EP0520010A1

EP0520010A1 - Decanter centrifuge.

Info

Publication number: EP0520010A1
Application number: EP91906597A
Authority: EP
Inventors: Bent Madsen
Original assignee: Alfa Laval Separation AS
Current assignee: Alfa Laval Copenhagen AS
Priority date: 1990-03-13
Filing date: 1991-03-12
Publication date: 1992-12-30
Anticipated expiration: 2011-03-12
Also published as: DE69104715D1; WO1991013686A1; DK65190A; DK170967B1; EP0520010B1; JPH05505557A; DK65190D0; DE69104715T2; JP2987519B2

Abstract

Séparateur centrifuge constitué d'un tambour (1) renfermant un convoyeur (2) au centre duquel est logé la chambre d'admission (4). Le flux de liquide à séparer s'écoule selon l'axe de la chambre d'admission (4) vers le fond (11) de celui-ci avant d'être réparti radialement et continuer de s'écouler à nouveau de manière axiale vers la deuxième extrémité (13) de la chambre d'admission en franchissant un secteur ne comportant pas d'ailettes qui communiqueraient au liquide une vitesse angulaire. La chambre d'admission (4) comporte des lumières (6) situées en un rayon supérieur à celui du débord (9) par lequel le liquide se déverse. La configuration de la chambre (4) est telle qu'en cours d'opération la surface libre du liquide est entraînée assez loin le long de l'axe du tambour, de sorte que l'excédent d'énergie communiqué au liquide lors de son accélération à la vitesse angulaire du convoyeur (2) est dissipée dans une couche de liquide assez épaisse avant que le liquide ne se déverse dans la chambre de séparation (1) via les lumières (6).Centrifugal separator consisting of a drum (1) containing a conveyor (2) in the center of which is housed the inlet chamber (4). The flow of liquid to be separated flows along the axis of the inlet chamber (4) towards the bottom (11) of the latter before being distributed radially and continuing to flow again axially towards the second end (13) of the inlet chamber crossing a sector having no fins which would communicate an angular velocity to the liquid. The inlet chamber (4) has slots (6) located at a radius greater than that of the overhang (9) through which the liquid flows. The configuration of the chamber (4) is such that during operation the free surface of the liquid is driven far enough along the axis of the drum, so that the excess energy imparted to the liquid during its acceleration to the angular speed of the conveyor (2) is dissipated in a fairly thick layer of liquid before the liquid flows into the separation chamber (1) via the ports (6).

Description

Decanter centrifuge.

The invention relates to a decanter centrifuge comprising a rotatably journalled drum and a conveyor rotatably journalled in the drum with a conveyor body containing an inlet in the form of a cavity for the feed to be separated, said inlet being radially defined by a wall coaxial with the conveyor body and provided with inlet apertures connecting the inlet with the space between the conveyor body and the internal side of the drum, a peripheral area of the inlet outwardly defined by the radius to the inlet apertures being free of carriers, inwards extending projections or the like, an inlet pipe for the feed coaxial with the drum, and at one end of the drum an outlet weir for the separated liquid phase.

GB patent No. 1 025 079 describes a decanter centrifuge of the above type in which the inlet is radially defined by a circular-cylindrical wall and axially defined at one end by an end wall forming a conical surface with an opening for an inlet pipe projecting into the inlet and whose orifice is located at the small end of the conical surface and points in a direction perpendicular to the drum axis. A large number of inlet apertures is distributed in the circular-cylindrical radial wall.

The decanter centrifuge further includes a supply pipe for a flocculant. Said supply pipe is inserted into the inlet through the inlet pipe and is concentric therewith. The purpose of the supply pipe is to allow the flocculant to be added to the feed after the feed has been accelerated to an angular velocity substantially corresponding to the angular velocity of the drum. In previous centrifuges the flocculant was added to the feed prior to the feed entering the inlet. This resulted in that the feed containing the floccul ant was exposed to large internal shear forces during acceleration to said angular velocity, thereby causing already precipitated material to be disintegrated again.

