[0001] The present invention relates to a centrifugal separator for treating sludges, suspensions
and, in general, mixes of substances in the liquid phase and substances in the solid
phase, adapted to separate more or less accurately the liquid phase from the solid
phase.
[0002] Known types of centrifugal separator consists of a drum which rotates at high speed
and is provided with an internal screw feeder. The loaded sludge undergoes centrifugation,
during which the phases stratify; the phase with highest density (solid phase) is
arranged on the outermost annular region.
[0003] The screw feeder rotates at a different rate with respect to the drum and entrains
the solid phase toward the discharge. The water (liquid phase) exits from the opposite
side.
[0004] Known types of centrifugal separator have several drawbacks.
[0005] First of all, the liquid phase discharged by the separator is generally rather rich
in the solid sediments: this means that the separation process does not ensure the
result of correct separation of the solid phase from the liquid phase. When separation
is required by environmental needs (separation of pollutants) or by the need to recover
valuable material (treatment of mining sludges), it is absolutely necessary for the
separation to be as thorough as possible.
[0006] Secondly, it should be noted that continuous settling of solid material occurs along
the path of the discharge of the liquid phase and leads, in the medium and long term,
to obstruction of such path.
[0007] It is therefore necessary to provide continuous maintenance to clean the path: these
operations must provide for a rather complex machine architecture in order to ensure
easy access to the path to be cleaned. This constructive architecture necessarily
causes an increase in the production and design costs of the machine.
[0008] The aim of the present invention is to provide a centrifugal separator which is suitable
for high-performance separation of the solid phase and of the liquid phase of a mix.
[0009] Within this aim, an object of the present invention is to provide a centrifugal separator
in which settling of the solid phase along the liquid phase expulsion path does not
occur.
[0010] Another object of the present invention is to provide a centrifugal separator which
can be operated easily, since it does not require particular maintenance.
[0011] Another object of the present invention is to provide a centrifugal separator with
an architecture which is particularly simple and can be assembled easily.
[0012] Another object of the present invention is to provide a centrifugal separator which
has low costs, is relatively simple to provide in practice and is safe in application.
[0013] This aim and these and other objects, which will become better apparent hereinafter,
are achieved by the present centrifugal separator, of the type that comprises an outer
casing, within which at least one hollow drum is actuated so that it can rotate, at
least one screw feeder which is actuated so that it can rotate, at a speed which is
substantially higher than the speed of the respective drum, within said drum, skimming
its internal surfaces, a circuit for feeding a solid-liquid mix and respective circuits
for the separate expulsion of the solid phase and of the liquid phase,
characterized in that the mix feed circuit comprises an inlet and a respective channel which leads out
along at least one portion of the internal surface of said drum to dispense mix along
the internal surface of said rotatable drum.
[0014] Further characteristics and advantages of the invention will become better apparent
and evident from the following detailed description of a preferred but not exclusive
embodiment of a centrifugal separator, illustrated by way of non-limiting example
in the accompanying drawings, wherein:
Figure 1 is a sectional front view, taken along an axial longitudinal plane, of a
centrifugal separator according to the invention;
Figure 2 is an enlarged-scale sectional front view, taken along an axial longitudinal
plane, of a detail of a centrifugal separator according to the invention.
[0015] With reference to the figures, the reference numeral 1 generally designates a centrifugal
separator according to the invention.
[0016] A particularly simple and efficient embodiment is described hereafter: any structural
complication that entails the adoption of multiple equivalent components and/or the
partial use of the components that are present is to be understood as being comprised
in any case within the scope of the present description.
[0017] The centrifugal separator 1 comprises an outer casing 2, within which a hollow drum
3 is actuated so that it can rotate: with reference to the general nature of the description,
for example, the separator 1 might also comprise a plurality of mutually independent
drums 3 contained within a common casing 2 or within respective separate casings 2.
[0018] A first screw feeder 4 is actuated so that it can rotate, at a speed which is substantially
higher than the speed of the respective drum 3, inside the drum 3 itself; the first
screw feeder 4, during its relative rotation with respect to the corresponding drum
3, skins internal surfaces 5 thereof.
[0019] This relative motion is intended to convey the solids toward the outlet.
