U.S. patent number 3,765,599 [Application Number 05/184,887] was granted by the patent office on 1973-10-16 for self cleaning centrifuge drum with stepwise variable closing pressure.
This patent grant is currently assigned to Westfabia Separator AG. Invention is credited to Heinrich Hemfort.
United States Patent |
3,765,599 |
Hemfort |
October 16, 1973 |
SELF CLEANING CENTRIFUGE DRUM WITH STEPWISE VARIABLE CLOSING
PRESSURE
Abstract
A centrifugal separator constructed for performing full
desludgings as well as partial desludgings during separation. One
end member of the separating chamber is a piston valve movable
axially to open and close sludge discharge openings disposed at the
outer periphery of the drum. The axially outward disposed side of
the piston valve is in sliding sealing engagemenet with confronting
drum portion at radially spaced intervals so that a radial
succession of divisions of the closing chamber is provided which
can be filled up in a known manner with control fluid and
selectively emptied for reducing the force acting on the piston
valve and thereby performing a full desludging or a partial
desludging.
Inventors: |
Hemfort; Heinrich (Oelde,
DT) |
Assignee: |
Westfabia Separator AG
(Oelde/Westf., DT)
|
Family
ID: |
5783995 |
Appl.
No.: |
05/184,887 |
Filed: |
September 29, 1971 |
Foreign Application Priority Data
|
|
|
|
|
Oct 2, 1970 [DT] |
|
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P 20 48 429.1 |
|
Current U.S.
Class: |
494/29; 494/40;
494/30 |
Current CPC
Class: |
B04B
1/18 (20130101) |
Current International
Class: |
B04B
1/00 (20060101); B04B 1/18 (20060101); B04b
011/00 () |
Field of
Search: |
;233/19R,19A,2R,2A,46,47R |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Krizmanich; George H.
Claims
What is claimed is:
1. In a centrifugal separator constructed for intermittent
discharge of sludge, comprising:
a. a rotatably mounted separator drum having an upper end member
and a lower end member defining a separating and sludge chamber, at
least one sludge discharge passageway disposed at the radially
outward periphery of the drum,
b. one of said end members including a piston valve movable axially
within said chamber to open and close the sludge discharge
passageway for desludging,
d. a fluid operated piston valve control means for alternatively
forcing the piston valve to the closed position by the pressure of
a control fluid and permitting the piston valve to move to an open
position by relieving the pressure of the control fluid,
d. control fluid routing means for pressurizing and depressurizing
of control fluid for controlling the position of the piston
valve,
the improvement which comprises:
e. said piston valve having an axially outwardly disposed surface,
and said drum having a surface confronting said surface of the
piston valve, said piston valve control means comprising a
plurality of closing chambers disposed in radial succession from
the axis, concentric slide seals between the axially outwardly
disposed surface of the piston valve and said confronting drum
surface, providing said plurality of closing chambers,
f. said control fluid routing means comprising means for
selectively pressuring and depressurizing of the closing chambers
permitting selection of the force imposed on the piston valve.
2. Separator according to claim 1, said control routing means
comprising fluid controlled valves for closing and opening of the
control chambers for, respectively, pressurization and
depressurization of control fluid therein.
3. Separator according to claim 1, said control fluid routing means
comprising conduits outfitted with control valves for controlled
routing of the control fluid and a controller for controlling
operation of the control valves in dependence on operation of the
separator.
Description
BACKGROUND
The invention relates to self-cleaning centrifuge drums in which
the separating chamber and the sludge chamber are defined at one
end by the piston valve controlling the sludge discharge outlet
apertures. Drums of this type of construction are provided with a
closing chamber located between the piston valve and the adjacent
portion of the drum, which is filled with a control fluid before
the centrifuging to impose pressure on the piston valve to move the
piston valve and thereby close the sludge discharge openings. The
closing chamber has a greater radial expanse than the sludge
chamber, so that when the closing chamber is completely filled with
fluid exerting closing pressure acting to close the piston valve,
the closing force on the piston valve is always greater than the
force of the drum charge acting on the other side urging the piston
valve open. For the ejection of solids, control fluid is let out of
the closing chamber with the drum running at full speed, and thus
the closing pressure is diminished. Under the pressure of the drum
charge the piston valve then moves to the position in which the
sludge discharge outlet apertures are uncovered.
