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GB2183502A - Inertial separator - Google Patents

Inertial separator Download PDF

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Publication number
GB2183502A
GB2183502A GB08626972A GB8626972A GB2183502A GB 2183502 A GB2183502 A GB 2183502A GB 08626972 A GB08626972 A GB 08626972A GB 8626972 A GB8626972 A GB 8626972A GB 2183502 A GB2183502 A GB 2183502A
Authority
GB
United Kingdom
Prior art keywords
duct
screen
separator
inlet
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.)
Withdrawn
Application number
GB08626972A
Other versions
GB8626972D0 (en
Inventor
Ralph William Johnson
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.)
Dickinson Eng Ltd W H
Original Assignee
Dickinson Eng Ltd W H
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 Dickinson Eng Ltd W H filed Critical Dickinson Eng Ltd W H
Publication of GB8626972D0 publication Critical patent/GB8626972D0/en
Publication of GB2183502A publication Critical patent/GB2183502A/en
Withdrawn legal-status Critical Current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
    • B65G53/34Details
    • B65G53/60Devices for separating the materials from propellant gas

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Cyclones (AREA)

Abstract

A separator for pneumatically conveyed solids comprising a generally horizontal inlet (14) at the upper end of a downwardly curved duct (16) which terminates in a solids outlet at the bottom, having a rotary outlet airlock (22, 24). A radially inward wall of the duct comprises a perforated screen on the other side of which is an outlet duct (18) for air. The solids are inertially separated from the airflow and tend to flow against the radially outward wall (20) of the duct, away from the screen. <IMAGE>

Description

SPECIFICATION Inertial Separator This invention relates to pneumatic conveying systems typically used for conveying andlor drying products such as tobacco in its various forms, wood shavings, sawdust, paper and cardboard scrap. At the termination or discharge of such a conveyor, it is necessary to separate the conveyed product from the conveying air or gas stream.
A number of different types of such separators have been proposed previously, some of which involve passing the flow to be separated over a screen behind which suction is applied, whilst others use a cyclone principle which has the disadvantage that the material being separated can remain within the separator for an undesirably long time, which can cause it to be mechanically degraded also also undesirably dried.
One well known type of separator is shown in U.S.
patent No. 3,727,755, and includes a suction drum (212) having an air permeable surface, and the stream of cut tobacco is directed to move almost tangentially beneath the drum, as it is delivered from the end of the conveyor 13. The movement of air through the surface of the drum causes relatively iight particles of tobacco from the stream to move upward and collect on the surface of the drum whilst the relatively heavy stem and foreign matter falls down into a collecting bin.
In this type of arrangement, the air inlet comprises a grating consisting of louvres (104) below the suction drum, and the gas turbulence caused by the presence of the grafting lifts some of the product being treated which then has to pass across the face of the grating in order to exit into the collecting bin.
Consequently the grating tends to become blocked.
An alternative type of arrangement is shown in GB patent No. 1,575,175, in which the pneumatically conveyed stream of product to be treated passes into the inlet 10, through a separation zone 14 in which it is directed towards a screen which is flat and slightly angled downwards. On leaving the screen, the material falls into an expansion chamber immediately above an air-lock exit and the gas passes through the screen to the exhaust exit. Since the screen is angled downwardly relative to the product flow, so that the product is in effect scrubbing the screen, blockage of the screen is effectively prevented. However, because the tobacco impacts against the screen, it can become degraded, and accordingly the present invention seeks to provide a separator which reduces the possibility of damage to the product, and also does not suffer from screen blockage.
Accordingly the present invention comprises a separator for pneumatically conveyed particulate material comprising a first curved duct defining a path which is substantilly horizontal at the inlet and then curves downwardly to terminate in a product outlet; the radially inward side of the duct being defined by a correspondingly curved screen having an air outlet on the other side.
Since the inlet is at the top of the apparatus, rather than at the bottom as in the above mentioned U.S. patent No. 3,727,755 the screen does not tend to become blocked by the incoming material, and since this material is directed away from the screen as it enters the apparatus, it is not degraded by impacting against the screen itself.
One embodiment of the invention will now be described by way of example with reference to the accompanying drawings, in which: Figure 1 is a vertical cross-section through an inertial separator according to the invention; Figure 2 is an end elevation, seen in the direction Z of Figure land Figure 3 is a partial horizontal cross-section through the device of Figure 1 taken on the iine w-w.
Referring first to Figure 1, the apparatus comprises a generally curved duct assembiy 10 which is mounted on a discharge air lock device 12, to be described in more detail below.
A pneumatically conveyed stream of tobacco enters the upper end of the curved duct via the inlet 14, and as can be seen from Figure 1, the duct then branches into a radially outward portion 16, and a radially inward portion 18. A curved screen 2 is interposed at the junction of the branch, so that the product entering the inlet 14 is prevented from passing into the exhaust plenum 3. As can be easily appreciated from a consideration of this layout, the stream of tobacco will tend to move outwardly, owing to its inertia, so as to flow round the inside of the outer wall 20 of the duct.
Since air flow out of the base of the device is effectively prevented by an air lock mechanism in the discharge section (to be described in more detail below), the conveying air, and any very light fractions to be separated, whose inertia is of course less, pass through the screen 2 and into the other branch of the duct 18 to the exhaust plenum 3. As will be seen from the drawing, a vane 4 is positioned in the plenum, to optimise the air distribution through the screen.
The base 12 of the device incorporates a rotary air lock of a well known type, comprising a cyiindrical housing 22, with an axially mounted set of radial vanes 24. These are equipped with resilient sealing blades 26 at their ends, and the vane assembly is rotated by means of a chain drive 30 powered by an electric motor 28. An adjustable tensioning device 32 (illustrated diagrammatically by dashed lines in Figure 1) may be incorporated to adjust the tension of the chain 34. In use, the air lock is driven at a suitable speed to enable the flow of tobacco to pass through it to a discharge port 36 in the base of the device, whilst effectively preventing the passage of air through the discharge port.
It will be clearly appreciated from a consideration of the layout of the device, that it avoids two significant problems of the prior art devices, namely the tendency to degrade the product to be separated, and the tendency to screen blockage, since the inertia of the product flow is employed to carry it away from the screen, so that it abuts against a smooth surface rather than a grating type of surface. In addition, since there is no recirculation of gas flow, in contrast to the cyclone type of separator, the time of residence of the product in the apparatus is kept to a minimum, avoiding over drying of the product.

