GB2102307A - Separator for precipitating particulate from an airflow - Google Patents
Separator for precipitating particulate from an airflow Download PDFInfo
- Publication number
- GB2102307A GB2102307A GB08122723A GB8122723A GB2102307A GB 2102307 A GB2102307 A GB 2102307A GB 08122723 A GB08122723 A GB 08122723A GB 8122723 A GB8122723 A GB 8122723A GB 2102307 A GB2102307 A GB 2102307A
- Authority
- GB
- United Kingdom
- Prior art keywords
- airflow
- chamber
- separator
- wall
- movable wall
- 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.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B7/00—Selective separation of solid materials carried by, or dispersed in, gas currents
- B07B7/02—Selective separation of solid materials carried by, or dispersed in, gas currents by reversal of direction of flow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B11/00—Arrangement of accessories in apparatus for separating solids from solids using gas currents
- B07B11/04—Control arrangements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B7/00—Selective separation of solid materials carried by, or dispersed in, gas currents
- B07B7/01—Selective separation of solid materials carried by, or dispersed in, gas currents using gravity
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B7/00—Selective separation of solid materials carried by, or dispersed in, gas currents
- B07B7/04—Selective separation of solid materials carried by, or dispersed in, gas currents by impingement against baffle separators
Landscapes
- Combined Means For Separation Of Solids (AREA)
Abstract
A separator for use in a pneumatic conveyor system has a fixed wall structure (2, 3, 4) and a movable wall (12, 12A) jointly defining a chamber (11) of greater cross section than a conduit (10) supplying a particulate carrying airflow to the chamber. Decreased airflow velocity and impingement of the air flow against the movable wall occuring in the chamber permits precipitation of heavier and/or oversize particles from the airflow. <IMAGE>
Description
SPECIFICATION
Separator for precipitating particulate from an airflow
The present invention relates generaily to a separator for removing particulate from an airflow carrying particles of different densities and more specifically to a separator accomplishing separation by a sudden change in airflow velocity and thereafter an upward, slowed flow through an enlarged separator chamber.
In the manufacture of various wood products such as plywood, dimensioned lumber, etc., the products are subjected to sanding or the like to provide the desired surface thereon. Provision is normally made in the manufacturing facility for the automatic and continuous removal of the resulting sander dust and other residue from such operations. Commonly, pneumatic conveyor systems are used to transfer the dust and other particulate to a remote collection point.
In the interest of better utilization of wood resources, such dust is commonly reclaimed and used as a constituent of other manufactured wood products. Undesirably, some abrasive particles such as those dislodged from a sander belt also become mixed with the dust and become part of the later manufactured wood product.
Subsequently, the amount of abradant particles in the manufactured wood product constitutes a significant factor in the wear of machinery and tools performing various operations on the wood product.
The minute, abrasive particles have a cumulative effect on saws, planer, sanders, etc., with resulting excessive wear and replacement of such equipment adding to product manufacturing costs over a period of time.
Also undesired in the reclaimed wood material are oversize wood particles or rejects which alter the desired homogeneous constituency of the finished product.
The present invention is embodied in a separator for use in a pneumatic conveyor system for removing particles, such as abradants or oversize woof particle rejects from an airstream carrying particles of different densities and/or aerodynamic characteristics.
A walled structure includes fixed walls with which a movable wall member jointly defines a variable size chamber into which an airflow is discharged. The chamber is of greater cross sectional area than a communicating inlet duct.
Impingement of the airflow against the chamber structure and reduced airflow velocity in the structure may be regulated so as to affect the precipitation of heavier particles, such as abradants or oversize wood particle rejects for collection within a hopper or the like. The movable wall member is positionable by adjustment means which may be a scissor linkage. An outlet duct receives chamber airflow for routing to additional particle collection means.
The present invention is embodied within a separator for the removal of particulate from an airflow carrying different density particles with the separator having fixed wall structure including contiguous walls partially defining an upright chamber through which the airflow passes, airflow inlet and outlet means in direct communication with said chamber, means inducing an airflow through said inlet and outlet means and said chamber, collector means disposed below said fixed wall structure, movable wall means disposed upright within said fixed wall structure and additionally defining said chamber, said movable wall means at all times offset from and extending substantially parallel to an opposed wall of the fixed wall structure, said inlet means being an air duct located normal to and offset from said movable wall means and discharging the airflow in a direction so as to cause impingement of the airflow against said wall means to initiate particle separation from the airflow and adjustable means coupled to said wall means enabling positioning and retaining same relative the oppositeiy disposed wall so as to permit altering the cross sectional area of said chamber and hence the velocity of the airflow passing upwardly therethrough to thereby control the precipitation of heavier density particulate from the chamber airflow.
In the accompanying drawings:
Figure lisa side elevational view of the present separator; and
Figure 2 is a horizontal sectional view taken downwardly along line 2-2 of Figure 1.
With continuing attention to the drawings, the reference numeral 1 indicates generally a box-like fixed wall structure including walls 2, 3, 4, and 5 joined at their common edges. Corner mounted legs are at 8. The lower end of walled structure 1 is closed by a later described collector.
An inlet 10 normally carries a sub-atmospheric pressure airflow as, for example, induced by a blower B (shown schematically) both of which may be part of a pneumatic conveyor system.
Such conveyor systems are used to collect and convey various mixed types of particulate which, in a wood products manufacturing plant, primarily consists of fine wood dust. Conveyed along with the dust, as earlier noted, are dislodged abrading particles usually of a mineral nature and of heavier density than the wood dust.