Depending on the nature and consistency of the separated solids, it
may be advantageous to perform so-called partial desludgings at
brief intervals of time, with occasional full desludging operations
at longer time intervals.
When partial desludging is performed, the sludge discharge outlet
apertures are opened only slightly and/or for a brief period, so
that only a portion of the accumulated solids in the sludge chamber
is ejected, while the rest remains as a safety ring within the
drum. This prevents any great amount of product fluid from being
ejected with the solids and going to waste.
When full desludging is performed, the drum is opened wide and the
entire contents of the drum is ejected. To achieve a thorough
cleaning, full desludging is often followed by a rinsing operation
in which the drum is filled with fresh water and spun to empty it
again.
To limit the length of time and the degree to which a self-cleaning
drum is opened for partial discharge purposes, the drum can be so
constructed that a portion of the closing fluid (the fluid in the
closing chamber urging the piston valve toward the closed position)
remains in the closing chamber. After the ejection of solids
commences, as soon as the fluid level in the separating chamber has
receded to such an extent that the opening pressure is lower than
the closing pressure of the closing fluid remaining in the closing
chamber, the piston valve immediately moves back to the closed
position. The greater the closing pressure of the control fluid
retained in the closing chamber is, the more rapidly the drum
recloses and the less solid matter is ejected in each opening
operation.
A drum of different construction, having a closing chamber that
does not have to be emptied, is shown for example in German Pat.
No. 1, 055,451. With this prior-art drum both partial and full
desludging can be performed, depending on how long an opening
chamber is kept filled with control fluid. This time-dependent
control, however, is quite critical in the performance of partial
desludging, because the time it takes to fill the opening chamber
of that device is dependent upon the water pressure, and is a
portion of the time that has to be preset in a control
apparatus.
But even in the case of a drum having a piston valve which defines
one side or end of the separating chamber, it is a known porcedure
to retain a portion of the closing fluid in the closing chamber.
German Auslegeschrift Pat. No. 1,432,760 discloses a plurality of
design possibilities for achieving this.
According to one of these proposals, a conical plate is inserted
into the closing chamber to divide the outer portion of the chamber
into two axially opposite chambers. The outlet passage, which is
controlled by a valve, extends from the periphery of the lower
chamber. When this valve is opened for the ejection of solid
matter, the closing fluid in the upper chamber of the outer portion
of the closing chamber always remains, and causes the piston valve
to move to its closed position whenever the fluid level in the
separating chamber recedes and the pressure on the top side of the
piston valve has become lower than the pressure of the retained
closing fluid acting on its bottom side. With this drum, however,
only partial desludging can be performed.
According to another proposal set forth in German Auslegeschrift
Pat. No. 1,432,760, the lower portion of the drum is provided at
various distances from the axis of rotation with outlet bores for
closing fluid, which extend from the closing chamber. The closing
chamber extends over the entire radial expanse of the piston valve.
These bores can be selectively stopped with plugs, so that the
level of the retained closing fluid can be adjusted to different
distances from the axis of rotation. The orifice of these bores on
the outside of the drum are uncovered by an axially movable valve
at predetermined intervals of time for the purpose of the ejection
of solid matter. With this drum it is possible to adjust the
draining of the closing fluid such that either full desludging can
be performed, or partial desludging operations adapted to the
specific weight of the mixture being centrifuged.
If the outlet bores on the periphery of the closing chamber are
uncovered, the chamber is completely emptied upon the opening of
the valve and thus a full desludging is performed. The closer the
open outlet bores are to the axis of rotation, the more closing
fluid is left in the closing chamber, and only partial desludging
can be performed.