US patent No. 3 143 504 describes another decanter centrifuge of the above type in which the inlet is radially defined by a circularly cylindrical wall and axially by an end wall that is plane and perpendicular to the drum axis, while a second end wall forms a conical surface with an opening for an inlet pipe projecting into the inlet and whose orifice is situated in a plane parallel to the drum axis. A large number of inlet apertures for discharging sediment is distributed over the circularly cylindrical wall and inlet apertures are provided in the plane end wall through which the liquid phase leaves the inlet.

In both of said prior art decanter centrifuges the feed flows or falls from the inlet pipe directly onto the conical surface of the second end wall where it is accelerated in a fraction of a second to the same angular velocity as the conveyor. Due to the position of the overflow edge a thin liquid layer settles on the inner wall of the inlet in which an initial separation takes place. The separated solids flow through the inlet apertures into the space between the conveyor body and the internal side of the drum, following which they are carried axially away by a screw conveyor in a known manner.

The US reference states that it is inconvenient to effect the separation in the space between the conveyor body and the internal side of the drum because the screw conveyor here provokes strong turbulent flows impeding a good separation, whereas separation already at the inlet is preferable because the space in which the separation is effected is free of built-in members, such as blades, guide plates, screw conveyors and similar members that might interfere with the separation. Both decanter cetrifuges represent attempts at solving a problem common to decanter centrifuges of this type, viz. that the feed during acceleration tothe angular velocity of the conveyor body receives twice as much energy as necessary for the liquid to form a liquid layer along the internal side of the inlet. The excess energy settles in the liquid in the centrifuge as undesired turbulent flows extending from the inlet into the space between the conveyor body and the internal side of the drum where the energy is finally converted to heat.

The circumstance that excess energy is supplied to the liquid will be recognized by studying a unit cube of liquid present at the internal liquid surface of the inlet. This cube will have a kinetic energy given by

½ρω²r²,

wherein ω is the angular velocity of the conveyor body, and r is radius to the overflow edge. The angular momentum L of the liquid cube about the axis of rotation is

ρωr².

This angular momentum results from the influence of the inlet which rotates with the angular velocity ω. The energy supplied from the motor propelling the decanter centrifuge is thus

Lω=ρω²r².

It will be seen that this energy is twice as large as the above stated energy that was necessary to keep the liquid cube in the free surface.

In prior art centrifuges the excess energy cannot be deposited in the liquid or dissipated without giving rise to interfering liquid flows in the comparatively thin liquid layer on the internal side of the inlet, thereby decreasing the efficiency of the separation. It is a main object of the invention to provide a decanter centrifuge with an inlet in which said excess energy may be dissipated before the feed flows through the inlet apertures and discharges into the space between the conveyor body and the internal side of the drum where the separation of the solid constituents is effected.

It is a further aim of the invention to demonstrate how the inlet of the decanter centrifuge may be shaped in order to regulate the flow therein to various rates of flow or different types of feed.

The decanter centrifuge according to the invention differs from the prior art in that the mouths of the inlet apertures in the inlet are located on a radius greater than the radius to the outlet weir, that the inlet is axially defined by a rotationally symmetrical first end wall positioned opposite the inlet pipe , and a rotationally symmetrical second end wall located opposite the first end wall and comprising a central projection extending towards the first end wall and having an axial bore for the inlet pipe, and that the mouth of the inlet pipe faces the inlet and is located in a plane perpendicular to the axis of the drum.

This provides for obtaining that the feed flowing through the inlet pipe is led as a jet directly towards the first end wall where it divides and flows towards the radially confining wall of the inlet. As the wall includes no members contributing to rotating the feed, merely a torque is transferred to the feed determined by the friction between the feed and the internal side of the end wall. The angular velocity of the feed in the inlet may therefore be kept substantially lower than the angular velocity of the conveyor body. The free liquid surface in the inlet will therefore be positioned on a considerably smaller radius than the radius to the outlet weir. It is then obtained that the flow in the inlet, when the decanter centrifuge has attained its normal operating condition, mainly passes in the direction from the first end wall and parallel to the free surface in the inlet towards the second end wall and a uniform outflow is concurrently effected through the inlet apertures. When the feed approaches the inlet apertures it has by and large attained the same angular velocity as the conveyor body, but due to the comparatively long path of flow in the thick liquid layer in the inlet, the excess energy has been disspipated in a manner as to prevent the occurrence of turbulent flows which are entrained through the inlet apertures into the space between the conveyor body and the internal side of the drum.

