U.S. patent number 3,608,716 [Application Number 04/794,000] was granted by the patent office on 1971-09-28 for recirculating pneumatic separator.
This patent grant is currently assigned to Imperial Tobacco Company of Canada Limited. Invention is credited to Lorne A. Rowell, Peter A. Tillich.
United States Patent |
3,608,716 |
Rowell , et al. |
September 28, 1971 |
RECIRCULATING PNEUMATIC SEPARATOR
Abstract
This invention relates to a recirculating pneumatic separator
which is particularly designed for separating threshed tobacco
leaves form the heavier tobacco parts. The lighter tobacco fraction
is carried up by air which is recirculated through the separator
and the heavier tobacco function falls to an endless belt and is
separately conveyed out of the separator. Means is provided for
accurately controlling the air velocity in the separation chamber
and for ensuring complete separation of the tobacco fractions by
means of an air jet impeller.
Inventors: |
Rowell; Lorne A. (Lachine,
Quebec, CA), Tillich; Peter A. (Montreal, Quebec,
CA) |
Assignee: |
Imperial Tobacco Company of Canada
Limited (Montreal, Quebec, CA)
|
Family
ID: |
25161379 |
Appl.
No.: |
04/794,000 |
Filed: |
January 27, 1969 |
Current U.S.
Class: |
209/139.1;
209/153; 209/154 |
Current CPC
Class: |
B07B
4/025 (20130101); A24B 5/10 (20130101) |
Current International
Class: |
A24B
5/00 (20060101); A24B 5/10 (20060101); B07B
4/02 (20060101); B07B 4/00 (20060101); B07b
004/08 () |
Field of
Search: |
;209/133,133T,134,135,138,139,502,140,141,154,143,380,153
;131/146 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Lutter; Frank W.
Assistant Examiner: Hill; Ralph J.
Claims
Obviously many modifications and variations of the invention are
possible in light of the above teachings. What is claimed as new is
desired to be secured by Letters Patent is:
1. A pneumatic separator for separating lighter particles from
heavier particles comprising, a separating chamber, means for
circulating air upwardly through said chamber, inlet impeller means
mounted on one side of said separating chamber for thrusting
particles to be separated into and across the chamber, an air jet
impeller means mounted on the side of said separating chamber
opposite to said inlet impeller means for thrusting the particles
across the chamber in a direction opposite to the direction in
which said inlet impeller means thrusts the particles, means for
separating the lighter particles from the upwardly circulating air
and means for collecting and carrying the heavier particles from
the chamber.
2. A pneumatic separator according to claim 1 and further including
means for recirculating the air from the upper end of the
separating chamber to the lower end thereof and bypass means in the
recirculating air means to cause a portion of the air recirculated
to bypass the separating chamber.
3. A pneumatic separator according to claim 2 and further including
a diffuser disposed adjacent the lower end portion of the
separating chamber for equalizing the velocity of the air across
the separating chamber.
4. A pneumatic separator according to claim 1 wherein the means for
separating the lighter particles from the upwardly circulating air
includes a rotating screen.
5. A pneumatic separator according to claim 1 wherein the means for
separating the lighter particles from the upwardly circulating air
includes a rotating screen and further including means for
recirculating the air from the upper end of the separating chamber
to the lower end thereof and bypass means in the recirculating air
means to cause a portion of the air recirculated to bypass the
separating chamber and pass to the rotating screen.
6. A pneumatic separator according to claim 1 and further including
a diffuser in said separating chamber whereby the upwardly moving
air has a substantially uniform velocity across the separating
chamber.
7. A pneumatic separator according to claim 1 wherein said means
for carrying the heavier particles from the chamber includes an
endless foraminous belt extending across the separating
chamber.
8. A pneumatic separator according to claim 7 wherein said means
for carrying the heavier particles from the chamber further
includes an air conveyor means and a damper in said air conveyor
means for diverting a portion of the air passing therethrough.
9. A pneumatic separator according to claim 8 and further including
a makeup air inlet into the separating chamber to replace the air
diverted from said air conveyor means.
