U.S. patent number 3,734,399 [Application Number 05/147,796] was granted by the patent office on 1973-05-22 for differential scroll drive.
This patent grant is currently assigned to Beloit Corporation. Invention is credited to David C. Oas.
United States Patent |
3,734,399 |
Oas |
May 22, 1973 |
DIFFERENTIAL SCROLL DRIVE
Abstract
A driven centrifuge mechanism for separating intermixed liquids
and solids including a hollow bowl supported for rotation about an
axis with a smaller inner diameter at one end and a larger at the
other end and a helical conveyor scroll extending through the
center for moving solids to a solids opening at one end of the bowl
and a liquid opening at the other end of the bowl and a drive at
one end of the bowl connected to the bowl and to the scroll for
driving the bowl off a main drive motor at a constant speed and for
varying the speed of the scroll relative thereto with the main
drive motor driving a hydraulic pump which drives a hydraulic motor
and through a differential gear means drives the scroll with the
speed between the hydraulic pump and motor variable so as to be
able to control the speed of the scroll.
Inventors: |
Oas; David C. (Pittsfield,
MA) |
Assignee: |
Beloit Corporation (Beloit,
WI)
|
Family
ID: |
22522932 |
Appl.
No.: |
05/147,796 |
Filed: |
May 28, 1971 |
Current U.S.
Class: |
494/8; 494/84;
494/53 |
Current CPC
Class: |
B04B
1/2016 (20130101); B04B 2001/2025 (20130101) |
Current International
Class: |
B04B
1/00 (20060101); B04B 1/20 (20060101); B04b
001/00 () |
Field of
Search: |
;233/7,19R,16,21,23R,24,19A |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Krizmanich; George H.
Claims
I claim as my invention:
1. A driven centrifuge mechanism for separating inter-mixed liquids
and solids comprising in combination,
a hollow bowl supported for rotation about an axis and having its
inner diameter decreasing toward one end with a solids opening at
said one end and a liquids opening at the other end,
a helical conveyor scroll coaxial within the bowl supported for
rotation at a controlled speed different than the bowl for moving
solids within said bowl toward the solids opening,
a feed means within the bowl for supplying a mixture of liquids and
solids to the bowl,
a differential gear drive means having an output shaft connected to
the scroll and having first and second input shafts, said first
input shaft connected to the bowl,
motor means drivingly connected to the first input shaft for
driving the bowl and first input shaft at a predetermined constant
speed,
a hydraulic pump driven by said motor means and having an output, a
hydraulic motor connected by fluid lines to the output of the
hydraulic pump for being driven thereby and drivingly connected to
the second input shaft of said gear drive means, and
means for controlling the relative flow displacement of said pump
and said motor so that the speed of said second input shaft is
controlled to thereby control the speed of said output shaft and
control the speed of the scroll relative to the speed of the
bowl.
2. A driven centrifuge mechanism for separating intermixed liquids
and solids constructed in accordance with claim 1 wherein said pump
is a positive displacement pump and with controlling means, varies
the fluid direction and output of the pump relative to its driven
speed.
3. A driven centrifuge mechanism for separating intermixed liquids
and solids constructed in accordance with claim 1 wherein said
differential gear drive means is a planetary gearing having sun
gears.
4. A driven centrifuge mechanism for separating intermixed liquids
and solids constructed in accordance with claim 3 wherein the sun
gears are connected to the first and second input shafts
respectively.
5. A driven centrifuge mechanism for separating intermixed liquids
and solids constructed in accordance with claim 1 and including a
liquid coupling between the motor means and said first input
shaft.
6. A driven centrifuge mechanism for separating intermixed liquids
and solids constructed in accordance with claim 1 and including a
pressure sensing valve connected to the output of the hydraulic
pump.
7. A driven centrifuge mechanism for separating intermixed liquids
and solids constructed in accordance with claim 6 including a feed
control valve connected to said feed means and connected to said
pressure sensing valve and operated as a function of the pump
pressure output to regulate the feed to the bowl.
