U.S. patent number 3,866,335 [Application Number 05/379,743] was granted by the patent office on 1975-02-18 for gas heated rotary drier.
This patent grant is currently assigned to AMF Incorporated. Invention is credited to Richard E. G. Neville.
United States Patent |
3,866,335 |
Neville |
February 18, 1975 |
GAS HEATED ROTARY DRIER
Abstract
A gas drier for tobacco and the like having a rotatable drum
with internally disposed axially extending V-shaped vanes each open
to the gas burners disposed along the bottom of the drier.
Inventors: |
Neville; Richard E. G.
(Salisbury, EN) |
Assignee: |
AMF Incorporated (White Plains,
NJ)
|
Family
ID: |
10363799 |
Appl.
No.: |
05/379,743 |
Filed: |
July 16, 1973 |
Foreign Application Priority Data
|
|
|
|
|
Jul 21, 1972 [GB] |
|
|
34291/72 |
|
Current U.S.
Class: |
34/602; 34/134;
432/107 |
Current CPC
Class: |
F26B
11/045 (20130101); A24B 3/04 (20130101); F26B
11/0445 (20130101) |
Current International
Class: |
A24B
3/04 (20060101); A24B 3/00 (20060101); F26B
11/00 (20060101); F26B 11/04 (20060101); F26b
011/02 () |
Field of
Search: |
;34/134,133,139
;432/107,112 ;165/89 ;259/89,90 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
Primary Examiner: Sprague; Kenneth W.
Assistant Examiner: Schwartz; Larry I.
Attorney, Agent or Firm: Price; George W. Worth; Charles
J.
Claims
1. A rotary drier for particulate or loose material comprising a
cylinder arranged to rotate about its axis inclined to the
horizontal, said cylinder having formed along its cylindrical
surface a plurality of hollow paddles extending axially along said
cylinder and inwardly thereof, said paddles being V-shaped in cross
section with one side of each paddle being disposed radially and
the other side being disposed obliquely thereto, the interior of
said paddles communicating with the exterior of the cylinder and at
least one gas burner arranged below the cylinder to direct
flame
2. A rotary drier as claimed in claim 1 in which said burner
comprises a plurality of strip burners which are provided
positioned obliquely with
3. A rotary drier as claimed in claim 1 in which said cylinder is
surrounded along its length by a cylindrical wall defining a
combustion space between said cylinder and said wall, the interior
of said paddles communicating with said combustion space, and the
bottom of the combustion
4. A rotary drier as claimed in claim 3 in which the top of the
combustion space includes a tapered flue gas collection manifold
which communicates
5. A rotary drier as claimed in claim 4 further including means for
introducing air into said cylinder, said means comprising a passage
way for conducting ambient air around said cylinder to preheat the
air and for separating the ambient air from combustion gases, a fan
for drawing air through said passage way and ducting for passing
the preheated air to the
6. A rotary drier as claimed in claim 5 further including an inlet
probe for introducing pre-heated air into said cylinder at a
position
7. A rotary drier for particulate or loose material comprising a
cylinder arranged to rotate about its axis inclined to the
horizontal, said cylinder having formed along its cylindrical
surface a plurality of hollow paddles extending axially along said
cylinder and inwardly thereof, the interior of said paddles
communicating with the exterior of the cylinder, at least one gas
burner arranged below the cylinder to direct flame into the
interior of the hollow paddles, said cylinder being surrounded
along its length by a cylindrical wall defining a combustion space
between said cylinder and said wall communicating with the interior
of said paddles and the bottom thereof being open to said burner,
the top of the combustion space including a tapered flue gas
collection manifold which communicates with a flue duct for
removing waste combustion gases, and means for introducing air into
said cylinder, said means comprising a passageway for conducting
ambient air around said cylinder to preheat the air and for
separating the ambient air from combustion gases, a fan for drawing
air through said passageway and ducting for the preheated air to
the interior
8. A rotary drier as claimed in claim 7 further including an inlet
probe for introducing pre-heated air into said cylinder at a
position intermediate its ends.
Description
This invention relates to driers for particulate or loose material
such as rag or stem tobacco.
With the general availability of natural or propane gas, the gas
drier is a relatively inexpensive and attractive alternative to the
steam drier for rag or stem drying. With a low thermal capacity and
rapid response it is particularly suitable for automatic moisture
control.
A known drier traditionally used for stem drying comprises a
rotatably mounted cylinder having radially inwardly extending
paddles. The cylinder is heated by strip type burners arranged
below and parallel to the cylinder axis to throw flame at the
cylinder along its entire length at the same moment. Its short
paddles and high cylinder temperatures suit the low flow/high
moisture removal stem application. The heat conduction along the
paddles is negligible and size is based on the cylinder heating
surface only.