10. A pneumatic separator for separating lighter particles from
heavier particles comprising, a separating chamber, means for
circulating air upwardly through said chamber, inlet impeller means
mounted on one side of said separating chamber for thrusting
particles to be separated into and across the chamber, means for
collecting and carrying the heavier particles from the chamber,
means for recirculating the air from the upper end of the
separating chamber to the lower end thereof, screen means for
separating the lighter particles from the circulating air, a bypass
means in the recirculating air means to supply additional
recirculated air to said screen means to remove lighter particles
from said screen means and means for adjusting the airflow through
said bypass means to vary the velocity of the air circulating
upwardly in the separating chamber.
11. A pneumatic separator according to claim 10 and further
including an air jet impeller means mounted on the side of the
separating chamber opposite to said inlet impeller means for
thrusting the particles to be separated across the chamber in a
direction opposite to the direction in which said inlet impeller
means thrusts the particles.
Description
BACKGROUND OF INVENTION
In our prior U.S. Pat. No. 3,164,548 issued Jan. 5, 1965 there is
disclosed a pneumatic separator which is designed to separate
heavier material from lighter material, such as, for example, the
stems from fragments of tobacco leaves. In this system the material
to be separated is forced into the separation chamber by an
impeller. Outside air is brought into the chamber and passes
upwardly through the chamber carrying with it the lighter fractions
whereas the heavier particles drop downwardly in the chamber and
are discharged through a separate outlet. This system functioned
effectively in separating tobacco stem particles from the finer cut
tobacco leaves. In the preparation of tobacco particles for use
there are a plurality of stages of separation, one of the initial
stages involving the separation of threshed tobacco leaves from the
heavier stems. It has been found that the pneumatic separator
disclosed in our prior patent could not be used efficiently in
these earlier stages of tobacco treatment as the threshed leaves
and stems tended to form entangled balls or mats within the
separator above the outlet screen for the heavier fraction and
these balls prevented efficient separation of the particles and
clogged the outlet passageway.
A further drawback of the separation system disclosed in our prior
patent is the large quantity of air which is continuously required
for operation of the separator. It can be appreciated that in a
plant where a large number of separators may be operating, large
quantities of air are drawn in from the plant, this air being
continuously exhausted to the outside atmosphere. Thus, there was a
clear need for a pneumatic separator wherein a recirculating air
system is provided thereby obviating the need for a continuous
supply of outside air.
SUMMARY OF INVENTION
According to the present invention there is provided a pneumatic
separator in which the air used to effect the separation of the
lighter particle fraction from the heavier particle fraction is
recirculated so that a minimum quantity of outside makeup air is
required.
The presently disclosed pneumatic separator may be used to effect
the separation of threshed tobacco leaves from the heavier stem
particles by reason of the provision of a secondary stage of
separation. The material to be separated is thrust into the
separation chamber by an impeller in a manner similar to that
disclosed in our prior U.S. Pat. No. 3,164,548. However, in the
wall opposite the wall in which the impeller is mounted there is
provided an air jet means which forces the particles apart, thereby
preventing the formation of the entangled balls or mats
characteristic of the system disclosed in our prior patent. The
particles are thrust across the chamber to subject the particles
again to the upflowing air in the separation chamber, thus
effecting a second stage of separation.
The lighter separated particles comprising the threshed tobacco
leaves pass upwardly with the air and there is provided a rotating
air screen through which the conveying air passes to be
recirculated through the separating chamber, with the particles
passing through a separate air lock and out of the pneumatic
separator through an independent air-conveying system. There is
provided an endless foraminous belt extending across the lower end
of the separating chamber and the heavier tobacco particles which
drop down on to the belt are conveyed outwardly through a separate
outlet and carried off by a separate air conveying system.
A bypass air duct is provided in the recirculating air system so
that a portion of the air which would normally be recirculated up
through the main separation chamber may be drawn off and
recirculated to the rotating air screen where the lighter tobacco
particles are separated from the conveying air. This bypass means
in the air-recirculating system performs two functions. It serves
to regulate the air velocity through the separating chamber so that
this velocity may be accurately controlled within close tolerance
and the bypass system also serves to ensure that an adequate supply
of air is provided at the rotating air screen. With an inadequate
supply of air at the air screen the tobacco particles tend to cling
to the air screen thereby clogging the screen and preventing
efficient operation of the system.