[0020] The same result can be achieved by working on the following parameters:
- direction of rotation
- turn winding direction
- relative speed of the screw feeder 4 and of the drum 3
[0021] The possible combinations for achieving correct operation (and therefore the desired
outflow of the solids) are the following:
➢ screw feeder 4 with right-handed helix, operating condition in which the drum 3
is faster than the screw feeder 4 with a clockwise rotation (if viewed from the liquid
discharge region);
➢ screw feeder 4 with right-handed helix, operating condition in which the drum 3
is slower than the screw feeder 4 with a counterclockwise rotation (if viewed from
the liquid discharge region);
➢ screw feeder 4 with left-handed helix, operating condition in which the drum 3 is
slower than the screw feeder 4 with a clockwise rotation (if viewed from the liquid
discharge region);
➢ screw feeder 4 with left-handed helix, operating condition in which the drum 3 is
faster than the screw feeder 4 with a counterclockwise rotation (if viewed from the
liquid discharge region).
[0022] Although only one of these constructive solutions is described in detail, it is evident
that they are equivalent from a mechanical standpoint and therefore are fully within
the scope of the protection of the present invention.
[0023] The separator 1 further comprises a circuit 6 for feeding a solid-liquid fit mix
and respective circuits for separate expulsion of the solid phase and of the liquid
phase.
[0024] The solid-liquid mix can be of different kinds: in particular, the separator 1 according
to the invention is suitable for treating sludge and the like, but use with other
mixes of another kind which require separation of the solid phase from the liquid
phase is not excluded.
[0025] It is noted that the separators 1 are particularly suitable for treating mixes for
purification purposes (therefore environmental use and the like) and for selection
purposes (use in mines or other plants adapted to provide a raw material which contains
a small part of valuable material to be selected).
[0026] In the centrifugal separator 1 according to the invention, the mix feed circuit 6
comprises an inlet 7 and a respective channel 8 which leads out along at least one
portion 9 of the internal surface 5 of the drum 3: this embodiment allows the delivery
of mix along the internal surface 5, proximate to its initial edge 10, of the rotating
drum 3.
[0027] This constructive choice to provide the separator 1 with the mix directly proximate
to the internal surface of the drum 3 allows to facilitate the immediate stratification
of the mix, with consequent centrifugal separation of the solid phase from the liquid
phase. In known types of separator, the mix is introduced coaxially with respect to
the drum and this entails a subsequent transfer by centrifugal action of such mix
toward the walls of the drum: of course, a transfer of the mix in this manner entails
the onset of turbulence which compromises the desired solid/liquid stratification.
[0028] Determining a constructive architecture in which the mix is dispensed directly in
the separator 1 proximate to the internal surface 5 of the drum 3 ensures that an
optimum centrifugal stratification is achieved immediately, minimizing interference
caused by any turbulence and the like.
[0029] In particular, the feed circuit 6 comprises one inlet 7 which is arranged at one
end 11 of the casing 2.
[0030] The end 11 is opposite to an end 12 in which an opening 13 for expelling the solid
phase is located.
[0031] The inlet 7 leads, by means of the respective channel 8, to an annular chamber 14,
which lies inside the casing 2 and the drum 3. The chamber 14 is adapted to force
the translational motion of the introduced mix in a radial direction by centrifugal
action toward the portion 9 of the internal wall 5 of the drum 3.
[0032] The annular input chamber 14 is arranged upstream of the beginning of a first start
15 of the first screw feeder 4.
[0033] The circuit for expelling the liquid phase comprises a channel 16, which is coaxial
to the at least one first screw feeder 4 and lies inside it in its portion located
further upstream. The channel 16 is adapted to convey the liquid phase with an axial
orientation with respect to the rotation axis of the separator 1 and in the opposite
direction with respect to the advancement direction of the solid phase on the drum
3 by way of the action of the first screw feeder 4.
[0034] In particular, the channel 16 comprises at least one portion of at least one second
screw feeder 17, in which the crests face, and are proximate to, an internal surface
18 of the channel 16 to remove any solid sediment from the surface 18 and to convey
the removed sediment toward the main screw feeder 4. Continuous removal of sediment
by the crests of the second screw feeder 17 from the internal surface 18 of the channel
16 ensures that such sediment does not accumulate and therefore that the operation
of the separator 1 is not compromised by the presence of solid sediment in the liquid
phase discharge channel 16. In practice, this solution entails the possibility to
reduce greatly maintenance interventions (aimed at cleaning the liquid phase discharge
channel) and therefore allows less expensive and simpler operation than known types
of separator.
[0035] It should be noted that the second screw feeder 17, in an embodiment of particular
interest in practice and in application, is constituted by a ribbonlike ring which
is arranged in a helical pattern on a plurality of radial supporting arms which extend
from the channel 16: this embodiment ensures that a channel 16 of large size is available
although the second screw feeder 17 designed to remove the sediment from the surface
18 is present.