Claims (6)

1 . A separator for pneumatically conveyed particulate material comprising a first curved duct defining a path which is substantially horizontal at the inlet and then curves downwardly to terminate in a product outlet; the radially inward side of the duct being defined by a correspondingly curved screen having an air outlet on the other side.
2. A separator according to claim 3 in which the air outlet comprises a second duct which is also curved and extends alongside and radially inwardly of the first duct, the said screen forming a common wall for the said ducts.
3. A separator according to claim 4 in which the second duct terminates in an outlet which is substantially horizontal so that the air leaves the duct in a direction opposite to the inlet direction.
4. A separator for pneumatically conveyed particulate material, comprising an inlet into which the stream of material is directed tangentially against a downwardly extending, smooth concave surface which terminates in a product discharge duct; and a generally coextensive convex perforated screen, facing the said concave surface, with an air outlet behind the said screen, the arrangement being such that the inertia of the material entering the inlet causes it to move outwardly aiong the concave surface, whilst the air is exhausted through the screen.
5. A separator according to any preceding claim in which said product outlet includes a rotary airlock.
6. An inertial separator substantially as herein described with reference to the accompanying drawings.
GB08626972A 1985-11-12 1986-11-12 Inertial separator Withdrawn GB2183502A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB858527919A GB8527919D0 (en) 1985-11-12 1985-11-12 Inertial separator

Publications (2)

Publication Number Publication Date
GB8626972D0 GB8626972D0 (en) 1986-12-10
GB2183502A true GB2183502A (en) 1987-06-10

Family

ID=10588127

Family Applications (2)

Application Number Title Priority Date Filing Date
GB858527919A Pending GB8527919D0 (en) 1985-11-12 1985-11-12 Inertial separator
GB08626972A Withdrawn GB2183502A (en) 1985-11-12 1986-11-12 Inertial separator

Family Applications Before (1)

Application Number Title Priority Date Filing Date
GB858527919A Pending GB8527919D0 (en) 1985-11-12 1985-11-12 Inertial separator

Country Status (1)

Country Link
GB (2) GB8527919D0 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE29821221U1 (en) * 1998-11-27 2000-03-30 Höcker Polytechnik GmbH, 49176 Hilter Device for separating solids from an air stream
DE19855030A1 (en) * 1998-11-28 2000-05-31 Mann & Hummel Protec Gmbh Conveying device for bulk goods with retention device for coarse fraction
US6510855B1 (en) * 2000-03-03 2003-01-28 Brown & Williamson Tobacco Corporation Tobacco recovery system
WO2006008048A1 (en) 2004-07-15 2006-01-26 Eisenmann Anlagenbau Gmbh & Co. Kg. Particle separator

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB539188A (en) * 1937-12-18 1941-09-01 Erik Torvald Linderoth Improvements in or relating to filters for filtering air or gases
GB662072A (en) * 1948-03-22 1951-11-28 Stork Koninklijke Maschf Improvements in and relating to apparatus for separating dust from gases
GB1124953A (en) * 1964-10-26 1968-08-21 Du Pont Vented pneumatic feeder
GB1247211A (en) * 1969-01-02 1971-09-22 William Boon Material collector assembly for the removal of material from a material-air conveying system

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB539188A (en) * 1937-12-18 1941-09-01 Erik Torvald Linderoth Improvements in or relating to filters for filtering air or gases
GB662072A (en) * 1948-03-22 1951-11-28 Stork Koninklijke Maschf Improvements in and relating to apparatus for separating dust from gases
GB1124953A (en) * 1964-10-26 1968-08-21 Du Pont Vented pneumatic feeder
GB1247211A (en) * 1969-01-02 1971-09-22 William Boon Material collector assembly for the removal of material from a material-air conveying system

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE29821221U1 (en) * 1998-11-27 2000-03-30 Höcker Polytechnik GmbH, 49176 Hilter Device for separating solids from an air stream
DE19855030A1 (en) * 1998-11-28 2000-05-31 Mann & Hummel Protec Gmbh Conveying device for bulk goods with retention device for coarse fraction
US6510855B1 (en) * 2000-03-03 2003-01-28 Brown & Williamson Tobacco Corporation Tobacco recovery system
WO2006008048A1 (en) 2004-07-15 2006-01-26 Eisenmann Anlagenbau Gmbh & Co. Kg. Particle separator
CN1997436B (en) * 2004-07-15 2011-01-26 艾森曼设备有限及两合公司 Particle separator
US8038755B2 (en) 2004-07-15 2011-10-18 Eisenmann Anlagenbau Gmbh & Co. Kg Particle separator

Also Published As

Publication number Publication date
GB8527919D0 (en) 1985-12-18
GB8626972D0 (en) 1986-12-10

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Legal Events

Date Code Title Description
WAP Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1)