In order to obtain efficient distribution of particles across the
entire cross section of the separating chamber it is essential that
the velocity of the air across the chamber be uniform. According to
the present invention there is provided means to ensure uniform air
velocity. Beneath the endless foraminous belt which carries off the
heavier tobacco particles there is provided a diffusion plate which
consists of a series of spaced vanes extending across the
separation chamber. These vanes form a diffuser plate creating an
area of pressure differential. As the air passes upwardly between
the vanes in the diffuser plate the airflow velocity tends to
become more even across the chamber in that as the amount of air
passing through a given area increases, the resistance to flow
increases and a greater amount of air tends to pass through other
areas of the diffuser plate. The air moving upwardly through the
separation chamber must also pass through the lower and upper runs
of the endless foraminous belt and this belt also serves to create
areas of pressure differential and functions to even out the air
velocity across the separation chamber.
Very fine tobacco particles which pass upwardly in the separation
chamber and pass through the rotating air screen will be
recirculated with the recirculating air and will be caught on the
lower surface of the foraminous belt. As the foraminous belt
rotates, these particles will be brought to the upper run of the
belt and the airflow through the belt will again convey these fine
tobacco particles upwardly through the chamber and eventually these
finer particles will pass through the outlet with the lighter
tobacco fraction.
Means is provided for diverting a portion of the air which serves
to convey the heavy particle fraction out of the pneumatic
separator. This diverted air is replaced by a portion of the main
separating air which flows outwardly with the heavier particle
fraction and serves to draw the heavy particle fraction out into
the outlet. Makeup air from the outside atmosphere is drawn into
the separating chamber to replace the main separating air which is
passed out with the heavier particle fraction and it is this makeup
air which provides the air jet impeller creating the secondary
separating stage within the separating chamber.
A primary object of the present invention is to provide a pneumatic
separator with a recirculating air system so that a minimum
quantity of outside air is required for operation of the
separator.
Another object of the present invention is to provide a
recirculating separator which is capable of separating threshed
tobacco leaves from the heavier stem particles by providing an air
jet impeller which creates a secondary separating stage so that the
particles to be separated are passed across the separating chamber
twice.
Still another object of the present invention is to provide a
bypass means in the air-recirculating system so that the air
velocity in the separating chamber can be accurately controlled and
so that efficient operation of the rotating air screen separating
means is ensured.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a perspective view of the recirculating pneumatic
separator,
FIG. 2 is a sectional view through the separator and
FIG. 3 is an end elevational view thereof.
DETAILED DESCRIPTION OF INVENTION
Referring now more specifically to the drawings wherein like
numerals indicate like parts throughout the several views the
recirculating pneumatic separator is housed within a casing
structure 1 and the material to be segregated by the pneumatic
separator is fed into the casing structure through an inlet 2, more
clearly seen in FIG. 2. There is provided a rotary screen 3 with a
mesh of sufficiently fine size that it prevents the material being
brought into the separator from passing therethrough. However, the
conveying air which brings the material into the separator passes
through the screen and out through an open end 4 of the rotary
screen. Thus, the conveying air for the material being fed into the
separator forms a closed circuit, passing into the separator
through the inlet 2 and out through the passageway 4. There is
provided an air lock 5 comprising a plurality of rotating gates
which permit the material to be segregated to pass therethrough but
prevents any substantial quantity of the conveying air from passing
through into the main portion of the pneumatic separator. The
material to be subjected to treatment within the pneumatic
separator passes downwardly where it is engaged by a rotary
impeller 6 and thrust by the vanes of the impeller into the main
chamber 7 of the pneumatic separator. The impeller imparts to the
particles of material to be separated a substantial velocity, for
example, within the range of 1,000 to 1,200 feet per minute. This
prevents the heavier particles from immediately dropping to the
bottom of the chamber and causes the particles to pass across the
chamber and be subjected to the upwardly passing air currents
within the main separating chamber 7. The lighter particle fraction
is carried upwardly by the upwardly moving air currents as shown at
8 whereas the heavier particles fraction passes across the chamber
as shown at 9 and may abut the wall 10 of the chamber which is
opposite the impeller 6. The heavier particles may drop down on to
an endless foraminous belt 11 which is supported by and driven from
end rolls 12 and 13. The heavier particle fraction rests on the
foraminous belt and is carried therealong to the heavier particle
fraction outlet 14. The heavier particles pass out of the pneumatic
separator through the outlet 14 and along the passageway 15 and are
carried therealong by conveying air which forms a separate external
circuit as shown by the arrows 16. The inlet for this heavier
particle fraction conveying system is shown at 17 and the conveying
air passes along the passageway 17 into the chamber 18 where a
portion of the air is drawn off as shown at 19 for a purpose which
will be explained more fully hereinafter. The main portion of the
air coming in through the inlet 17 passes through chamber 18 and
back through the passageway 20 to the heavier particle fraction
inlet 14.
