CENTRIFUGAL SEPARATOR

Abstract: The invention is related to a liquid separator having a centrifuge rotor (1) with a set of conical separation discs (21) arranged coaxially in the separation chamber (13). The inlet of the separation chamber is formed as inlet passages (20) which extend radially outwards from a central inlet chamber (16) in the rotor along the end wall of the separation chamber towards which the separation discs turn their apex ends. The inlet passages (20) are formed between said end wall and partition member (18, 19) situated between the rotor end wall and the separation discs (21). The outlet of the separation chamber (13) for separated liquid is formed by a number of channels (22) through said partition member (18,19) and aligned channels through tubular members (23) bridging said inlet passages (20). The channels through the tubular members (23) thus cross the inlet passages (20) and communicate with the channels (24) in the above said rotor end wall, which channels (24) also constitute parts of the outlet from the separation chamber (13) for separated liquid.

Description: This invention relates to a centrifugal separator for separating two components from a liquid mixture. In particular the invention concerns a centrifugal separator having a rotor body forming a central inlet chamber and a separation chamber, the separation chamber having an inlet for the liquid mixture and at least one outlet for a separated liquid component, a set of conical separation discs arranged in the separation chamber coaxially with the rotor body, the base portions of the discs facing towards one end and the apex portions of the discs facing towards the other end of the separation chamber, and a partition member arranged between the separation discs and a part of the rotor body to delimit inlet passages connecting the central inlet chamber with the separation chamber at the said other end of the latter. A centrifugal separation of the foregoing construction is disclosed in Swedish Patent No. 19666 dating from 1904. It is unknown whether this centrifugal separator has ever been made and used. Since the turn of the century it has been the practice for the inlet of the separation chamber in centrifugal separators of this form to be situated at the said one end of the separation chamber, i.e. that towards which the base portions of the separation discs are directed. A conventional centrifugal separator of this kind is shown for instance in US-A-3986663. A principal advantage of a centrifugal separator, in which a mixture is conducted into the separation chamber at the said other end thereof, i.e. that towards which the apex portions of the separation discs are directed is that maximum advantage can be taken of a pre-separation which takes place in the inlet passages before the mixture enters the separation chamber. Thus, a part of a relatively heavy component of the mixture, for instance solids, may be separated when the mixture passes through the inlet passages extending between the central inlet chamber and the inlet of the separation chamber. Relatively heavy component of the supplied mixture, separated in the inlet passages, may slide along the outer walls of the inlet passages directly out into the outermost part of the separation chamber radially outside the separation discs without being disturbed by or disturbing the flow of the rest of the mixture into the separation chamber. In a conventional centrifugal separator, in which the liquid mixture is instead introduced through inlet passages at the one end of the separation chamber, i.e. that towards which the base portions of the separation discs are directed (see for instance US-A-3986663), relatively heavy component of the mixture separated in the inlet passages is forced to cross the flow of the rest of the mixture entering the separation chamber. This is a consequence of the fact that the inlet passages have an inclination relative to the rotor axis just about that of the conical separation discs. Thus, the result of the pre-separation in the inlet passages is spoiled wholly or partly. This undesired effect of the cross flow will become largest when all the mixture is introduced into the separation chamber at the outer edge of the separation disc situated closest to the inlet passages. A possible reason why the design already known in 1904 has not become generally accepted may be the practical difficulties of ensuring the necessary sealing within the centrifuge rotor to separate the crossing flows of liquid mixture on its way into the separation chamber and separated liquid component on its way out of the separation chamber. In the known design the previously mentioned partition member is axially movable relative to a central column, in the rotor body, against which it should seal radially with its inner edge during operation of the rotor. The inner edge of the partition member and, thus, the sealing location are very close to the outlet of the separation chamber for separated liquid component. Since the partition member has to be separated from the column each time the centrifuge rotor is disassembled, e.g. for removal of separated sludge from the separation chamber, difficulties may arise with the sealing between the column and the partition member. A leakage of inflowing mixture into the outflowing separated liquid will, of course, destroy the separation results. The aim of the present invention is to provide a centrifugal separator which embodies the same principle as the separator proposed in the above mentioned patent specification for the introduction of the mixture into the rotor, and which overcomes the sealing problem in a simple and practical