For rag drying, larger paddles are required to match the larger
volume flow. To keep the size and dwell time of the drier
comparable to that of a steam drier for the same working
temperatures (or smaller for higher working temperatures) the
paddles must supply heat to the tobacco.
Conducting paddles are not practicable. Using the best practical
conductor, copper, a 1 inch base triangular section only barely
conducts sufficient heat; combined with an one-half inch cylinder
thickness the thermal capacity of the whole would be totally
unacceptable. The conduction of steel is about eight times worse
and stainless 24 times worse.
According to the invention there is provided a rotary drier for
particulate or loose material comprising a cylinder arranged to
rotate about its axis disposed horizontally or inclined to the
horizontal and having formed along its cylindrical surface a
plurality of hollow paddles extending axially along said cylinder
and inwardly thereof. The interior of said paddles communicate with
the exterior of the cylinder and at least one gas burner arranged
below the cylinder to direct flame into the interior of the hollow
paddles.
In the present drier the paddles are heated directly by gas flame,
giving the maximum heat transfer and ensuring a high thermal
efficiency. The paddles are preferably of a V-shape or hollow
triangular sections each with an open base exposed to the
combustion space. If strip burners parallel to the cylinder axis
are used there would be no room for the cooled gases in he paddle
to escape, which would consequently prevent the flame entering the
hollow paddle. The present construction avoids this problem by, in
effect, dividing the normal strip type burner into short lengths
which are inclined to the cylinder axis. Accordingly, at any one
moment the flame only enters the paddle at the intersections of the
open paddle base and the inclined burners. This arrangement allows
the flame to enter the hollow paddle by leaving space either side
of the scouring out of cooled gases, and insures uniform heating of
the cylinder throughout its length.
Further features of the present invention are cylinder temperature
control by cylinder expansion measurement, or differential or zonal
cylinder temperature control by thermistor, and combined casing
cooler and air pre-heater.
The foregoing and other objects and advantages will appear more
fully hereinafter from a consideration of the detailed description
which follows, taken together with the accompanying drawings
wherein several embodiments of the invention are illustrated by way
of example. It is to be expressly understood, however, that the
drawings are for illustration purposes only and are not to be
construed as defining the limits of the invention.
FIG. 1 is a side view of the rotary drier,
FIG. 2 is a view of the drier at the feed end thereof,
FIG. 3 is a view on the delivery end of the drier
FIG. 4 is a section taken along the line 4--4 in FIG. 1,
FIG. 5 is a plan view of the burners taken in the direction of the
arrows 5--5 in FIG. 1,
FIG. 6 is a scrap view of an expansion follower for temperature
measurement, and
FIG. 7 is a side view of a rotary drier which includes an air inlet
probe for suppressing exhaust air ventilation.
Referring now to the drawings, a drier in accordance with the
invention is provided with a chasis 10 comprising longitudinal side
channels 11 supported on legs 12 and having cross channels 13. On
the cross channels 13 are mounted pairs of support rollers 14,
preferably of a reinforced phenolic resin which carry a cylinder 15
by way of track rings 16 and 17 attached by spacers. The cylinder
15 is driven by belts 18 passing around a belt ring, formed as part
of the track ring 16, and driven by a geared motor 19 or the like.
The cylinder has its axis of rotation disposed at an angle of
13/4.degree. or 31/2.degree. according to the desired flow rate and
drying capacity. Generally, the inclination is preferably between
1.degree. and 5.degree.. A thrust roller 20 is mounted on the cross
channel 13 at the feed end for engagement with a rim 21 provided on
the cylinder 15. A feed conveyor 47 which may be of the vibratory
type is provided at one end of the drier with a discharge chute 55
being provided at the other end.
As is seen from FIG. 4, the cylinder 15 is formed with a series of
inwardly projecting paddles 24 which are generally V-shaped or of
an open base triangular cross section all extending axially off the
cylinder. One side of each paddle 24 is positioned radially and the
other obliquely relative to the rotation axis of the cylinder 15.
This is to insure that the radial sides of paddles 24 which when
the cylinder 15 rotates clockwise or in the direction shown by the
arrow will carry the tobacco up to the top of the cylinder and the
enlarged opening will provide maximum exposure to the combustion
space to a greater extent than the oblique side.
BURNER EQUIPMENT
Normally forced draught ribbon type gas burners are fitted, with
pilot burners, flame failure control and pneumatically operated
modulating valve giving a 20:1 turn down range. The burner assembly
(see FIG. 5) is pivotably mounted on an axis adjacent and parallel
to a chassis side member so that it can be swung down for access to
the burners. Heating by diagonal strip burners has the following
advantages compared with other known methods, viz.
