U.S. patent number 3,561,351 [Application Number 04/734,925] was granted by the patent office on 1971-02-09 for method for feeding material to a mechanical press.
This patent grant is currently assigned to The French Oil Mill Machinery Company. Invention is credited to Alfred W. French, Forest J. Starrett, Jr..
United States Patent |
3,561,351 |
French , et al. |
February 9, 1971 |
**Please see images for:
( Certificate of Correction ) ** |
METHOD FOR FEEDING MATERIAL TO A MECHANICAL PRESS
Abstract
A bed of sugar cane bagasse of substantially uniform thickness
is formed on an endless conveyor and is fed into one or more
mechanical presses for removing liquid from the bagasse, and the
expressed liquid is filtered by directing it through the bed of
bagasse supplied to the press.
Inventors: |
French; Alfred W. (Piqua,
OH), Starrett, Jr.; Forest J. (Piqua, OH) |
Assignee: |
The French Oil Mill Machinery
Company (Piqua, OH)
|
Family
ID: |
24953611 |
Appl.
No.: |
04/734,925 |
Filed: |
June 6, 1968 |
Current U.S.
Class: |
100/37; 100/74;
100/92; 100/130; 198/550.4 |
Current CPC
Class: |
B30B
9/127 (20130101) |
Current International
Class: |
B30B
9/12 (20060101); B30b 009/02 (); B30b 013/00 () |
Field of
Search: |
;100/37,38,73,74,75,92,93,117,118,130,131 ;198/52,53,54,66,57,58
;214/(Inquired) |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Feldman; Peter
Claims
We claim:
1. A method of processing sugar can material, comprising the steps
of collecting batches of the sugar cane material within a hopper
having an inclined bottom wall, conveying a portion of the sugar
cane material upwardly adjacent said wall with an endless conveyor,
forming the sugar cane material being conveyed upwardly by said
conveyor into a bed of substantially uniform thickness by retaining
within said hopper the sugar cane material above a predetermined
distance from said conveyor, and feeding the bed of sugar cane
material from said conveyor into a mechanical screw press for
expressing juice from the material with minimum fluctuation of
pressure within the press.
2. A method as defined in claim 1 including the step of heating the
sugar cane material within said hopper by directing a flow of hot
fluid upwardly into the material being conveyed upwardly by said
conveyor.
3. A method as defined in claim 1 including the step of directing a
flow of liquid through the bed of sugar cane material prior to
feeding the bed of material into the screw press.
4. A method as defined in claim 1 including the step of
simultaneously conveying a second portion of the sugar cane
material within said hopper upwardly adjacent another inclined
bottom wall of said hopper by another endless conveyor, forming the
second portion of sugar cane material into a second bed of
substantially uniform thickness, and feeding the second bed of
sugar cane material into a second mechanical screw press.
Description
BACKGROUND OF THE INVENTION
When sugar cane bagasse is fed in an interrupted or irregular
manner into a mechanical screw press such as disclosed in U.S. Pat.
No. 3,086,452 assigned to the assignee of the present invention,
both the power required by the press and the internal pressure
within the press fluctuates accordingly. This results in discharge
of the material having a wide variation in moisture content as the
amount of moisture expressed from the material is directly related
to the expressing pressure within the press. The irregular feeding
also causes inefficient power fluctuation in the press drive.
It is also common for the juices or liquid discharged from the
press to contain small foreign particles or "fines," and thus
usually it is necessary to subject the liquid to a straining
operation for removing the fines. For example, the liquid may be
filtered through a fine mesh endless screen which moves across the
top of a collecting tank or the liquid may be directed through a
rotary driven screening device.
SUMMARY OF THE INVENTION
The present invention is directed to improved method for feeding
fibrous material such as sugar cane bagasse to one or more
mechanical presses capable of continuous operation such as a
mechanical screw press or disc press. The apparatus is especially
suited for receiving the material in irregular surges and to
distribute or supply the material at a uniform rate to a single
press or a series of presses and thereby minimize fluctuations in
power required by each press in addition to minimizing wear on the
press bearings and other components. The invention also provides a
simplified method for filtering or clarifying the juice or liquid
expressed from each press.
