beschränkter Haftung Pneumatic sand conveying device for a sanding system of a rail vehicle, sanding system, and method for operating a pneumatic sand conveying device

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0720771B2 (en) * 1988-11-30 1995-03-08 エーザイ株式会社 Pneumatic transportation device for powder

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB485159A (en) * 1936-11-09 1938-05-09 Smidth & Co As F L Improvements relating to discharge arrangements of containers for powdered or granular material
GB1012592A (en) * 1963-08-29 1965-12-08 Baker Perkins Ltd Improvements in and relating to pneumatic conveying apparatus

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE75525C (en) * G. LENTZ in Düsseldorf, Uhlandstr. 18 Sand spreader for locomotives
FR585888A (en) * 1924-09-03 1925-03-09 Kestner & Neu Snc Material introduction device, applicable to pneumatic transport or cleaning installations
FR2067102A7 (en) * 1969-11-04 1971-08-20 Hedde Francois
FR2579573A1 (en) * 1985-03-28 1986-10-03 Barron Claude Method and device for extracting pulverulent and/or granular substances

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB485159A (en) * 1936-11-09 1938-05-09 Smidth & Co As F L Improvements relating to discharge arrangements of containers for powdered or granular material
GB1012592A (en) * 1963-08-29 1965-12-08 Baker Perkins Ltd Improvements in and relating to pneumatic conveying apparatus

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2259911A (en) * 1991-09-03 1993-03-31 Ingersoll Rand Co Flow reduced feed collector and transporter apparatus.
GB2259911B (en) * 1991-09-03 1995-04-19 Ingersoll Rand Co Flow induced feed collector and transporter apparatus
FR2796004A1 (en) * 1999-07-06 2001-01-12 Monique Bassaler Device adapted to long distance lorries to provide better driving wheel adherence on slippery ground uses dry heated sand contained in tank withdrawn by compressed air and ejected in front of wheel
EP1182109A1 (en) * 2000-03-17 2002-02-27 Railway Technical Research Institute Slip prevention particle injection device
EP1182109A4 (en) * 2000-03-17 2003-06-25 Railway Technical Res Inst Slip prevention particle injection device
US6722589B1 (en) 2000-03-17 2004-04-20 Railway Technical Research Institute Slip prevention particle injection device
CN100434317C (en) * 2002-10-11 2008-11-19 财团法人铁道总合技术研究所 Antiskid material sprinkling apparatus
FR2879578A1 (en) * 2004-12-22 2006-06-23 Cms Automatisme Sarl Filling device for fluid products e.g. granulates has input line having one end exposed to ambient air while other end is inserted into storage vessel
EP2775142A1 (en) * 2013-03-07 2014-09-10 Forges de Belles Ondes Device for ejecting granular material by venturi effect
FR3002990A1 (en) * 2013-03-07 2014-09-12 Belles Ondes Forges DEVICE FOR EJECTING GRANULAR MATERIAL WITH VENTURI
CN104554298A (en) * 2015-02-05 2015-04-29 南车株洲电力机车有限公司 Locomotive and sanding device thereof
WO2022043546A1 (en) * 2020-08-31 2022-03-03 Knorr-Bremse Gesellschaft Mit Beschränkter Haftung Pneumatic sand conveying device for a sanding system of a rail vehicle, sanding system, and method for operating a pneumatic sand conveying device

Also Published As

Publication number Publication date
WO1988007017A1 (en) 1988-09-22
AU1349488A (en) 1988-10-10
GB8804971D0 (en) 1988-03-30

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