U.S. patent number 3,771,715 [Application Number 05/201,314] was granted by the patent office on 1973-11-13 for self-cleaning centrifugal separator.
This patent grant is currently assigned to Escher Wyss Aktiengesellschaft. Invention is credited to Martin Baram.
United States Patent |
3,771,715 |
Baram |
November 13, 1973 |
SELF-CLEANING CENTRIFUGAL SEPARATOR
Abstract
Fluid controlled pulsations of one or several elastic and or
pliable annular membrane linings in a centrifugal separator,
preferably of the "Decanter"-type, to transport precipitated sludge
and solids to ejection openings.
Inventors: |
Baram; Martin (Brondy Strand,
DK) |
Assignee: |
Escher Wyss Aktiengesellschaft
(Zurich, CH)
|
Family
ID: |
8146640 |
Appl.
No.: |
05/201,314 |
Filed: |
November 23, 1971 |
Foreign Application Priority Data
|
|
|
|
|
Nov 24, 1970 [DK] |
|
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5989/70 |
|
Current U.S.
Class: |
494/11; 494/27;
494/50; 494/81 |
Current CPC
Class: |
B04B
11/04 (20130101); B04B 15/06 (20130101) |
Current International
Class: |
B04B
15/06 (20060101); B04B 11/00 (20060101); B04B
11/04 (20060101); B04B 15/00 (20060101); B04b
001/00 () |
Field of
Search: |
;233/3,9,19R,19A,2R,2A,27,28,46 ;210/211,74 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Krizmanich; George H.
Claims
What is claimed is:
1. A centrifugal separator comprising a conical bowl having an
inner surface presenting a wide end and a narrow end opposite
thereto, means for delivering a fluid-sledge mixture into said
bowl, in which the bowl is provided with discharge opening means at
said wide end for discharging fluid phase of said mixture and
discharge means at said narrow end for discharging a precipitated
sludge of said fluid-sludge mixture while the fluid phase leaves
the bowl via the wide end, a plurality of ring-shaped elastic
membrane sections covering said inner wall of the bowl, means
engaging opposite ends of said sections in fluid tight relation to
said inner surface for allowing said sections to be inwardly flexed
therebetween, the bowl being provided with an opening below each
membrane section, and means connected with said openings for the
supply and the withdrawal of a pressure fluid to flex and release
said sections and including means for controlling the supply and
withdrawal of the pressure fluid such that when supplying pressure
fluid the membrane section are flexed away from the wall of the
bowl in a predetermined sequence which progresses from the wide
toward the narrow end of the bowl thereby to effect discharge of
said sludge while the mixture is still being delivered to the bowl
and the fluid phase is being discharged, said membrane sections
being detailed in design so that at least a part of the surface of
each ring-shaped membrane section when flexed is slanted toward
said narrow end of the bowl where the precipitated sludge is
ejected.
2. Centrifugal separator according to claim 1 in which the inner
surface of the bowl is provided with adjacent open annular grooves,
said membrane sections being in fluid tight connection with the
rims of the grooves, the membrane sections following the shape of
the grooves when the membrane is not pressurized.
3. Centrifugal separator according to claim 1 in which the
ring-shaped sections are divided in two or more groups, each group
being connected with a common supply for pressure fluid, such that
the groups can be pressurized at will.
4. Centrifugal separator according to claim 1 characterized in that
only the membrane section lying at the end remote from the end
where the precipitated sludge is ejected is directly connected with
the supply for pressurized fluid, each section communicating with
the adjacent section through a duct with a flow restriction.
5. Centrifugal separator according to claim 1 in which the several
membrane sections are combined to one single membrane extending
through the whole length of the bowl of the separator.
6. Centrifugal separator according to claim 5 in which the membrane
between the ring-shaped sections is connected with the wall of the
bowl.
7. Centrifugal separator according to claim 5 in which the membrane
between the ring-shaped membrane sections has a portion which is
less elastic than the material of the membrane sections
themselves.
8. Centrifugal separator according to claim 5 in which the
separator consists of ring-shaped segments which are combined to
centrifugal units of predetermined length.
