U.S. patent number 3,777,972 [Application Number 05/235,633] was granted by the patent office on 1973-12-11 for sludge centrifuge.
This patent grant is currently assigned to Alfa-Laval AB. Invention is credited to Ove Allan Valentin Kjellgren.
United States Patent |
3,777,972 |
Kjellgren |
December 11, 1973 |
SLUDGE CENTRIFUGE
Abstract
Spaced around the periphery of the centrifugal rotor are
permanently open nozzles for discharging sludge separated from the
liquid fed to the separating chamber of the rotor. To remove the
sludge cushions accumulating on the peripheral wall of this chamber
between the permanently open nozzles, the rotor periphery has at
least one sludge outlet which is alternately opened and closed by
an axially movable piston valve.
Inventors: |
Kjellgren; Ove Allan Valentin
(Stockholm, SW) |
Assignee: |
Alfa-Laval AB (Tumba,
SW)
|
Family
ID: |
20263053 |
Appl.
No.: |
05/235,633 |
Filed: |
March 17, 1972 |
Foreign Application Priority Data
|
|
|
|
|
Mar 25, 1971 [SW] |
|
|
3877/71 |
|
Current U.S.
Class: |
494/48;
494/27 |
Current CPC
Class: |
B04B
1/18 (20130101) |
Current International
Class: |
B04B
1/00 (20060101); B04B 1/18 (20060101); B04b
001/12 () |
Field of
Search: |
;233/19R,19A,2R,2A,46,47R |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Krizmanich; George H.
Claims
I claim:
1. In a centrifuge for separating a sludge-containing liquid, the
combination of a centrifugal rotor having a separating chamber and
including a peripheral portion, said chamber having permanently
open nozzle means leading outward from the chamber periphery for
discharging sludge separated therein, said peripheral portion
having a sludge outlet opening, and a piston valve movable in the
rotor axially thereof between a first position for preventing
sludge discharge from said peripheral portion of the chamber except
through said nozzle means and a second position for discharging
sludge through said outlet opening independently of said nozzle
means.
2. The combination according to claim 1, in which said nozzle means
are in the piston valve.
3. The combination according to claim 1, in which said nozzle means
are in said peripheral portion of the rotor.
Description
The present invention relates to centrifuges for separating a
sludge-containing liquid and in which the rotor is provided along
its periphery with circumferentially spaced nozzles which are
permanently open to discharge sludge separated in the separating
chamber of the rotor.
A difficulty with centrifuges of this type is that the nozzles are
easily clogged if the sludge contains particles larger than the
inner diameter of the nozzles. The sludge concentration obtained in
the separation depends upon the number as well as the inner
diameter of the nozzles, since a reduced number of nozzles requires
an increased inner diameter of the nozzles. If, in order to avoid
this clogging of the nozzles, their inner diameter is increased and
consequently their number is reduced correspondingly, the sludge
cushions formed between the nozzles will grow faster radially
inward toward the periphery of the disc set and into the latter,
due to the bosh angle of the sludge. This means that the centrifuge
must be stopped more often for cleaning than when using the smaller
nozzles. Each cleaning of the centrifuge rotor requires dismounting
of the rotor and consequently troublesome and time-consuming work.
Different methods have been attempted for clean-flushing the
centrifuge rotor while keeping it in rotation, without reaching any
satisfactory solution of the problem.
According to the present invention, which aims at eliminating this
difficulty, the separating chamber of the centrifuge rotor has the
afore-mentioned nozzles, and the rotor is provided along its
periphery with one or more sludge outlet openings arranged to be
opened and closed by an axially movable piston valve. When using a
single sludge outlet opening, this opening can extend continuously
along the entire periphery of the rotor. The opening and closing
movements of the piston valve can be effected in a manner which is
conventional in the art.
The invention is described more in detail below with reference to
the accompanying drawing, in which the single illustration is an
axial sectional view of the left-hand half of an example of the new
centrifuge.