In order to change over from full desludging to partial desludging,
and to adapt the level of the retained closing fluid to the
specific weight of a different mixture, the drum has to be stopped
and at least partially disassembled.
THE INVENTION
The invention is first addressed to the problem of creating a
centrifuge drum which selectively permits the performance of
partial and full desludging operations without shutting down the
separator.
In further development of this main idea, it will be possible in a
step-wise manner to vary the closing pressure of the retained
closing fluid during operation.
The invention is characterized by the fact that the piston valve,
in addition to its customary guidance, is additionally guided
sealingly on the adjacent drum portion at different distances from
the axis of rotation and thereby divides the closing chamber into a
plurality of radially successive divisions which can be fed with
control fluid in a known manner and can be selectively emptied
through passages which lead outwardly from the peripheral portions
of the individual divisions. In the case of simultaneous emptying
of all divisions, the closing pressure is completely eliminated, so
that full desludging operations can be performed.
When only one or several of the divisions are emptied, a portion of
the closing fluid is retained, so that partial desludging can be
performed.
The radial dimensions of the individual divisions can be such that
different partial pressures result, which individually or in
combination permit extensive adaptation of the residual closing
pressure to the specific weight of the mixture being centrifuged
and of the solids being separated.
Thus, in summary, the invention is concerned with a centrifugal
separator constructed for intermittent discharge of sludge,
comprising a rotatably mounted separator drum having a separating
chamber defined by an upper end member and a lower end member, and
at least one sludge discharge passageway disposed at the radially
outward periphery of the drum. One of said end members of the
separating chamber is a piston valve movable axially to open and
close the sludge discharge passageway for desludging Fluid operated
piston valve control means are provided for alternately forcing the
piston valve to the closed position by a fluid pressure created in
a closing chamber by feeding a control fluid thereto and permitting
the piston valve to move to an opened position by draining off the
control fluid therefrom. Further included are control fluid routing
means for controlling the position of the valve. The invention
provides the improvement which comprises the piston valve control
means including a plurality of divisions of the closing chamber
disposed in radial succession from the axis, provided by concentric
slide seals between the axially outwardly disposed surface of the
piston valve and the confront1ng drum portion. The control fluid
routing means includes means for connecting the different divisions
of the closing chamber with the infeed of the control fluid and
means for selectively depressurizing of the different divisions of
the closing chamber permitting selection of the force imposed on
the piston valve.
A number of embodiments of the invention are represented in the
drawing.
FIG. 1 shows a centrifuge drum in which the closing chamber is
divided into two divisions which can be emptied selectively through
valves which are held in closing position by feeding a liquid
thereto and brought to the open position by shutting off the
infeed. (In each of the figures, the piston valve is shown in the
closed position (sludge discharge passageways closed) on the left
of the figure, and in the open position on the right side. Also,
like reference characters refer to corresponding parts.)
FIG. 2 shows the same drum, in which the valves are normally in
closed position and brought to the open position by the infeed of
fluid, and
FIG. 3 shows a centrifuge drum in which the closing chamber is
divided into three divisions from whose peripheral portions
calibrated bores lead outward.
With reference to FIG. 1, a separating and sludge chamber is
provided by separating section 1 and sludge section 2. The chamber
is defined by upper end member 3a and lower end member 3, which is
a piston valve which is axially movable. Axial movement of piston
valve 3 opens and closes the sludge discharge apertures 4 for the
ejection of solids. Between the piston valve 3 and the lower drum
wall 5 is located the closing chamber which in the present
embodiment is divided so as to provide two chambers or two
divisions 6 and 7, which are sealed from one another and are at
different radial distances from the axis so that they are disposed
in radial succession from the axis, the piston or slide valve 3
being not only sealingly guided in the conventional manner at 8 and
8a, but being also sealingly guided at 9 on the adjacent drum part
5.