Thus it can be seen that the heavier particle fraction is drawn out
of the pneumatic separator through the outlet 14 by a separate
conveying air which takes this fraction out through passageway 15
where the heavier particle fraction is separated and removed by
means not shown and the conveying air recirculated through the
inlet 17.
The lighter particle fraction passes upwardly through the main
separating chamber 7 with the air currents passing upwardly through
the chamber and through a substantially tangential passageway 21
into a substantially cylindrically shaped chamber 22. Centrally
disposed within the chamber 22 is a cylindrical screen 23 which is
mounted for rotation within the chamber. The screen 23 is of a mesh
size insufficient to permit the passage of the lighter fraction
particles which are carried by the air current but permit the air
to pass therethrough into the central portion 24 and thence
outwardly through the open ends of the rotary screen. Referring to
FIG. 3 it can be seen that the air passing through the rotary
screen 23 and through the open ends of the screen passes into
downwardly extending ducts 25 and 26 and into the outer ends of a
fan casing 27. The fan casing 27 shown in FIG. 2 houses a rotary
fan which draws the air through the ducts 25 and 26 and forces the
air through the fan outlet 28 and back into the lower end portion
of the separating chamber 7. Thus it can be seen there is a
recirculating system for the air used to effect the separation
between the lighter and heavier particle fractions. This
recirculating circuit comprises the main chamber 7, the passageway
21, through the rotary screen 23, outwardly through the open ends
of the screen and downwardly through ducts 25 and 26, through the
open ends of the fan casing 27 and through the fan outlet 28 back
through the lower end of the separating chamber 7.
The lighter particles fraction passes downwardly within the
cylindrical chamber 22 and into an air lock 29, through the air
lock and into the lighter particle fraction passageway 30. The
conveying air for the lighter particle fraction enters on one side
of the casing 1 and exits through a duct 31 (FIG. 1) on the
opposite side of the casing. The conveying air forms a separate
circuit for drawing off the lighter particle fraction and the
lighter particle fraction is collected at a location spaced from
the pneumatic separator. Additional air for this conveying system
may be drawn in through an upwardly extending duct 32 which draws a
portion of the air 19 from the air in the conveying circuit for the
heavier particle fraction. The amount of this air which is drawn
off is determined by the position of a damper 33 located in the
passageway 20 of the conveying circuit for the heavier particle
fraction. The portion of the heavier particle fraction conveying
air which is diverted into the lighter particle fraction conveying
circuit is replaced by a portion of the recirculated air passing
through the main separating chamber 7. The passageway of this air
out through the outlet 14 assists in drawing out the heavier
particle fraction from the end portion of the endless belt 11.
Thus, it can be seen that a portion of the recirculated air within
the chamber 7 is continuously drawn off through the outlet
passageway 14. This drawn off air is made up for by drawing in
outside air through a makeup inlet 34. Air drawn in through this
makeup air inlet passes into the main separating chamber 7 beneath
the lower end portion of wall 10 and below an adjustable deflector
blade 35. The makeup air passing between the adjustable deflector
35 and the upper end of endless belt 11 creates an air jet impeller
which forces the particles of material outwardly across the chamber
7. Referring to applicant's prior U.S. Pat. No. 3,164,548 it was
found that when that pneumatic separator was used to separate
threshed tobacco leaves from the larger stem parts a conglomerate,
ball or mass of material formed at the wall opposite to the inlet
impeller and these particles would not separate satisfactorily,
eventually clogging the heavier particle outlet. The air jet
impeller provides a secondary stage of separation, thereby
preventing the formation of the ball or mass of particles and
insures effective separation of all of the tobacco particles. By
adjusting the position of damper 33 the amount of air to be
diverted up through passageway 32 is determined and this determines
the amount of main chamber air drawn out with the heavier particle
fraction and thus the amount of makeup air drawn in through inlet
34. The position of deflector 35 determines the size of the inlet
through which the makeup air passes into the main chamber 7 and
thus the position of damper 33 and reflector 35 determined the
velocity and size of the air jet impeller creating the secondary
stage of separation.