An embodiment of the invention is characterized in that the projection of the second end wall has the shape of a truncated cone whose pointed end faces the first end wall. Possible air occurring in the feed or being entrained by the feed while flowing into the inlet may be passed away along the periphery of the projection of the second end wall, thereby preventing an air cushion from occurring in the inlet which may interfere in the intended flow. With the stated design of the projection any liberated air will flow along the periphery of the projection and leave the inlet through the axial bore in the projection.

In preferred embodiments of the invention the projection of the second end wall may have substantially radial, longitudinal ribs uniformly distributed along the periphery of the projection, or there may be one or more substantially radial ribs following helices along the periphery of the projection. A larger momentum is thus transferred to the liquid in the inlet in case the free liquid surface approaches the periphery of the projection, e.g. because the rate of flow of the feed increases. By altering the shape of the ribs, e.g. from rectilinear ribs to ribs twisting several times round the projection following a helix, the flow may be directed more strongly towards the second end wall, thereby obtaining an improved axial distribution of the feed, and by altering the radial extension of the ribs it is possible to obtain that the free surface of the liquid does not approach such a small radius that the liquid may discharge through the bore of the inlet pipe in the projection.

An alternative preferred embodiment is characterized in that the first end wall centrally includes a baffle knob protruding towards the inlet pipe. This provides for obtaining an improved control of the inflowing feed when it changes from being an axial flow to being a radial flow because such a sudden change in direction is prevented.

In a further embodiment the baffle knob may have radial ribs uniformly distributed along the periphery of the baffle knob. The ribs may extend along straight lines or helical lines. This may be necessary in order to impart a sufficient rotation to the feed in the inlet with the view of obtaining a stable circulation flow in the inlet.

In other embodiments the inlet may be provided in an exchangeable part of the conveyor body and the baffle knob may be exchangeably secured to the first end wall and the projection containing the axial bore of the inlet pipe may be exchangeably secured to the second end wall. It is obtained by these measures that one and the same decanter centrifuge may be used for various types of feed, in that one or more of said components is/are exchanged.

In a preferred embodiment of the decanter centrifuge according to the invention the inlet pipe may be axially displaceable. It is thus obtained that the diameter of the jet at the baffle knob may be altered by displacement of the inlet pipe, thereby making it possible to adapt the flow in the inlet to the type of feed and/or the rate of flow thereof.

The invention will now be explained in detail by some embodiments and with reference to the drawings, in which

Fig. 1 in a very schematical form shows a section of a decanter centrifuge according to the invention,

Fig. 2 shows an embodiment of the inlet of a decanter centrifuge, as illustrated in Fig. 1,

Fig. 3 shows an inlet as in Fig. 2, in which the path of the flow in the feed in the inlet is indicated,

Fig. 4 shows an inlet as in Fig. 3, in which the projection of the second end wall has two ribs following helices along the periphery of the projection,

Fig. 5 shows an inlet as in Fig. 4, in which the first end wall has an annular projection,

Fig. 6 shows an inlet as in Fig. 2, in which the inlet, the baffle knob and the projection of the second end wall are exchangeably mounted,

Fig. 7 is a schematical view of a baffle knob with retilinear ribs, and

Fig. 8 is a schematical view of a baffle knob with helical ribs.

The decanter centrifuge illustrated in Fig. 1 includes a drum 1, rotatably journalled in bearings 22 at each end. A conveyor 2 is rotatably journalled in drum 1 in relation to the drum by means of bearings 23 at each end. Conveyor 2 comprises a conveyor body 3 with an external helical flight 21. The conveyor body 3 includes an inlet 4 axially defined by a first end wall 11 and a second end wall 13. Inlet 4 is radially defined by a wall 5 that is coaxial with the conveyor body 3 and comprises inlet apertures 6 connecting the inlet 4 with the space 7 between the conveyor body 3 and the internal side of drum 1. The decanter centrifuge further inlcudes an inlet pipe 8 having a mouth 16 directed towards inlet 4.