1. It is simple and avoids the use of a fan found in other driers
which has to handle very hot gasses,
2. The cylinder and especially its open paddles can be uniformly
heated from end to end, or
3. The cylinder and especially its open paddles can be heated
differentially to reduce the overdried tobacco at start-up and
shut-down and to give quick response control during normal
running,
4. Direct flame exposure of the open paddles gives a more efficient
heat transfer from gas to cylinder.
The hot combustion gases are kept in close proximity to the
cylinder by a cylindrical combustion space casing 27, (see FIG. 4)
which is concentric with the cylinder 15 and surrounds it at a few
inches distance. The bottom of the casing 27 is open for the
burners 28 and the top includes a tapered flue gas collection
manifold 29 which connects to a flue duct 30.
A few inches outside the combustion space casing 27 are two further
concentric curved sheets 31 and 32, one on each side of the
cylinder 15, forming a narrow curved air passage way. The passage
way finishes either side of the flue manifold where a thin slot 33
connects with the corner space 35 formed by the outer insulation
boards 34.
Both corner spaces 35 are connected to a fan 36 (see FIG. 1) which
enables air to be drawn up through the curved passage way, heated
and delivered to the cylinder via a ducting 37. Ambient air is
drawn in through an adjustable entry 39. This method of pre-heating
the cylinder drying air has the double purpose of improving the
overall thermal efficiency of the drier and considerably reducing
the heat conducted to the outer insulation. As a result the outside
surface of the insulation is below 100.degree.F. and typically only
20.degree.F. above ambient. The outer casing is of conventional
asbestos board construction.
Alternatively, where pre-heating of the drying air is not required,
the corner spaces are connected to the combustion gas flue 29 and a
flow of casing cooling air induced by convection.
EXHAUST AIR
For high duty application the drying air is contra flow and the
cylinder is provided with a cylindrical feed end sieve 40 as an
extension of the cylinder 15, and a sieve cleaner 41. Contra flow
is essential for applications with high input moisture content
where the exhaust air is saturated. Additional air is fed via fan
inlet 57 to the feed hood from a pre-heater in such applications to
prevent condensation.
For lesser duties a lower volume air flow is used without a
sieve.
______________________________________ Proposed Range of sizes
______________________________________ Cylinder diameter in feet 3
4 6 Number of paddles 4 8 16 cylinder rotational 21 18 15 speed in
r.p.m. Maximum rag flow rate at: 31/2.degree. cylinder inclination
in lb/hr 5,000 10,000 20,000 13/4.degree. cylinder inclination in
lb/hr 2,500 5,000 10,000 Heated cylinder lengths in feet: 8 12 12
16 16 16 20 20 24 ______________________________________
The volume of the hollow paddle is sufficient to contain a high
proportion of the hot products of combustion which continue to
condut to the paddles 24 while they are rotated to the top of the
cylinder 15. The flame jets also can be inclined to the vertical so
that they are directed toward the working radial surfaces of the
paddles 24.
This direct heating of the paddles 24 permits a thin cylinder and
paddle wall to be used, giving a lower thermal capacity than the
corresponding size of steam drier. Typical heating and cooling
rates for a one-eighth inch thick cylinder being 50.degree.F/min
under normal working conditions. At 15 r.p.m. this is a fluctuation
of only 31/3.degree.F per revolution.
CYLINDER TEMPERATURE CONTROL
The traditional gas control from the cylinder exhaust air
temperature is not satisfactory for use with automatic moisture
control system or for good manual control. The exhaust air
temperature is only a poor reflection of the cylinder temperature
as it is effected by exhaust air flow, tobacco temperature and
moisture removal and it furthermore lags behind the cylinder
temperature.
For manual control and the simpler automatic control systems, the
gas drier of the present invention is fitted with average cylinder
temperature control by measurement of cylinder expansion using
followers 42 (see FIG. 6) on one but preferably on both runner
track rings 16 (not shown) and 17. The position of a follower 42 is
converted by a transducer 43 into an electric signal and the
difference between the signals from the transducers 43, after
smoothing, gives a measure of cylinder expansion and hence cylinder
temperature.
The resulting signal is fed to a temperature indicating process
controller (not shown) which controls a modulating valve 44 in the
gas supply to maintain a set temperature. With automatic moisture
control the set point of the temperature is adjusted automatically
by cascade control.
THE CYLINDER TEMPERATURE IS SET MANUALLY
The virtually instantaneous reaction to cylinder temperature
results in a very tight control of cylinder temperature. The
burners are sized to give double the normal working heat. This,
combined with the low thermal capacity of the cylinder, enables the
cylinder temperature to be increased or reduced rapidly and
accurately within the normal working range of 150.degree.to
400.degree.F.
An over-riding safety control is fitted based on the conventional
exhaust air temperature measurement.