According to one embodiment of the invention, the sugar can bagasse
which is discharged in surges from a diffuser is collected within a
hopper having an inclined bottom wall. An endless drag conveyor has
an upper reach supported by the inclined wall and is arranged to
convey the material from the hopper to the inlet of a mechanical
screw press. A rotary kicker member is positioned within the hopper
and spaced above the inclined wall and cooperates with the endless
conveyor to form a material supply bed of substantially uniform
thickness. The liquid expressed from the material within the
mechanical press is directed through the material supply bed which
serves as a filter to remove the fines and other foreign
particles.
In accordance with another embodiment of the invention, the bagasse
which is discharged from the diffuser is collected within a chamber
from which extends an endless drag slat conveyor having a
distribution reach and a return reach. A rotary kicker is mounted
within the chamber to form the material into a uniform supply bed
or the distribution reach for delivery to one or more mechanical
presses. Any excess material remaining in the distribution reach
after supplying the presses is returned by the return reach to the
collecting chamber. As in the first embodiment, the liquid
discharged from each press is directed through the material supply
bed for filtering and clarifying the liquid. Furthermore, in each
embodiment, provision is made for introducing steam or other hot
fluid into the material for macerating and heating the same.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is an elevational view partly in section of a press feeding
apparatus constructed in accordance with the invention;
FIG. 2 is a plan view of the apparatus shown in FIG. 1;
FIG. 3 is an enlarged fragmentary section of the apparatus shown in
FIg. 1;
FIG. 4 is a fragmentary vertical section of a modified form of the
apparatus;
FIG. 5 is a fragmentary plan view of the apparatus as taken
generally along the line 5-5 of FIG. 4;
FIG. 6 is an elevational view in part section of apparatus
constructed in accordance with another embodiment of the invention
and illustrating somewhat schematically an installation of the
apparatus for feeding a series of presses;
FIG. 7 is a section of the apparatus taken generally along the line
7-7 of FIG. 6;
FIG. 8 is a section of the apparatus taken generally along the line
8-8 of FIG. 6; and
FIG. 9 is a fragmentary section showing a modification of the
apparatus shown in FIG. 7.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
Referring to the drawings which illustrate preferred embodiments of
the present invention, the apparatus shown in FIGS. 1--3 generally
includes a hopper 10 supported by base members 11 and adapted to
receive surges of material such as sugar cane bagasse B discharge
from a diffuser or a roll mill. The hopper 10 is preferably
constructed with a pair of generally triangular-shaped vertical
sidewalls 15 connected by sloping bottom walls 16 and 17 to define
a receiving chamber 18 having a V-shaped configuration. The
sidewalls 15 include upwardly extending portions 19 which are
connected by the bottom wall 17 to form an extension of the hopper
10.
Mounted on the bottom of the hopper 10 is a manifold 20 (FIG. 3)
having a drain outlet 21 which receives liquid through a part
cylindrical bottom plate 23 having a series of small drain holes 24
defining a screen. The holes 24 provide for drainage of liquid from
the bagasse B contained within the chamber 18.
Mounted within the chamber 18 adjacent the bottom wall 17 is an
endless conveyor 25 which includes a pair of parallel-spaced
endless chains 27 (FIG. 3) directed around corresponding sprockets
29 mounted on shafts 30. The shafts are rotatably supported by
bearings 32 (FIG. 2) mounted at the bottom of the sidewalls 15 and
on the upper end portion of the extending wall portions 19. The
endless conveyor 25 includes a series of uniformly spaced drag
slats or members 33 which are mounted on the chains 27 and extend
laterally across the hopper 10. The lower reach of the conveyor is
supported by the bottom wall 17 of the hopper 10 while the upper
distribution reach is supported by an inclined wall member or plate
35 extending parallel to the bottom wall 17.
Mounted within the upper portion of the hopper 10 are a pair of
rotary kicker members 38 each including a series of spike members
39 extending radially from a shaft 40 which is positioned parallel
to the plate 35 and extends between the vertical sidewalls 15.
Covering the upper end portion of the conveyor 25 and the uppermost
rotary kicker member 38 is a housing 42 which is mounted on the
sidewall portions 19 and cooperates with the bottom wall 17 to
define a discharge outlet 43. A chute 45 extends downwardly from
the outlet 43 to the inlet 46 of the mechanical screw press 50.
While a mechanical screw press is shown for purposes of
illustrating a press, it is to be understood that the apparatus of
the invention may be used for feeding material to other types of
extraction presses or mills.