Fig. 2 illustrates inlet 4 with the end wall 11 having centrally a baffle knob 12, in this embodiment shaped as an approximately spherical face smoothly merging into end wall 11 which per se constitutes a smooth transition to the radially confining wall 5. Opposite the baffle knob the second end wall 13 has a projection 14 which includes a bore 15 for inlet pipe 8 and is coaxial with the drum axis. Projection 14 has the shape of a truncated cone whose small end faces the baffle knob. At the large end projection 14 merges smoothly into end wall 13 which per se merges smoothly into wall 5. Six, substantially radial, slightly helical, longitudinal ribs 17 uniformly distributed along the periphery of the projection are positioned on the periphery of projection 14. The mouth of inlet pipe 8 is situated in a plane perpendicular to the drum axis. Inlet pipe 8 is axially displaceable, thereby allowing the distance between mouth 16 and baffle knob 12 to be varied. The adjustment of this distance may according to choice be effected during operation and the variation of the distance may be effected manually or automatically by means of a control mechanism, not shown.

The radial wall 5 is provided with inlet apertures 6 all of which are positioned between the helical flight 21. The apertures are, moreover, provided uniformly across the entire axial extension of wall 5. The liquid may then flow freely from the inlet through the inlet apertures into space 7 without passing members capable of provoking turbulence and vortices. Fig. 3 illustrates the flow paths in the inlet. In dashed lines the upper half of the figure shows various characteristic flow areas through which thefeed flows when passing the inlet.

Arrows in the lower half of the figure shows the direction of the non-tangential velocities of the feed in the inlet.

The path of the feed through the inlet may be described as follows. The feed leaves inlet pipe 8 and continues in a jet towards baffle knob 12 at which it is radially dispersed between the baffle knob and a vortex area 31 located at the free liquid surface. The feed subsequently passes into an agitation zone 30 in which a mixing is effected with liquid from a radially external area 33 of the inlet, thereby increasing the angular velocity of the feed. Said angular velocity is somewhat smaller than the angular velocity in the adjacent zone 33, the socalled dissipation area, and the feed will therefore be forced back towards the liquid surface in the direction towards the radial outer edges of ribs 17. In view of the fact that the ribs rotate with the same speed as the conveyor body, the liquid in this area is imparted an angular acceleration preventing the liquid from penetrating further towards projection 14. The ribs are slightly helical, thereby forcing the liquid towards end wall 13. In the area of acceleration 32 the feed attains the same angular velocity as the ribs whereas the excess energy brought about by this acceleration occurs as a radial velocity carrying the feed into the disspipation area 33 throughout the length of projection 14.

Through a turbulent flow the radial velocity in the dissipation area 33 is converted to a temperature rise in the feed and a mixing takes place so that the high angular velocity in the liquid coming from ribs 17 is converted to an average angular velocity in the liquid moving radially towards area 34 surrounding inlet apertures 6. The three inlet apertures 6 are positioned between the flights so that there are no edges capable of imparting tubulence or retaining threads or similar bigger particles in the feed. The apertures are so large that they do not form any restriction to the flow and as they follow the flights they are axially displaced in relation to each other and cover almost the entire length of the circularly cylindrical wall 5. By the passage of one of the inlet apertures the feed is imparted a small supplementary acceleration, but this influence is only slight because the feed already has obtained approximately the same angular velocity as the conveyor body on said location.

The figure shows that the end walls 11 and 13 merge smoothly into the circularly cylindrical wall 5.

This is not a necessary prerequisite in order that the inlet functions as explained above. If the transition between the end walls and the circularly cylindrical wall were designed as a right-angled corner a stationary flow would just be created in this corner and would not interfere with the above mentioned flows. In such a case it would be possible that a sediment from the feed would precipitate on the actual spot, and this might necessitate a cleaning of the inlet after some time in operation. In order to avoid this, the various faces of the inlet should merge smoothly into each other.