8. A driven centrifuge mechanism for separating intermixed liquids
and solids comprising in combination,
a hollow bowl supported for rotation about an axis and having its
inner diameter decreasing toward one end with a solids opening and
a liquids opening,
a helical conveyor scroll coaxial within the bowl supported for
rotation at a controlled speed different than the bowl for moving
solids within said bowl toward the solids opening,
a feed means within the bowl for supplying a mixture of liquids and
solids to the bowl,
a variable speed output drive means having an output shaft
connected to the scroll and having first and second input
shafts,
motor means drivingly connected to the bowl and connected to the
first input shaft for driving the bowl and first input shaft at a
predetermined constant speed,
a hydraulic pump driven by said motor means,
a hydraulic motor connected by fluid lines to the hydraulic pump
for being driven thereby and drivingly connected to the second
input shaft of said gear drive means, and
means for controlling the relative flow displacement of said pump
and said motor so that the speed of said second input shaft is
controlled to control the speed of the scroll relative to the speed
of the bowl.
9. A driven centrifuge mechanism for separating intermixed liquids
and solids constructed in accordance with claim 1 wherein the
controlling means includes a control valve means for controlling
flow direction.
Description
BACKGROUND OF THE INVENTION
The invention relates to a centrifuge mechanism for separating
solids and liquids from a mixture and controlling the speed of the
separator for optimum separation.
Centrifuge separators of this type have been employed in various
industries and operate with a mechanism wherein a solid or
perforated bowl centrifuge rotates at an optimum separation speed
and has an axial screw conveyor or scroll extending coaxially
therethrough. The screw conveyor functions to move the solids
toward one end of the bowl for a discharge and liquids are
discharged at the other end. An unseparated mixture of liquids and
solids is supplied to the bowl coaxially through the conveyor to be
fet at the processing speed of the conveyor. Control of the speed
of the feed may be provided and an important factor is the speed of
the scroll. With variant consistencies of the mixture and varying
speeds of separation within the bowl, the speed of the screw
conveyor must be controllable independent of the bowl speed.
Various mechanisms have been provided heretofore to control the
speed of the screw conveyor, and each of these structures have
encountered disadvantages. Without control of the speed of the
screw conveyor scroll, the mixture will not separate properly and
matting and jamming can occur within the bowl. Also, because of the
relative speed of the screw conveyor, an agitation and resuspension
of the solids occurs as they progress toward the solid discharge
end of the bowl. Rapid sedimentation without resuspension is
essential for effective and efficient separation.
Also, it is essential to be able to control the speed of the
conveyor scroll without providing a mechanism which results in the
substantial loss of energy or power, for purposes of reducing the
initial cost of the mechanism, the operating cost and the space
requirements.
It is accordingly an object of the present invention to provide an
improved centrifugal separating mechanism for the separation of
intermixed liquids and solids which has an improved drive
arrangement that results in an enhanced separation function of the
machine.
A still further object of the invention is to provide an improved
centrifugal separator and drive which effects a saving in power
consumption, space and cost for devices heretofore available.
It will be apparent from the description of the invention that
alternate embodiments may be employed within the scope and spirit
of the invention, and other objects and advantages will become more
apparent with the teaching of the principles of the invention in
connection with the disclosure of the preferred embodiments in the
claims, specification and drawings in which:
DESCRIPTION OF THE DRAWINGS
FIG. 1 is a somewhat schematic side elevational view, taken
partially in section, of a structure constructed and operating in
accordance with the principles of the present invention; and
FIG. 2 is a schematic showing of a portion of the drive
mechanism.
DESCRIPTION
As illustrated in FIG. 1, the separator includes an elongate
cylindrically shaped imperforate bowl 10 which is driven by shaft
41 and is supported for rotation about a central axis on end
bearings 14 and 15. Surrounding the bowl is a casing 11 which is
provided with a solids discharge outlet 12 at one end and a liquid
discharge outlet 13 at the other end, and these outlets are lead
from solids discharge ports 12a at one end of the bowl 10 and
liquid discharge ports 13a at the other end of the bowl.
The bowl is driven in rotation for centrigugal separation of
liquids and solids from a mixture fed therein.
Within the bowl is a rotating conveyor scroll 19 having helical
lands thereon for moving the solids toward the solids discharge
ports 12a. The scroll 19 rotates coaxial with the bowl 10, but at a
slightly slower speed being supported the shaft 18 supported on one
end on bearing 24 and on the other end on a bearing not shown.
A mixture of liquids and solids is supplied in a continual flow to
the bowl through an inlet line 20 which feed axially inwardly past
a feed control valve 22 within the scroll and the mixture passes
radially outwardly through feed ports 21 in the scroll body.