Adjacent the lower end portion of the main separating chamber 7
there is provided a diffuser 36 comprising a series of angularly
extending spaced vanes which extend across the separating chamber.
The air passing from the circulating fan outlet 28 passes upwardly
through the diffuser and the diffuser performs the function of
insuring an even flow of air up through the main separating chamber
7 with a uniform velocity across the chamber. In effect the
diffuser provides an area of pressure differential and provides for
evening out of the air velocity in that in the event the velocity
in one area increases, the resistance to flow increases and there
will be a greater flow through other portions of the diffuser. The
air passing through the diffuser 36 passes upwardly through the
lower run of endless belt 11 and through the upper run of this
belt. Any very fine tobacco particles which may have passed through
screen 23 and recirculated with the recirculating air will be
caught on the lower run of endless belt 11 and when the lower run
of belt 11 becomes the upper run as the belt rotates, these fine
particles will again be picked up and carried through separating
chamber 7.
There is provided a bypass system for the recirculating air passing
through the chamber 7. This bypass means includes an upwardly
extending bypass duct 37 with an inlet at the lower end adjacent
the outlet 28 from the fan casing 27. The outlet for the bypass
passageway 37 is shown at 38 and this outlet passes air into the
cylindrical chamber 22 housing the rotating separating screen 23.
An adjustable damper 39 disposed within bypass duct 37 controls the
amount of air flowing through this bypass duct. Thus it can be seen
that a portion of the air recirculates from the chamber 22 through
the central portion 24 of the rotary separating screen 23
downwardly through ducts 25 and 26 through the fan casing 27 and
back up to the chamber 22 through the bypass duct 37. The bypass
system shown performs two functions. The primary purpose of the
bypass system is to provide adequate control over the velocity of
the air passing upwardly through the main separating chamber 27.
Accurate control over the velocity of the upwardly passing air is
critical to the successful operation of the system. Obviously, this
velocity will vary depending upon the material to be separated. In
separating threshed tobacco leaves from the heavier stem particles
it is desirable that an air velocity of from 600 to 800 feet per
minute be maintained. With lighter products a lower velocity range
is used. Within the ducts 25 and 26 as shown in FIG. 3 there are
provided boltable gates 40 and 41 which may be moved inwardly and
outwardly of the ducts to set the air velocity range. Thus, with
the gates in their outermost position permitting maximum velocity
through separating chamber 7. This maximum velocity flow may be
decreased by opening the damper 39 to permit some of the
recirculated air to be bypassed. The adjustable damper 39 permits
approximately 30 percent control over the air velocity passing
through the main separating chamber 7.
The bypass air also provides for uniform operation of the screen
separator 23. That is to say, the rotating screening separator 23
operates at a maximum efficiency when sufficient air is passing
over and through the screen. If the air velocity drops to too low a
value the particles of product tend to cling to the screen thereby
blocking the screen and preventing the recirculating air from
passing therethrough and also preventing the particles from passing
through the air lock 29. It is also possible that a brush might be
employed adjacent to the outer surface of the screening separator
23 to remove the lighter particles from the outer surface of the
screen so that these particles can pass to the lower end portion of
the chamber 22 and then out through the air lock 29.
If desired, fluorescent lights may be provided as at 42 and 43 and
a viewing window 44 may be provided so that the separation taking
place within the chamber 7 may be viewed and adjustments made in
the air velocity or the air jet impeller by setting the gates 40,
41 dampers 33 and 39 and deflector 35. The pneumatic separator
disclosed herein provides a recirculating air system utilizing a
minimum of outside makeup air. The bypass system for the
recirculated air permits the velocity of the air passing upwardly
through the main separating chamber 7 to be controlled and maintain
adequate air loading of the separator screen 23. The diffuser plate
36 ensures a uniform velocity of air across the separating chamber
7 and the endless foraminous belt 11 provides a means for removing
the heavier particle fraction and for collecting and recirculating
the finer particles which may pass through the screening separator
23.
The air jet impeller created by the makeup air passing beneath
deflector 35 provides a secondary separation stage which is
essential in separating threshed tobacco leaves from the heavier
stem particles. This air jet impeller thrusts the particles across
the separating chamber in much the same way as the inlet impeller 6
and prevents the formation of balls or mats of conglomerate
particles. The velocity of the air jet impeller may be controlled
by adjusting the damper 33 and deflector 35 in the manner
previously described.
* * * * *