[0036] The drum 3 and the first screw feeder 4 have a first upstream portion 19 which is
substantially cylindrical and a second downstream portion 20 which is substantially
frustum-shaped.
[0037] The first portion 19 is arranged directly downstream of the region where the mix
is introduced by the feed circuit 6, while the second portion 20 has its end part
substantially aligned with the opening 13 for expelling the solid phase.
[0038] The crest of the first screw feeder 4 faces, and is proximate to, the internal surface
5 of the drum 3, while the crest of the second screw feeder 17 faces, and is proximate
to, the internal surface 18 of the channel 16.
[0039] During operation, both crests skim the corresponding surfaces 5 and 18 to remove
and convey the solid phase deposited thereon.
[0040] The first screw feeder comprises, at a part 21 of the first portion 19, at least
one tubular portion 22, within which the second screw feeder 17 is accommodated so
that it can rotate.
[0041] The second screw feeder 17 is jointly connected to the corresponding drum 3; the
corresponding crests therefore slide proximate to the internal surface of the tubular
portion 22 of the first screw feeder 4: the starts of the second screw feeder 17 are
arranged in a helical winding direction which is opposite with respect to the direction
of the first screw feeder 4.
[0042] A relative speed of the first screw feeder 4 with respect to the drum 3 causes an
advancement, toward the respective expulsion opening 13, of the solid phase, in the
drum 3, by way of the action of the first screw feeder 4, and in the tubular portion
22, by way of the action of the second screw feeder 17. A positive relative speed
(which therefore corresponds to a higher rotation rate for the screw feeder 4 with
respect to the drum 3) in fact entails entrainment toward the opening 13 of the solid
matter comprised between the starts of the first screw feeder 4. Simultaneously, the
relative speed is such that the tubular portion 22 (connected to the first screw feeder
4) move at a higher speed than the second screw feeder 17 (the relative speed is therefore
negative in this case): since the helical winding direction is opposite with respect
to the one of the first screw feeder 4, transfer of the sediment that is present on
the surface of the channel 16 (internal surface of the portion 22) toward the opening
13 still occurs.
[0043] The separator 1 further comprises at least one external traction unit (not shown
in the figure), which is intended to drive rotationally the drum 3, jointly with the
second screw feeder 17, and the first screw feeder 4.
[0044] In particular, it is possible to adopt a single unit which is associated with respective
pulleys 23 and 24 having different diameters, one pulley 23 being coupled to the drum
3 and to the second screw feeder 17 and the other pulley 24 being coupled to the first
screw feeder 4.
[0045] The different diameter of the pulleys 23, 24 determines the different rotation rate
of the drum 3 with respect to the first screw feeder 4.
[0046] Introduction of the mix through the circuit 6 entails that such mix flows by way
of the action of the first screw feeder along the part 21 until it reaches the end
of the first upstream portion 19.
[0047] At the end of the portion 19 there are passages 25 designed to allow the outflow
of the liquid phase through the respective channel 16.
[0048] The remaining solid phase continues to be entrained by the first screw feeder 4 to
the opening 13: the centrifugal action contributes, throughout the entrainment, to
separate from the solid phase the liquid phase, which tends to retract to be then
expelled through the channel 16.
[0049] The second screw feeder 17 (by way of its relative movement with respect to the walls
of the channel constituted by the internal surface of the tubular portion 22 of the
screw feeder 4) removes sediment from the surfaces that face it.
[0050] It has thus been shown that the invention achieves the proposed aim and objects.
[0051] The invention thus conceived is susceptible of numerous modifications and variations,
all of which are within the scope of the appended claims.
[0052] All the details may further be replaced with other technically equivalent ones.
[0053] In the exemplary embodiments shown, individual characteristics, given in relation
to specific examples, may actually be interchanged with other different characteristics
that exist in other exemplary embodiments.
[0054] Moreover, it is noted that anything found to be already known during the patenting
process is understood not to be claimed and to be the subject of a disclaimer.
[0055] In practice, the materials used, as well as the shapes and dimensions, may be any
according to requirements without thereby abandoning the scope of the protection of
the appended claims.
[0056] Where technical features mentioned in any claim are followed by reference signs,
those reference signs have been included for the sole purpose of increasing the intelligibility
of the claims and accordingly such reference signs do not have any limiting effect
on the interpretation of each element identified by way of example by such reference
signs.