9. A centrifugal separator comprising, in combination:
a horizontally elongate drum and means for supporting said drum for
rotation about its longitudinal axis, said drum having an interior
surface defining a chamber which decreases in diameter from one end
of the drum to the opposite end thereof;
fluid outlet means at said one end of the drum;
solids outlet means at said opposite end of the drum;
means for introducing a fluid-solids mixture into said chamber;
membrane means on said interior surface of the drum; and
means for periodically deforming said membrane means to work
centrifugally separated solids toward said opposite end of the
drum.
10. The centrifugal separator as defined in claim 9 wherein said
means for periodically deforming said membrane means comprises a
pressure fluid-conveying system communicating with the interface
between said interior surface and said membrane means, and means
for periodically conveying pressure fluid to such interface.
11. The centrifugal separator as defined in claim 10 wherein said
pressure fluid-conveying system includes means for conveying
pressure fluid to different longitudinal sections of said drum in
time-delayed relation from said one end of the drum to said
opposite end thereof.
12. The centrifugal separator as defined in claim 10 wherein the
interior surface of said drum is formed as a series of
frusto-conical sections.
13. The centrifugal separator as defined in claim 12 wherein said
pressure fluid-conveying system communicates with interfaces at
alternate ones of said frusto-conical sections.
14. The centrifugal separator as defined in claim 10 wherein said
pressure fluid conveying system includes inlet means, discharge
means having a restricted opeining, and means for introducing
pressure fluid through said inlet means alternately at rates
exceeding and less than the rate at which pressure fluid escapes
through said restricted opening.
15. The centrifugal separator as defined in claim 9 including
anchoring means spaced longitudinally of said drum for anchoring
said membrane means to the interior surface of said drum, said
interior surface of the drum and those portions of the membrane
means between said anchoring means being detailed in design to
allow said solids to be worked toward and discharged from said
opposite end of the drum without affecting the normal centrifugal
separating action of the separator.
16. The centrifugal separator as defined in claim 15 wherein said
means for periodically deforming said membrane means comprises a
pressure fluid-conveying system communicating with the interfaces
between said portions of the membrane means between said anchoring
means and said interior surface of the drum.
17. The centrifugal separator as defined in claim 16 wherein said
pressure fluid-conveying system includes means for conveying
pressure fluid to different longitudinal sections of said drum in
time-delayed relation from said one end of the drum to said
opposite end thereof.
18. The centrifugal separator as defined in claim 16 wherein said
pressure fluid-conveying system includes means for conveying
pressure fluid to different longitudinal sections of said drum in
time-delayed relation from said one end of the drum to said
opposite end thereof.
19. The centrifugal separator as defined in claim 15 wherein the
interior surface of said drum is formed as a series of
frusto-conical sections.
20. The centrifugal separator as defined in claim 15 wherein each
of said portions of the membrane means is of annular form and of
V-shaped cross section.
21. The centrifugal separator as defined in claim 9 wherein said
membrane means comprises a plurality of annular sections each of
generally V-shaped cross section, and including anchoring means
attaching the opposite edges of each such annular section to the
interior surface of said drum.
22. The centrifugal separator as defined in claim 21 wherein said
means for periodically deforming said membrane means comprises a
pressure fluid-conveying system communicating with the interfaces
between said portions of the membrane means between said anchoring
means and said interior surface of the drum.
23. The centrifugal separator as defined in claim 22 wherein said
pressure fluid-conveying system includes means for conveying
pressure fluid to different longitudinal sections of said drum in
time-delayed relation from said one end of the drum to said
opposite end thereof.
24. The centrifugal separator as defined in claim 21 wherein said
interior surface of the drum is formed as a series of
frusto-conical sections mating with said V-shaped annular sections
of the membrane means.
25. A centrifugal separator as defined in claim 9 wherein said
means for introducing said fluid-solids mixture continuously
maintains a body of fluid in said chamber which terminates short of
said opposite end thereof whereby separation of said solids from
said fluid phase and discharge of said fluid phase occur
continuously and discharge of said solids occurs during such
continuous separation and such continuous discharge of fluid phase.