The process of centrifugal separation which occurs within the bowl
is known to those versed in the art and need not be discussed
further in detail, however, in operation, the mixture feeds in
through the inlet 20 and out through the ports 21 to come into
engagement with the inner surface of the rotating bowl 10, and as
the solids centrifugally separate from the liquid the solids are
conveyed by the scroll toward the smaller diameter end of the bowl,
and the liquids flow toward the larger diameter end. The speed of
rotation of the scroll for the proper speed of conveyance of the
solids is essential for the operation and effective separation and
continued satisfactory operation can be attained only by obtaining
the proper speed of scroll rotation relative to the speed of
rotation of the bowl and the speed of separation of the mixture of
products therein.
The bowl is driven directly by a main drive motor 27 through
suitable means such as V-pulleys and belts 26. In one form a fluid
coupling 28 may be provided within the main drive motor, and the
V-belt drive.
For driving the scroll at a controlled speed, a variable speed
drive means perferably in the form of a planetary gear reducer 29
is provided. The gear reducer, and its associated mechanism, are
driven off of the same main drive motor so that only a single main
source of power need be provided. As shown in FIG. 2, the gear
reducer in a preferred form embodies a planetary gearing with an
output shaft 39 and a first input shaft 41 and a second input shaft
43. The planetary gears 32 are connected to the output shaft 39,
and the first input shaft is connected to the sun gear 31, and the
second input shaft 43 is connected to the sun gear 33.
The planetary gearing is driven through the input shaft 41 from the
main drive motor 27. Control of the speed is attained through the
second input shaft 43 which is driven by a hydraulic motor 34. The
hydraulic motor is operated from a hydraulic pump 35 and connector
lines 36 extend between the pump and motor. The pump is driven also
by the main drive motor 27.
In a preferred form, the hydraulic pump 35 and hydraulic motor 34
are variable positive displacement types with the displacement of
the pump and motor controlled by control members. Therefore, the
pump may operate at a constant speed as driven by the motor 27, and
the hydraulic motor 34 will operate at a speed determined by the
setting of the displacement of the hydraulic pump 35. On the pump
35 or in the hydraulic lines 36 is a valve 37 which operates to
reverse the lines so that the flow between the pump and motor can
be set for operation in mode I or mode II. In mode I the sun gear
member 33 is allowed to rotate in the same direction as the
centrifuge bowl. The differential speed, which is the speed of the
bowl minus the speed of the scroll, is determined from the
equation:
The hydraulic drive is normally functioning in mode I as a retarder
and power flow is such that the fixed displacement hydraulic motor
is actually performing as a pump, and the variable displacement
pump operates as a motor. This accomplishes energy recovery by
hydraulic transmission from the sun gear back to the main drive
motor.
In mode I the hydraulic drive may also function as a drive, wherein
the hydraulic motor performs as a motor and the hydraulic pump
performs as a pump.
In mode II the sun gear member 33 is driven in the opposite
direction of rotation of the centrifuge bowl. In this mode the
differential RPM is calculated from the equation:
In this mode the hydraulic drive functions as a drive, and the
output of the hydraulic pump drives the hydraulic motor. The
reduction ratio of the planetary gear reducer, of course, will be
chosen as optimum relative to the required speed of the scroll
relative to the bowl. For example, in a preferred arrangement the
scroll may operate at a differential speed of 16 RPM (absolute
speed of 3,784 RPM) while the bowl operates at 3,800 RPM, and the
speed of the scroll may be adjusted upwardly or downwardly in
accordance with the wetting of the hydraulic pump.
An advantage of this arrangement, as illustrated, is that the
output hydraulic pressure of the pump is proportional to the torque
required to drive the scroll. Thus, a pressure valve 38 is
connected to the lines 36 to indicate fluid pressure and hence
indicate the scroll drive torque. The valve 38 may be provided with
an overload protection arrangement to prevent damages to drive
mechanism, which limits torque on reducer 29, allows motor 34 to
"free wheel" or which shuts down the entire mechanism at maximum
torque. In the structure shown in FIG. 2, the pressure valve 38 is
connected to the feed control valve supplying the mixture of solids
and liquids to the separator. By thus decreasing the feed as the
torque increases, uniform separation and uniform constant operating
conditions can be maintained.
It will be appreciated that the drive arrangement is not positively
limited to the exact separator shown, but may be used with
different design separators.
Thus, with the arrangement of the instant invention, torque
overload protection is obtained, only a single drive source need be
provided, accurate differential speed control is obtained, torque
overload possibility has been eliminated, and a compact power
saving unit has been provided. Recovery of approximately 75 percent
of the scroll horsepower consumption which is normally lost through
structures of the prior art that employ separate braking devices,
is attained.
* * * * *