The separator includes control fluid routing means for pressurizing
and depressurizing of control fluid for controlling the position of
the piston valve. Outlet passages 10 and 11 run from the radially
external end of divisions 7 and 6, respectively, and are
controlled, respectively by fluid controlled valves 12 and 13.
These valves are held in the closed position by the constant infeed
of fluid and are brought into the open position by shutting off the
feed of fluid. Their manner of operation is described in detail in
the copending German Pat. application P 20 22 197.0 of the assignee
hereof; U.S. Ser. No. 139,078 filed Apr. 30, 1971, also of the
assignee hereof.
Prior to the opening of the inlet (not shown) for the liquid that
is to be separated, control valves 14 and 15 in control fluid
infeed conduits or lines 16 and 17 are opened, this being brought
about in the present embodiment by the control apparatus 18. The
control fluid passes from feed line 16 through bore 19 into the
receiving groove 20 and from feed line 17 through bore 21 into the
receiving groove 22. From the receiving groove 20 the control fluid
flows first through the passage 23 which runs out radially and
brings the valve 12 into the closed position. The receiving groove
22 communicates with valve 13 through a passage 24, so that this
valve, too, shifts to the closed position.
The controller 18 can actuate the various valves such as 14 and 15
to control desludging in dependence on operation of the separator,
e.g., based on a time interval or operation, e.g., properties of
product.
After passage 23 is filled up, the control fluid passes in known
manner from the receiving groove 20 to the closing chamber, passing
in the present embodiment through one or more passages 25 into the
outer division 7 of the closing chamber, and through one or more
passages 26 into the inner division 6 of the closing chamber. In
both instances, control fluid overflows from groove 20 in the
respective bores leading to the respective chamber divisions. The
sum of the closing forces produced in divisions 6 and 7 is equal to
the closing force which the control fluid would produce in an
undivided closing chamber. The filling up of divisions 6 and 7
brings the piston valve 3 into the closed position (left side of
FIG. 1).
After a certain quantity of solid matter has collected in the
sludge chamber 2, the outlet valve 12 is opened by the closing of
valve 14 in the control fluid infeed line 16 and the outer division
7 is thereby emptied, while the closing fluid is retained in the
inner division 6.
Starting with both valves 14 and 15 open, by the closing of valve
15 in the control fluid infeed line 17, the outlet valve 13 is
opened and the pressure in the inner division is thereby relieved
since the fluid can then run freely through the inner division,
while the closing fluid is retained in the outer division 7. In
both cases partial desludging is performed. The individual closing
pressures in divisions 6 and 7 can be different. The piston valve 3
moves to the open position (right side of FIG. 1) and immediately
moves back to the closed position whenever the opening pressure has
become lower than the closing pressure of the retained closing
fluid as a result of the receding liquid level in separating
chamber 1.
The closing of both valves 14 and 15 brings both outlet valves 12
and 13 into the open position and both divisions 6 and 7 are
emptied so that the drum is completely emptied.
To avoid the trouble that would develop if excess control fluid
were to pass over from receiving groove 20 into receiving groove
22, receiving groove 20 is provided with an overflow pipe 27 to
limit the fluid level to prevent overflow from groove 22 into
groove 20, the diameter of the overflow lip 28 is made larger than
that of of the annular flange 29 which separates grooves 20 and
22.
In the embodment in FIG. 2, the outlet valves 12 and 13 are closed
in the fluid-free state and are brought into the open position by
the infeed of control fluid. The manner of operation of such valves
is also described in detail in copending German Pat. application P
20 22 197.0, U.S. application Ser. No. 139,078 filed Apr. 30, 1971,
both assigned to the assignee hereof. This embodiment is
advantageous wherever there is a shortage of fresh water and its
consumption must be kept down.