Inlet means 10 discharges the airflow so as to move along a projected axis A into a chamber 11 and impinge against movable wall means at 12. A flared duct segment 1 OA disperses the airflow across the width of the movable wall means. Said wall means desirably includes an inclined segment at 1 2A swingably mounted at 1 3 and weighted at 14 for rested, sealing engagement with wall means 12. Along the side edges of wall means 12 are neoprene seals as at 1 6.
Outlet means at 1 5 receives an upward airflow from the upper portion of chamber 11 and may direct same to blower B and to a second particle separator such as one of the cyclone type as shown schematically, a filter collector device or another one of the present type separator.
With attention again to movable wall means 12, the same is positionable in a substantially parallel manner relative to opposite separator wall 4 to enable varying of the cross sectional area of chamber 11.
Upper and lower pairs of guide bars at 1 7 slidably support guides 18, the latter integral with wall means 12 to enable forward advancement of same toward wall 4 or, conversely, rearward retraction toward the left hand side of the separator as shown in Figure 1.
Adjustment means acts on wall means 12 and may be, for example, of the scissors type including upper and lower pairs of scissor linkages at 20 and 21 controlled by a screwshaft 22 and an operator actuated hand wheel 23.
Disposed below upright chamber 11 is a collector 1 9 which is embodied in a hopper type structure having inclined walls defining a discharge opening at their lower extremities, said opening normally closed by movably mounted plates 24 which permit periodic emptying of the collector. A latch mechanism 25 retains the plates in upward abutment with the hopper wall.
Obviously, other types of collector arrangement may be utilized to receive precipitated particulate
P from chamber 11.
In operation, the sub-atmospheric pressure airflow within duct 10 is discharged into the lower portion of chamber 11 so as to impinge against and across movable wall means 12 resulting in a turbulent area within the lower portion of the chamber. The axis A of the inlet airflow is substantially normal or perpendicular to wall means 12 resulting in wall impingement of the airflow and some particle separation from the airflow. Subsequent passage of the airflow is upwardly through chamber 11 at a reduced velocity (relative to duct velocity) during which passage particle precipitation occurs with higher density particles gravitating into the collector.
Positioning of wall member 12 so as to decrease the cross sectional area of chamber 11 will increase chamber velocity resulting in less
particle precipitation. To enable precise control of chamber velocity, pressure gauges at 26-27 read respectively duct and chamber pressures while a window at 28 provides for operator surveillance of separator operation and wall member positioning.
Claims (6)
1. A separator for the removal of particulate from an airflow carrying different density particles comprising, a fixed wall structure including contiguous walls partially defining an upright chamber through which the airflow passes, airflow inlet and outlet means in direct communication with the chamber, means inducing an airflow through the inlet and outlet means and the chamber, a collector disposed below the fixed wall structure, an upright movable wall disposed within the fixed wall structure and additionally defining the chamber, the movable wall at all times being offset from and extending substantially parallel to an opposed wall of the fixed wall structure, the inlet means being an air duct located normal to an offset from the movable wall and discharging the airflow in a direction so as to cause impingement of the airflow against the moveable wall to initiate particle separation from the airflow and adjustable means coupled to the movable wall enabling positioning and retaining it relative the oppositely disposed wall so as to permit altering the crosssectional area of the chamber and hence the velocity of the airflow passing upwardly therethrough to control the precipitation of heavier density particulate from the chamber airflow.
2. A separator as claimed in claim 1, in which the inlet and outlet means convey airflows moving along perpendicularly oriented vectors.
3. A separator as claimed in claim 1 or 2, in which pressure gauges are in communication with the interior of a duct and with the chamber and indicate a pressure differential during separator operation.
4. A separator as claimed in claim 1, 2 or 3, in which the movable wall includes a swingable inclined segment terminating upwardly at the airflow outlet means.
5. A separator as claimed in any of claims 1 to 4, in which the movable wall includes seals coacting with the fixed wall structure.
6. A separator substantially as herein described with reference to and as illustrated in the accompanying drawings.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB08122723A GB2102307B (en) | 1981-07-23 | 1981-07-23 | Separator for precipitating particulate from an airflow |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB08122723A GB2102307B (en) | 1981-07-23 | 1981-07-23 | Separator for precipitating particulate from an airflow |
Publications (2)
Publication Number | Publication Date |
---|---|
GB2102307A true GB2102307A (en) | 1983-02-02 |
GB2102307B GB2102307B (en) | 1985-08-14 |
Family
ID=10523438
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB08122723A Expired GB2102307B (en) | 1981-07-23 | 1981-07-23 | Separator for precipitating particulate from an airflow |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB2102307B (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1987000454A1 (en) * | 1985-07-24 | 1987-01-29 | Magyar Aluminiumipari Tröszt | Apparatus for sizing grains between 20 and 300 microns |
CN118002477A (en) * | 2024-03-12 | 2024-05-10 | 河北悦欣新型建材制造有限公司 | Sedimentation type classifier |
-
1981
- 1981-07-23 GB GB08122723A patent/GB2102307B/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1987000454A1 (en) * | 1985-07-24 | 1987-01-29 | Magyar Aluminiumipari Tröszt | Apparatus for sizing grains between 20 and 300 microns |
CN118002477A (en) * | 2024-03-12 | 2024-05-10 | 河北悦欣新型建材制造有限公司 | Sedimentation type classifier |
Also Published As
Publication number | Publication date |
---|---|
GB2102307B (en) | 1985-08-14 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PCNP | Patent ceased through non-payment of renewal fee |
Effective date: 19920723 |