Description
BACKGROUND OF THE INVENTION
The present invention relates to new fluid controlled annular
membrane linings to be used in particular but not exclusively in
connection with a centrifugal separator with conical bowl and
usually supported in a horizontal position where the precipitated
sludge of a fluid-sludge mixture is conveyed to the narrow end of
the bowl to one or several ejection openings, while the fluid phase
leaves the bowl via the wide end. It is known in the art to employ
centrifugal separators with a bowl of a generally conical shape and
incorporating a conveyor screw in a coaxial position. Bowl and
screw rotate at different speeds, and thus the peripheral windings
of the screw scrape most of the sludge along the inner surface of
the bowl towards one or several ejection openings at the narrow end
of the bowl. This construction suffers from several serious
drawbacks such as:
1. the conveyor screw is a very expensive part to fabricate;
2. the peripheral edge of the conveyor screw is worn away
relatively quickly resulting in expensive work stoppage and
repairs;
3. the difference in speeds of bowl and conveyor screw respectively
demands expensive and damage prone differential gears or equivalent
mechanical means;
4. because of the necessary gap between the wall of the bowl and
the periphery of the conveyor screw not all the sludge is moved but
a thin compressed layer of solids is always left behind prone to
bacterial contamination and unwanted chemical processes;
5. the conveyor screw stirs up already settled sludge and smashes
advantageous coagulations; and
6. this kind of machine works at a very high noise level.
SUMMARY OF THE INVENTION
The object of the present invention is to eliminate conveyor screw
and differential gears, and to substitute instead one or several
membrane linings of a suitably resilient and or pliable material
capable to generate pulsating movements in a predetermined
direction and able to propel precipitated sludge and solids in a
predetermined direction.
Another object of the invention is to provide a centrifugal bowl
furnished with adjacent open annular grooves which in connection
with the annular membrane linings or lining form annular pockets
for sludge and solids when deflated, and profilated chambers with
slanting outer surfaces when inflated by a control fluid
respectively.
A further object of the invention is to provide an advantageous
hydraulic system incorporated in the bowl and or the membrane
lining to generate predetermined pulsation sequences.
These and other novel features and advantages of the present
invention will be described and defined in the following
specification and claims.
BRIEF DESCRIPTION OF DRAWINGS
FIG. 1 is a diagrammatic vertical sectional view of a centrifugal
separator furnished with a membrane lining of the present
invention, shown only in the upper half of the bowl in connection
with suitably shaped adjacent open annular grooves of the present
invention, the latter being shown without membrane lining in the
lower half of the bowl;
FIG. 2 is an enlarged diagrammatic detail in vertical sectional
view of the bowl with membrane lining illustrating by way of
example a way of securing the lining to the bowl;
FIG. 3 is a diagrammatical sectional view of a special type of
lining attached to a bowl without said annular grooves; and
FIG. 4 is a diagrammatical sectional view of another embodiment
according to the invention.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
Referring more specifically to the drawing in FIG. 1 is shown a
centrifugal separator bowl 1 with end sections 2 and 3 which are
furnished with hollow shafts 4 and 5 respectively, said bowl and
shafts 1, 2, 3 rotating in connection with suitable bearings,
supports and driving means not shown in the drawing.
The inner surface of bowl 1 is furnished with adjacent open annular
grooves 6 each being covered by an annular membrane lining 7. All
linings will preferably be integrated into one single membrane
lining 8 as indicated in the drawing made of a suitably pliable and
or elastic material. In the drawing, the individual membrane
linings 7 are shown alternatingly in a deflated and in an inflated
condition, thus either forming a kind of annular pocket together
with grooves 6 or forming inflated chambers under the influence of
a control fluid injected through channels 9 belonging to control
fluid conduits 10 or 11 which are connected to annular fluid
chambers 12 and 13 respectively which in turn are supplied through
stationary pipes 14 and 15 respectively inserted through hollow
shaft 4. Fluid conduits 10 and 11 are also furnished with
evacuation valves 16 and 17 respectively. The sludge-fluid mixture
to be separated enters the bowl 1 through a stationary pipe 18
projecting through hollow shaft 5. Pipes 14, 15 and 18 need no
expensive means of tightening such as packings. The clean phase
leaves the bowl 1 through openings 19 while the sludge is ejected
through openings 20. When under the influence of the control fluid
linings 7 will be inflated to form outer surfaces 21 which slant
downwardly in the direction of ejection openings 20.