The drum shown in FIG. 2 requires three infeed lines 30, 31 and 32
for control fluid with valves 33, 34 and 35, respectively, and
three separate receiving grooves 36, 37 and 38. When valves 33 and
35 are closed, the outlet valves 12 and 13 are also closed. when
valve 34 opens, control fluid flows in a known manner through the
aperture 39 into the receiving groove 36 and thence through
passages 25 and 26 to the inner and outer divisions 6 and 7 of the
closing chamber. After both divisions have been filled up, the
piston valve 3 is in the closed position and the fluid infeed can
be shut off.
After a certain amount of solid matter has built up in the sludge
chamber 2, the outlet valve 12 or 13 can be put into the open
position by a selective, momentary opening of valve 33 or 35, these
outlet valves being fed with control fluid from bores 67 and 68
through receiving grooves 38 and 37, respectively, and passage 69
and 70, respectively. In this manner the inner division 6 or the
outer division 7 of the closing chamber is emptied and a partial
desludging is performed. By the simultaneous opening of both valves
33 and 35 both divisions 6 and 7 are emptied and full desludging is
performed. To prevent the overflow of control fluid from one
receiving groove into another, overflow bores 40 and 41 are
provided for the two upper grooves 36 and 37, respectively, while
overflow lip 42 of the bottom groove 38 has a larger diameter than
the annular flange 43.
In the embodiment represented in FIG. 3 the closing chamber is
divided into three divisions 44, 45 and 46 of successively greater
radius by the fact that the piston valve 3 is sealingly guided at
47 and 48 in addition to the conventional guidance it has at 8 and
8a. Instead of outlet valves such as 12 and 13 in FIG. 1 for
controlling flow from the chamber divisions calibrated bores are
used, the bores permitting a small bleed stream to be discharged
continously from the chamber divisions when the divisions hold
fluid under pressure. If infeed to a division is shut off, the
division empties as calibrated bores 49,50 and 51 lead outward from
the peripheral portion of divisions 44,45 and 46.
The control fluid is fed in through separate lines 52. 53 and 54,
into which valves 55, 56 and 57, respectively, are installed. It
passes in known manner through bores 58, 59 and 60 into receiving
grooves 61, 62 and 63, and thence through passages 64, 65 and 66 to
divisions 46,45 and 44, respectively of the closing chamber. This
drum, like the one in FIG. 1, requires a constant infeed of control
fluid.
If all three valves 55, 56 and 57 are simultaneously closed the
control fluid is dumped by centrifugal force from the three
divisions 44,45 and 46 through the calibrated bores 49, 50 and
51.
Upon the selective closing of the individual valves or of two
valves in combination, partial desludging takes place. The closing
force of the retained fluid can be varied step-wise over a wide
range.
EXAMPLE
Let us say that the radial dimensions of the individual divisions
44, 45 and 46 are such that the fluid in the inner division
produces three twelfths, the fluid in the middle division produces
four twelfths and the fluid in the outer division produces five
twelfths of the total closing pressure. The following closing
pressure settings are then possible.
I Inner chamber only 3/12 of the total closing pressure
II Middle chamber only 4/12 of the total closing pressure
III Outer chamber only 5/12 of the total closing pressure
IV Inner + middle chamber 7/12 of the total closing pressure
V nner + outer chamber 8/12 of the total closing pressure
VI Middle + outer chamber 9/12 of the total closing pressure
VII Inner + middle + outer chamber 12/12 of the total closing
pressure
Any other desired division can, of course, be chosen.
The closing chamber may also be divided into four or more
divisions, thereby appreciably increasing the number of possible
combinations.
Also, it is possible to provide the drum in FIG. 1 with calibrated
outlet bores instead of outlet valves, or the drum in FIG. 3 can be
equipped with valves as in FIGS. 1 or 2 instead of calibrated bores
as in FIG. 3. The control fluid infeed passages must then be
arranged in accordance with the construction of the drum. With the
drums of the invention it is possible selectively to perform full
or partial desludging without any conversion, and, in the
performance of partial desludging, to adapt the closing pressure of
the retained fluid to the specific weight of the liquid being
centrifuged and to the solid matter being separated.
* * * * *