The inlet illustrated in Fig. 4 has ribs 17 that are helically positioned along the circumference of projection 14. Such ribs provoke a stronger flow in the area of acceleration 32 towards end wall 13 than the ribs 17 shown in Fig. 3. Six inlet apertures 6 all of which are positioned between the screw flights 21 are provided in this latter embodiment of the inlet. The inlet illustrated in Fig. 5 has an end wall

11 with an angular projection 20 which on the radially internal and external side of the projection merges smoothly into end wall 11. With such a projection it is possible to obtain a strong control of the flow path in the inlet and by comparison with the upper half of Fig. 3 it is apparent that the projection divides the agitation zone from the dissipation zone, thereby forcing the feed to flow through a longer distance, thereby disspitating its energy prior to approaching the inlet area 34.

Fig. 6 illustrates an inlet substantially designed as the inlet in Fig. 2, but the inlet portion proper is designed as a separate component joined with conveyor body 3 by bolts 25 and flanges on the conveyor body. Baffle knob 12 is also designed as a separate component fixedly bolted on end wall 11 by means of a central bolt 26. Projection 14 is likewise designed as a separate component which through bolts 27 is fixedly bolted on end wall 13.

By the adaptation of a decanter centrifuge according to the invention to a specific form of operation, the described inlet offers great possibilities of varying the size and the shape of the various members concerned with the view of obtaining an optimum yield. The radius of the inlet may be altered only within narrow limits, but it is possible to extend the inlet in the axial direction. In this respect, it must be taken into account that an extension of the inlet generally implies that projection 14 has to be extended too, because it is necessary to control the internal surface of the liquid in the inlet in order to ensure that it does not penetrate so far towards the axis of rotation that the liquid discharges through bore 15 in the projection. If the inlet apertures 6 of a long inlet are uniformly distributed throughout wall 5, there is a risk that part of the feed will only have a short path through the inlet before passing an inlet aperture and penetrating into space 7. In such a case it may be advantageously to make use of an end wall 11 with an annular projection 20 , as illustrated in Fig. 5.

The function of ribs 17 throughout a large span of flow rates is to prevent overflow through bore 5, to impart angular velocity to the feed and to distribute the feed axially throughout the entire inlet, thereby enabling excess energy originating from the acceleration to dissipate throughout the entire dissipation area 33 of the inlet. The axial extension of ribs 17 must therefore be adapted to the axial length of the inlet. The ribs 17 should, however, cover the area at the inlet apertures. Radially the ribs must be positioned on the smallest possible radius, in respect of the diameter of the inlet pipe and also of the bore 15, and the length and also the strength of projection 14.

The individual rib may extend completely axially, at a constant angle in relation to the axis of rotation or at a variable angle in relation to the axis. The angle in relation to the axis caters for the axial distribution of the feed throughout the dissipation area 33 and must be adapted to the rate of flow, the type of feed to be separated and the axial extension of ribs 17 and inlet 4, as mentioned above. The ribs are designed so that hair and threads in the feed do not settle and cling to edges but are thrown off. The purpose of the baffle knob is to alter the direction of the feed so that it is carried into the agitation area 30 with a minimum interference with the free surface of the feed in the inlet and so as to obtain a uniform distribution across the surface of end wall 11 . If ribs 17 on projection 14 do not result in the desired rotation there may, as illustrated in Fig. 6, be provided radial ribs 19 uniformly distributed along the periphery of the baffle knob and following straight lines, as shown in Fig. 7, or helices, as shown in Fig. 8. Said ribs should likewise be shaped so that hair and threads do not settle.

By passing through inlet apertures 6 into space 7, a small acceleration is imparted to the feed, as mentioned above. With the view of reducing this supplementary acceleration, it is advantageous that the thickness of material in the area at the inlet apertures is as small as allowed by the considerations relating to strength and wear.