FIG. 2 exemplifies means of securing membrane linings 7 or lining 8
to the bowl 1. At every top of grooves 6 a further narrow groove is
provided to house a suitably formed part or lip of linings 7 or 8
respectively under the pressure of an expandable ring 22 of steel
or other suitably resilient and strong material. Rings 22 may have
advantageous slanting outer surfaces.
FIG. 3 illustrates the employment of an outer lining 23 preferably
of the same material as the membrane linings 7 or 8 respectively,
these parts being bonded together by way of example by welding
along seams 24. The outer lining 23 needs only to be fastened at
its ends near end sections 2 and 3. Thus, the inside of bowl 1
needs no expensive machining.
Returning to FIG. 1, bowl 1 is shown to include an alternative
fluid conduit 25 which is in direct connection with the first
channel 9 and from there through a short length of conduit 11 to
chamber 13. A bowl of this type has neither chamber 12, conduit 10
with its channels 9 and valve 16 nor the rest of conduit 11. Pipe
14 is not needed. Conduits 25 may be holes interconnecting grooves
6 or open channels milled through the tops of the grooves.
OPERATION
Regardless of whether the embodiment of the invention is as shown
in FIG. 1 or FIG. 3, the centrifugal separator may work as
follows:
When bowl 1 rotates at full speed control fluid is injected through
both fluid systems at the same time. Thus, all linings 7 will be
inflated and will act as accelerators on the sludge-fluid mixture
fed through pipe 18 provided the supply of control fluid exceeds
the constant losses through valves 16 and 17. At a certain moment,
the supply of control fluid is stopped for example through pipe 14
as shown in FIG. 1 causing the fluid in conduit 10 and its channels
9 to leave through valve 16. As a result, the particular membrane
linings 7 subside into their grooves 6 forming annular pockets to
receive sludge sliding down from slanting surfaces 21 in addition
to the sludge already deposited therein. After a suitable interval,
this procedure is reversed, the fluid supply through pipe 15 is
stopped, the fluid pressure falls through valve 17 and pipe 14 is
opened. In this manner, the sludge deposited in the subsided
membrane lining pockets will be lifted up by the expanding membrane
7 and transferred into the annular pocket next to it. In this
manner, all sludge will be propelled through the length of the bowl
1 towards openings 20.
In FIG. 4, the bowl 1 incorporates only control fluid conduit 26
with one channel 25 and part of conduit 10 with chamber 12 and
supply pipe 15, the transportation of the sludge will be obtained
by intermittent opening and closing of pipe 15. As pipe 15 is
opened, the control fluid will run through said conduits into the
first groove 6. Conduits 26 must be dimensioned in such a manner
that the first membrane lining is expanded entirely before the
adjacent membrane lining changes considerably from its pocket shape
inside groove 6. In this manner, membrane linings 7 will expand one
after the other like a wave rolling through the length of bowl 1
propelling all the deposited sludge before it towards openings
20.
When the control fluid supply is closed, the hydrostatic pressure
inside the fluid conduits will be evacuated through valve 17, and
all the members linings 7 will subside into the grooves 6. This
procedure can be repeated at predetermined intervals. The scope of
the present invention is not necessarily limited to parallel
annular grooves 6. Especially in connection with said
wave-principle propulsion, it is possible to use one single groove
spiralling through the length of the bowl beginning in connection
with channel 9 and ending blindly near openings 20. This feature
applies also to the embodiment shown in FIG. 3. The scope of the
present invention also embraces the employment of a membrane lining
which is inflatable in a rolling wave fashion without any grooves
either in the wall of the bowl or integrated in outer lining 23. In
that case, the lining will have suitably elastic and or pliable
parts either parallel and adjacent to each other or in the shape of
a spiral acting as a rolling wave by expanding progressively under
the influence of the progressively advancing control fluid as
described above.
While the preferred embodiments of the present invention have been
shown and described herein, it is obvious that many structural
details may be changed without departing from the spirit and scope
of the appended claims .
* * * * *