A series of conduit members 52 are mounted on the underneath
surface of the plate 35 and define corresponding chambers 53 which
are connected to steam supply lines 54. Perforations 55 are formed
within the plate 35 and open into the chamber 53 so that the
bagasse B or other material may be heated by steam or other hot
fluid to increase the temperature of the material before feeding
the material into the press 50. A housing 58 is mounted on the
cover member 42 and is provided with an inlet 59. Openings 60 are
formed within the cover 42 under the housing 58 and similar
openings 61 are formed within the plate 35 generally across from
the openings 60 and open into a chamber 62 defined by a housing 63
mounted on the underneath surface of the plate 35. The chamber 62
is provided with a drain outlet 64.
A motor driven variable speed drive unit 65 (FIG. 2) supported by a
frame 66 drives the endless chain conveyor 25 through a chain drive
68 connected to the upper conveyor shaft 30. The unit 65 also
drives the rotary kicker members 38 through a chain drive 69 (FIG.
2) connected to the upper shaft 45 and a chain drive 71 connecting
the lower shaft 45 to the upper shaft 45.
To illustrate the operation of the apparatus shown in FIGS. 1--3, a
portion of the bagasse B which is collected and heated within
hopper 10 is dragged upwardly on the plate 35 by the drag members
33 of the endless conveyor 25. Since the bagasse tends to cling
together as it moves upwardly on the conveyor 25, the rotary kicker
members 42 are so positioned to engage the bagasse above a
predetermined distance from the plate 35 and thereby produce a
moving bed or mat of bagasse having a substantially uniform
thickness. This uniform bed or mat of bagasse is conveyed upwardly
around the upper shaft 30 and is discharged downwardly through the
chute 45 to the inlet of the press 50.
The kicker members 38 are rotated counterclockwise (FIG. 1) so that
the excess bagasse which extends above a predetermined distance
from the plate 35 is picked up by the spikes 39 and is rolled or
tumbled down into the chamber 18. This tumbling action is desirable
to assure that all of the bagasse is heated and saturated by the
steam introduced through the perforations 55. As a result of the
adjustable speed of the conveyor 25 provided by the drive unit 65,
a uniform flow rate of bagasse can be selected for discharge
through the chute 45 to assure that the press 50 will receive a
continuous and uniform flow of bagasse so that the press will
operate smoothly and will continuously discharge dewatered bagasse
having a consistently low moisture content.
By directing the press water or juice expressed from the material
within the press 50 into the inlet 59 and through the openings 60,
the uniform bed of material carried upwardly by the conveyor 25
provides a filter for removing fines and other particles from the
press water with the result that the juice received within the
chamber 62 and drained through the outlet 64 is substantially
clear. The addition of lime to the press water prior to filtering
has been found desirable to increase the pH value of the bagasse
prior to feeding the bagasse into the press. The higher pH value of
the bagasse not only increases the efficiency of the press by
making the bagasse somewhat slippery but also helps to reduce
corrosion of the press.
It has also been found desirable to supply live steam or hot water
through the openings 55 to heat the bagasse within the chamber 18.
That is, it has been found that hot bagasse can be compacted within
a screw press with less power required to drive the press and
without reducing the amount of moisture which can be expressed from
the bagasse.
In accordance with a modified embodiment of the invention shown in
FIGS. 4 and 5, a hopper 75 is supported by a frame 76 and including
a pair of opposed sloping end walls 77 connected by parallel spaced
sidewalls 78 and bottom walls 79 to define a chamber 80.
Perforations 82 are formed in the bottom walls 79 to provide for
drainage of liquid from the material contained within the chamber
80 into the chambers 82 defined by the bottom pans 84 which are
provided with drain outlets 85.
A series of lower shafts 86 are rotatably supported adjacent the
bottom walls 79 by bearing 87 (FIG. 5), and each shaft supports a
pair of sprockets 88 and is driven by a drive 89. Similar sprockets
are mounted on upper shafts (not shown) each of which corresponds
to the upper shaft 30 shown in FIG. 1. A pair of endless chain
conveyors 90 are directed around the sprockets, and each conveyor
includes a series of laterally extending drag members 91 similar to
the drag members 33 of the conveyor 25 shown in FIG. 1. As shown in
FIG. 4, the lower reach of each conveyor 90 extends adjacent the
corresponding sloping endwall 77 and the upper reach extends
adjacent the upper surface of a wall member or plate 92 so that the
material is dragged up the surface by the drag members 91 and
discharged from each end of the hopper 75 in a manner the same as
shown in FIG. 1.