In the drawing, a centrifuge rotor 1 comprises an upper part 1a and
a lower part 1b which are clamped together by a lock ring 2. In the
rotor wall is a sludge outlet opening 3 and similar openings (not
shown) spaced around the periphery of the rotor, these openings
being opened and closed in a conventional manner by a valve piston
4. The latter has a plurality of holes passing radially through the
piston at its upper annular portion and spaced therearound to form
permanently open sludge outlet nozzles, one of these holes being
shown at 5. Alternatively, such holes may be formed in the upper
part 1a of the rotor body, as shown with dash-dotted lines at 5a.
The holes 5 or 5a open into the openings 3. When separating
bacteria from milk, the holes 5 can have a diameter of 0.4 mm; and
when separating baker's cottage cheese from sour coagulated skim
milk, these holes can have a diameter of 1.0 mm.
The rotor 1 is carried and driven by a hollow shaft 6, through the
central channel of which liquid to be separated is supplied to the
separating chamber of the rotor. The liquid enters this chamber
past the lower edge of a distributor 7. Separated sludge is thrown
outwardly through the holes 5; but between these holes (reckoned
peripherally) sludge deposits are eventually formed as indicated at
8. Purified liquid flows through a disc set 9 inwardly toward the
axis of the rotor and thence, via an overflow outlet 10, into a
paring chamber 11. The latter is provided with a stationary parting
disc 12 connected to an outlet pipe 13.
Assuming that baker's cottage cheese is to be separated from sour
coagulated skim milk, the skim milk is fed through the shaft 6 to
the separating chamber of the rotor and is divided into whey and
baker's cottage cheese. The whey passes inwardly and is discharged
by the paring disc 12, while the cheese passes outwardly toward the
periphery of the rotor for discharge through the holes 5 and the
openings 3. Despite this discharge through the holes 5, some of the
cheese deposits on the inner surface of the rotor periphery at its
regions located between the circumferentially spaced holes 5, so
that these deposits eventually form substantially conical cushions
each having its apex extending inwardly toward the periphery of the
disc set 9. These cheese cushions, however, must not be allowed to
grow into the disc set, since they would then impair the separation
efficiency of the centrifuge. To avoid such impairment without
having to stop the centrifuge rotor in order to dismount and clean
it, the openings 3 are opened by downward actuation of the valve
piston 4 without stopping the centrifuge rotor. Due to the
centrifuge force, the cheese cushions are then thrown out directly
through the openings 3; and after the valve piston 4 is returned to
its closing (upper) position as illustrated, the separation can be
continued.
In those cases where bacteria are separated from whole milk, a
layer of impurities settles along the inside of the rotor
periphery, and through this layer extend radial channels which are
formed just opposite the holes 5 and which remain open during the
separation course. Bacteria separated from the milk are thrown out
through these channels, as long as the sludge layer does not build
up sufficiently to reach the periphery of the disc set. To avoid
this build-up, the sludge layer may be discharged in the
afore-mentioned manner at suitable intervals (for example, 1
hour).
After a separation course has been completed, the centrifuge rotor
can be cleaned by opening the valve piston 4 while keeping the
rotor in continued rotation.
In the illustrated embodiment, the valve piston 4 is actuated
conventionally by varying the feed rate of an operating liquid from
a stationary duct 15 into an annular space 4a between the valve
piston 4 and the lower bowl part 1b, this liquid entering the space
4a near the rotor axis. To keep the piston 4 in its raised position
as shown, the space 4a is maintained completely filled with the
operating liquid despite a continual bleeding thereof through a
peripheral outlet 4b. Thus, the pressure of the operating liquid is
sufficient to hold the upper edge of the piston against the
opposing edge of the upper bowl part 1a, as shown at 16, thereby
preventing discharge directly through the openings 3. By
sufficiently reducing the flow rate from duct 15, the operating
liquid drains from space 4a through outlet 4b until the upward
pressure on piston 4 is diminished enough to allow lowering thereof
under the pressure exerted by the contents of the separating
chamber, whereupon the openings 3 are unblocked for direct
discharge therethrough independently of the holes 5. Piston 4 is
returned to its raised (closing) position by increasing the feed
rate from duct 15 so as to re-fill the space 4a.
* * * * *