In respect of the fact that the inlet apertures are located beneath the free surface of the liquid in the inlet, only very small quantities of air may discharge through the inlet. This is the reason why the projection, as mentioned above, is advantageously given the form of a truncated cone, whereby possible air in the inlet may be carried back along the inlet pipe.

In decanter centrifuges having rotating inlet pipes journalled within the conveyor body, means of ensuring that the inlet may be vented through the bearing should be provided. In such a decanter centrifuge it is possible to further improve the separation by establishing partial vacuum in the inlet by exhaustion. Such a partial vacuum reduces the energy to be dissipated, some of the excess energy being in this case used to compensate for the partial pressure.

Claims

P A T E N T C L A I M S

1. A decanter centrifuge comprising a rotatably journalled drum (1) and a conveyor (2) rotatably journalled in the drum with a conveyor body (3) containing an inlet (4) in the form of a cavity for the feed to be separated, said inlet (4) being radially defined by a wall (5) coaxial with the conveyor body and provided with inlet apertures (6) connecting the inlet (4) with the space (7) between the conveyor body (3) and the internal side of the drum (1), a peripheral area of the inlet (4) outwardly defined by the radius to the inlet apertures (6) being free of carriers, inwards extending projections or the like, an inlet pipe (8) for the feed coaxial with the drum, and at one end of the drum an outlet weir (9) for the separated liquid phase, characterized in that the mouths of the inlet apertures (6) in the inlet (4) are located on a radius greater than the radius to the outlet edge (9), that the inlet (4) is axially defined by a rotationally symmetrical first end wall (11) located opposite the inlet pipe (8), and a rotationally symmetrical second end wall (13) located opposite the first end wall (11) and comprising a central projection (14) extending towards the first end wall (11) and having an axial bore (15) for the inlet pipe (8), and that the mouth (16) of the inlet pipe (8) faces the inlet (4) and is located in a plane perpendicular to the axis of the drum.

2. A decanter centrifuge as claimed in claim 1, characterized in that the projection (14) of the second end wall (13) has the shape of a truncated cone whose pointed end faces the first end wall (11).

3. A decanter centrifuge as claimed in claim 1 or 2, characterized in that the projection (14) of the second end wall (13) has a substantially radial rib (17) following a helix along the periphery of the projection.

4. A decanter centrifuge as claimed in claim 1 or 2, characterized in that the projection (14) of the second end wall has several, substantially radial ribs(17) following helices along the periphery of the projection.

5. A decanter centrifuge as claimed in claim 1 or 2, characterized in that the projection (14) of the second end wall (13) is provided with substantially radial, longitudinal ribs ( 17 ) uniformly distributed along the periphery of the projection.

6. A decanter centrifuge as claimed in any of the preceding claims, characterized in that the first end wall (11) centrally is provided with a baffle knob (12) protruding towards the inlet pipe (8).

7. A decanter centrifuge as claimed in any of the preceding claims, characterized in that the baffle knob (12) has substantially radial ribs uniformly distributed along the periphery of the baffle knob.

8. A decanter centrifuge as claimed in claim 7, characterized in that the substantially radial ribs of the baffle knob (12) follow helices along the periphery of the baffle knob.

9. A decanter centrifuge as claimed in any of the preceding claims, characterized in that the first end wall (11) has an annular projection (20) facing the inlet pipe (8).

10. A decanter centrifuge as claimed in any of the preceding claims and in which the conveyor (2) comprises a helical flight (21), characterized in that each inlet aperture (6) is positioned between two adjacent screw flights.

11. A decanter centrifuge as claimed in any of the preceding claims, characterized in that the conveyor body (3) has an exchangeable part (24) accommodating the inlet (4).

12. A decanter centrifuge as claimed in claims 6 to 11, characterized in that the baffle knob (12) is exchangeably secured to the first end wall (11).

13. A decanter centrifuge as claimed in any of the preceding claims, characterized in that the projection (14) containing an axial bore (15) for the inlet pipe (8) is exchangeably secured to the second end wall (13).

14. A decanter centrifuge as claimed in any of the preceding claims, characterized in that the inlet pipe (8) is axially displaceable.