While not shown, a series of rotary kicker members 38 are mounted
within the upper portion of the hopper 75 in spaced relation to the
wall members 92 in the same manner as the kicker members 38 mounted
within the hopper 10 as shown in FIG. 1. It has been found that the
hopper 75 having twin conveyors 90 is particularly desirable for
feeding a uniform flow of sugar cane bagasse simultaneously to a
plurality of dewatering screw presses 50 or other presses when a
single conveyor hopper is not sufficient to handle the capacity. It
also can be seen that the drag members 91 slide across the bottom
walls 79 and prevent clogging of the drainage perforations 82 in
the same manner as the self-cleaning operations shown in FIG.
3.
Conduits 52 are mounted on the underneath surfaces of both wall
members 92 in the same manner as shown in FIG. 1, for supplying
steam or hot water from the lines 54 and through the perforations
or openings 55 for heating the bagasse within the hopper 75. It has
been found desirable to maintain or increase the temperature of the
bagasse within the hopper 75 to at least 160.degree. F. and
preferably within a range of 180.degree. F. to 200.degree. F. so
that, as mentioned above, the bagasse becomes slippery and will
flow more smoothly through the screw press 50 with the result that
less power is required to operate the press and the bagasse
discharged from the press has a uniformly low moisture content.
Referring to FIGS. 6--9 which illustrate another embodiment of the
invention, the apparatus includes a housing 100 defining a
receiving chamber 102 into which sugar cane bagasse B is supplied
from a source such as a diffuser (not shown) which normally
discharges the material in periodic surges. The bagasse is
discharged from the diffuser into a laterally extending screw
conveyor 104 (FIG. 7) which directs the bagasse laterally and into
an inlet opening 106 at the top of the chamber 102.
Extending horizontally from the housing 100 is an elongated housing
108 which encloses an endless conveyor 110 having a pair of spaced
apart endless chains 112 (FIG. 8) which are directed around a pair
of sprockets 113 rotatably supported on a shaft 114 within the
receiving chamber 102 and a pair of drive sprockets 115 rotatably
mounted at the opposite end of the housing 100 on a shaft 116. The
endless chains 112 are also directed around sprockets 117 and 118
rotatably supported within the upper portion of the receiving
chamber 102 to provide a slight incline of the conveyor 110 within
the receiving chamber.
A series of uniformly spaced drag members 120 are mounted on the
chains 112 as shown in FIGS. 7 and 8 and define a corresponding
series of open top and bottom compartments 122 between adjacent
drag members 120. As shown in FIGS. 6 and 8, the housing 108 has a
bottom 124 which slidably supports the drag members 120 along the
lower distributing reach of the conveyor 110, and a top member 125
covers the lower reach. Similarly, the housing has a bottom member
124' which supports the drag members along the upper return reach
of the conveyor.
To prevent the bagasse from jamming the movement of the conveyor, a
series of kicker members 126 constructed substantially the same as
the kicker members 38 shown in FIG. 1, are rotatably mounted within
the receiving chamber 102. Each of the kicker members 126 includes
a series of spikes 127 (FIG. 7) which extend radially from a
laterally extending support shaft 128 which is driven in a
clockwise direction as shown by the arrow in FIG. 6 by a suitable
drive unit (not shown) connected to the sprocket 129 (FIG. 7)
mounted on the end of the shaft 128.
As shown in FIG. 6, the kicker members 126 are positioned at
different elevations in relation to the bottom wall member 124 and
are covered by a ramp member 130 which forms an extension of the
top wall member 125 so that the pile of bagasse B is progressively
reduced in height to form a substantially uniform layer or bed 132
of material which is generally flush with the top of the drag
members 120. Thus the bagasse extending above the drag members is
rolled back into the receiving chamber 102 producing a tumbling
action of the pile of bagasse. If desired, steam or hot water may
be introduced into the bagasse for heating the bagasse, as for
example, by employing self-cleaning perforations within the bottom
wall 124 of the chamber 102 and mounting steam supply conduit
members 52 on the bottom wall in the same manner as shown in FIGS.