1. A centrifugal separator (1), of the type that comprises an outer casing (2), within
which at least one hollow drum (3) is actuated so that it can rotate, at least one
first screw feeder (4) which is actuated so that it can rotate, at a speed which is
substantially higher than the speed of the respective drum (3), within said drum (3),
skimming its internal surfaces (5), a circuit (6) for feeding a solid-liquid mix and
respective circuits for the separate expulsion of the solid phase and of the liquid
phase, characterized in that the mix feed circuit (6) comprises an inlet (7) and a respective channel (8) which
leads out along at least one portion (9) of the internal surface (5) of said drum
(3) to dispense mix along the internal surface (5) of said rotatable drum (3).
2. The centrifugal separator according to claim 1, characterized in that said feed circuit (6) comprises an inlet (7) which is arranged at an end (11) of
said casing (2), said end (11) being arranged opposite the end (12) in which the opening
(13) for expelling the solid phase is arranged, said inlet (7) leading, by means of
a channel (8), to an annular chamber (14) which lies inside said casing (2) and said
at least one drum (3), said chamber (14) being adapted to impose a translational motion
in a radial direction by centrifugal action, toward at least one portion (9) of the
internal wall (5) of said at least one drum (3), of the introduced mix.
3. The centrifugal separator according to claim 2, characterized in that said annular intake chamber (14) is arranged upstream of the beginning of the first
start (15) of said at least one first screw feeder (4).
4. The centrifugal separator according to claim 1, characterized in that said circuit for expelling the liquid phase comprises a channel (16) which is coaxial
to said at least one first screw feeder (4) and is internal thereto in its portion
located further upstream, said channel (16) being adapted to convey said separated
liquid phase in an axial orientation with respect to the rotation axis of the separator
(1) and in the opposite direction with respect to the advancement direction of said
solid phase on the at least one drum (3) by way of the action of said at least one
first screw feeder (4).
5. The centrifugal separator according to claim 4, characterized in that said channel (16) comprises at least one portion of at least one second screw feeder
(17) whose crests face, and lie proximate to, the internal surface (18) of said channel
(16) for the removal of any solid sediment from said surface (18) and for the conveyance
of said removed sediment towards the at least one first main screw feeder (4).
6. The centrifugal separator according to claim 1, characterized in that said at least one drum (3) and said corresponding at least one first screw feeder
(4) have a first upstream portion (19) which is substantially cylindrical and a second
downstream portion (20) which is substantially frustum-shaped, said first portion
(19) being arranged directly downstream of the region where the mix is introduced
by said feed circuit (6) and said second portion (20) having its end part which is
substantially aligned with an opening (13) for expelling the solid phase.
7. The centrifugal separator according to claim 1, characterized in that the crest of said at least one first screw feeder (4) and the crest of said at least
one second screw feeder (17) face, and lie proximate to, respectively the internal
surface (5) of said drum (3) and to the internal surface (18) of said channel (16),
skimming, during the operation of said separator (1), said surfaces (5) and (18) to
remove and convey the solid phase deposited thereon.
8. The centrifugal separator according to one or more of the preceding claims, characterized in that said at least one first screw feeder (4) comprises, at a part (21) of said first
portion (19), at least one tubular portion (22), within which the at least one second
screw feeder (17) is accommodated so that it can rotate.
9. The centrifugal separator according to one or more of the preceding claims, characterized in that said at least one second screw feeder (17) is coupled to the corresponding drum (3),
the corresponding crests sliding proximate to the internal surface (18) of said tubular
portion (22) of said first screw feeder (4), the starts of said at least one second
screw feeder (17) being arranged in the opposite direction with respect to the starts
(15) of said at least one first screw feeder (4), a relative speed of the first screw
feeder (4) with respect to the drum (3) producing an advancement, toward the respective
expulsion opening (13), of the solid phase in the drum (3) by way of the action of
the at least one first screw feeder (4) and in the tubular portion (22) by way of
the action of the at least one second screw feeder (17).
10. The centrifugal separator according to one or more of the preceding claims, characterized in that it comprises at least one external traction unit which is intended to entrain rotationally
said at least one hollow drum (3) jointly with the at least one second screw feeder
(17) and said at least one first screw feeder (4).
11. The centrifugal separator according to the preceding claim, characterized in that said unit is a single unit and is associated with respective pulleys (23, 24) having
different diameters, one pulley (23) being coupled to said at least one drum (3) and
to said second screw feeder (17) and the other pulley (24) being coupled to said first
screw feeder (4), the different diameter of the pulleys (23, 24) determining the different
rotation rate of the at least one drum (3) with respect to the at least one first
screw feeder (4).