ZONAL CYLINDER TEMPERATURE CONTROL
For applications with fully automatic feed forward and feed back
control from moisture meters with automatic start-up and shut down
the burner 28 is divided into two or more sections (see FIG. 5)
depending on the length of the drier. Each section has an
independent gas control valve (not shown).
The temperature of each zone of the drier corresponding to each
burner section is measured by a number of thermistors 56 (of which
only one is shown in FIG. 1) fixed to the cylinder surface and
connected in parallel to give an average temperature for each zone.
This replaces the overall cylinder expansion measurement used for
manual and simpler automatic control systems.
One side of each thermistor is connected to the cylinder and
connection is made to the rotating cylinder by a sprung metal
roller on the track ring.
The other connection from the thermistors in each zone is brought
to a slip ring mounted on an insulated extension of the track ring.
Thermistors are used for the temperature measurement as their very
high resistance change with temperature makes them insensitive to
variation in slip ring resistance. Instead of arranging slip rings
on the outside of the cylinder the connections may extend to one
end of the cylinder where longitudinally extending arms are
provided with a connected arm diametrically positioned, at the
centre of which arm is mounted a slip ring of considerably less
diameter than that of the cylinder. Since a small diameter slip
ring can be used in such a construction a proprietory slip ring and
brush enclosed in a dustproof housing can be used.
A separate temperature controller for each zone enables the
temperature of each zone to be controlled independently of its
neighbor. This zonal or differental temperature control is used at
start up and shut down and also during normal running.
At start up as the tobacco runs in from the infeed 47 to the
discharge 55, the down stream zones are heated up successively
after the upstream zones using a programmed start. Similarly at
shut down as the tobacco runs out the upstream zones are turned off
successively before the down stream zones. This avoids over-dried
tobacco during run-in and run-out.
During normal working the feed end zone only is used to control
short term variations in output moisture control and the delivery
end zone is correct short term output variations in mositure
content. This is achieved by a system of duel control which ensures
that short term fluctuations are corrected by the appropriate end
zones and long term variations are corrected by the general
temperature level of all zones.
This arrangement of zonal cylinder temperature control enables
quick response corrections to be made which are not possible with a
cylinder of a uniform temperature throughout its length. The
Paddles are divided between zones to allow for any differential
expansion.
To improve the ability of the tobacco to fill cigarettes using a
minimum amount of tobacco, it is often required to `stew` the
tobacco in the drier, i.e., suppress the exhaust air ventilation
and raise the tobacco to around 170.degree.F. The heat for drying
is supplied by the drier and though the majority of the moisture
removal still takes place in the drier, a greater proportion is
removed in the cooler by evaporative cooling.
A weakness of this method of operation is the uneven moisture loss
that can occur at this high temperature both between the drier and
cooler and in the cooler. To overcome this there is provided a
pre-heated air inlet probe 45 as shown in FIG. 7.
This probe 45 is introduced at the delivery end of the drier and
discharges air via an air diffuser 46 about one-third of the heat
length from the delivery end. The feed-end of the cylinder is
carefully sealed and the tunnel of the vibrating feed conveyor 47
is sealed by a succession of curtain seals (not shown). A small
controlled amount of air (approximately 250 c.f.m. in a 4 ft.
diameter drier) is exhausted from the feed hood. Adjustment of this
air flow determines the temperature achieved by the tobacco in the
first two-thirds of the cylinder heated length. The tobacco
temperature at this point is sensed by a thermistor 48 attached to
the end of the probe and so arranged that it is always covered with
a fresh fall of tobacco.
The majority of the air (approximately 1,250 c.f.m. in a 4 ft.
diameter drier) is exhausted from the deliver end hood so that the
ventilation which takes place in the last one-third of the cylinder
heated length cools the tobacco to normal drier outlet temperature
of around 100.degree./120.degree.F.
The air inlet probe 45 is cantilevered from the delivery end and
arranged to rotate to keep it clear of falling tobacco. The probe
is rotated through a shaft 49 driven by a motor 50. The hot air
from the curved air space and the slots 33 is fed to the probe by a
fan 51 and ducting 52. Ambient air enters through an adjustable
entry 53. The thermistor connections are brought out via a small
slip ring (not shown). The air diffuser has sufficient pressure
drop across it to prevent tobacco settling on it.
The drying capacity of the first two-thirds of the drier length is
reduced due to the suppressed ventilation. In a 4' dia. .times. 16'
heated length cylinder of the kind (shown in FIG. 7) up to 5
percent moisture from 5,000 lbs/hr. of rag can be removed. This
removal figure includes the removal in the cooler, the heat for
which is supplied in the drier.
Although several embodiments of the invention have been illustrated
and described in detail, it is to be expressly understood that the
invention is not limited thereto. Various changes may be made in
the design and arrangement of the parts without departing from the
spirit and scope of the invention as the same will now be
understood by those skilled in the art.
* * * * *