1 and 4.
The bed 132 of bagasse is carried by the drag members 120 within
the compartments 122 along the lower distributing reach of the
conveyor to feed one or more mechanical presses such as the screw
presses 50 having inlets connected by corresponding feed chutes 134
to a corresponding series of openings 135 formed within the bottom
wall member 124. As shown in FIG. 8, preferably a transfer screw
136 is rotatably supported within a housing 138 mounted on the
underneath side of the bottom wall member 124 for each press 50 to
feed the bagasse which drops through the opening 135 into the
smaller feed chute 134.
As illustrated in FIG. 6, the conveyor 110 is constructed with a
capacity to supply the material at a somewhat greater rate than is
necessary for maintaining each of the housings 138 filled with
material when the presses 50 are operating at maximum capacity.
Thus excess material E remains in the lower distributing reach of
the conveyor 110 after feeding the final screw press 50 and is
carried around the end of the conveyor enclosed by the
semicylindrical housing portion 140 and along the upper return
reach of the conveyor where it is released to drop past the
downwardly formed end 141 of the ramp member 130 onto the top of
the pile of material.
In a suitable construction of the apparatus, the conveyor 110 has a
width of approximately 5 feet and the kicker members are positioned
to form a material bed 132 having a substantially uniform thickness
of approximately 8 inches. The conveyor 110 has been driven at a
rate of approximately 6 feet per minute to feed a predetermined
supply of material into the lower distributing reach of the
conveyor. Preferably, approximately 25 percent excess material E is
carried along the lower reach of the conveyor to assure that the
final screw housing 138 is maintained completely filled with
material.
A modification of the embodiment shown in FIGS. 6--8 is shown in
FIG. 9. As mentioned above, it has been found desirable to use the
uniform bed of bagasse as a filter for removing fines and
undesirable particles from the juice which is expressed out of the
bagasse by the screw presses 50. To provide this feature in the
apparatus shown in FIG. 6, a section of the housing 108 is provided
within perforations or openings 144 in the top and bottom wall
member 125" and 124", respectively. Contaminated juice is fed
through the inlet opening 145 formed, within a housing 146 mounted
on the upper wall member 125" and feeds into the bed 132 of
bagasse. Filtered juice is collected within the pan 148 mounted on
the bottom wall member 124" and drains into the conduit 149.
From the drawings and the above description, it can be seen that
the apparatus formed in accordance with the present invention
provides several desirable features and advantages. Basically, the
apparatus is adapted to receive surges or an irregular supply of
hard to handle material such as sugar cane bagasse and then
distribute a uniform mat or bed of material for feeding one or more
expressing devices such as a series of mechanical screw presses.
The apparatus produces this uniform supply of material by retaining
within the receiving chamber the excess material which projects
above a predetermined distance on the feed conveyor.
Another important feature is provided by the conduits 52 for
introducing steam into the bagasse while in the receiving chamber
for raising the temperature of the bagasse to a predetermined
minimum level and thereby provide a more efficient and effective
processing of the bagasse B in each screw press 50. The embodiment
shown in FIGS. 6 and 7 provides the additional feature of two
inclined conveyors for handling a higher capacity of bagasse and
feeding a plurality of presses.
A further feature is provided by the cooperation between the lower
end of the conveyor 25 or conveyors 90 and the corresponding bottom
drainage openings 24 or 82 whereby the drag members 33 or 91 sweep
past the openings and prevent them from clogging with material. A
similar self-cleaning action of the steam inlet openings 55 is
provided by the sweeping movement of the conveyor drag members 33
or 91. The embodiment shown in FIGS. 6--8 not only provides a
steady, uniform supply of material to each of the presses, it
assures this continuous supply by carrying an excess of material
which is directed back to the main source material for
recirculation.
Still another important feature of the invention is provided by the
filtering means shown in FIGS. 1 and 9. That is, by directing the
expressed juice or liquid through the uniform bed of bagasse as it
is fed to the inlet of a press, fines and foreign particles are
removed from the expressed juice. In addition, the material is
effectively macerated before it enters the press.
While the forms of apparatus herein described constitute preferred
embodiments of the invention, it is to be understood that the
invention is not limited to these precise forms of apparatus, and
that changes may be made therein without departing from the scope
of the invention which is defined in the appended claims.
* * * * *