manner. In accordance with the present invention there is provided a centrifugal separator for separating two components from a liquid mixture, comprising a rotor body forming a central inlet chamber and a separation chamber having an inlet for the liquid mixture and at least one outlet for a separated liquid component, a set of conical separation discs arranged in the separation chamber coaxially with the rotor body, the base portions of the discs facing towards one end and the apex portions thereof facing towards the other end of the separation chamber, and a partition member arranged between the separation discs and a part of the rotor body to delimit inlet passages connecting the central inlet chamber with the separation chamber at the said other end of the latter, characterised in that the partition member has a number of through holes and said part of the rotor body has corresponding through holes, and that tubular members interconnect the partition member and the rotor body around the through holes whereby enclosed outlet channels leading from the separation chamber are formed and intersect the direction of the inlet passages connecting the inlet chamber to the separation chamber. If a centrifuge rotor designed in this way comprises a central column as previously mentioned and sealing means between this column and the partition member, substantially lower demands may be put on such sealing means than on the corresponding sealing means in the known design of 1904. This is due to the fact that the outlet of the separation chamber for separated liquid component does not have to be situated in the vicinity of the inner edge of the partition member but may be instead be located at a distance therefrom radially as well as axially. Preferably, the partition member has a central sleeve-like part situated radially inside the separation discs and extending axially past several of them, so that said sealing location can be at a large distance from said outlet of the separation chamber. If in such a design of rotor a small leakage of mixture occurs at the sealing location the leaking mixture would have time to be subjected to sufficient centrifuging to be freed from particles suspended therein, before it reaches the outlet of the separation chamber. The invention however, is not restricted to a centrifuge rotor in which the partition member should seal radially against a central column. Since the inlet chamber of the rotor may be situated on one side and the separation chamber on the other side of the partition member, the latter need not have any central opening for admitting throughflow of mixture on its way into the separation chamber. A rotor of this design is suitable if the rotor body comprises two main parts held axially together at the periphery of the rotor body. Regardless of whether two main parts of the rotor body are connected with each other at the periphery or through a central column, the partition member is preferably firmly connected with the above mentioned part of the rotor body by means of the tubular members, so that it can be removed together with one main part of the rotor body when this main part is separated from the other during disassembly of the rotor body, for instance in for cleaning. In a preferred embodiment of the invention the tubular members are formed in one piece with either the partition member or the rotor body. Preferably at least one of the partition member and the rotor body is made of plastic material, so that a tight so-called snap lock connection can easily be established between these rotor parts around each of the tubular members. The present invention makes it possible to produce a small centrifugal separator at a very low price. Some embodiments of the invention will now be described in detail with reference to the accompanying drawings, in which: Fig. 1 shows partly in axial cross-section a preferred centrifugal separator according to the invention; Fig. 2 shows in enlarged plan a part of the centrifugal separator of Fig. 1; Fig. 3 shows in axial section a modified part corresponding to that shown in Figs. 1 and 2; and Fig. 4 shows another modified part of the centrifugal separator in Fig. 1. Fig. 1 shows a centrifugal separator having a rotor 1, a vertical drive shaft 2 supporting the rotor, a driving device 3 in engagement with the drive shaft, a lower housing 4 for the driving device 3 and an upper housing 5 for the rotor. The upper housing 5 includes an inlet tube 6 for a mixture of two liquids having different densities and having particles suspended therein. Further, the housing 5 forms a receiving chamber 7 having an outlet 8 for a separated relatively light liquid and a receiving chamber 9 having an outlet 10 for a separated relatively heavy liquid. The rotor 1 comprises two rotor parts 11 and 12, which are kept axially pressed against each other and which surround a separation chamber 13. The rotor part 11, which forms a bottom in the separation chamber 13 and is connected with the drive shaft 2, has a central column 14 the upper part of which is arresting the rotor part 12 by means of an annular locking member 15. The rotor part 12 forms a substantially cylindrical surrounding wall and a substantially conical upper end wall of the rotor. A narrow end portion of the inlet tube 6 extends axially through the locking member 15 into a central inlet chamber 16 formed in a tubular upper portion of the central column 14. This tubular portion of the column 14 has several openings 17 in its surrounding wall. The locking member 15 forms an upper annular end wall in the inlet chamber 16. Around the central column 14 there is arranged a partition member having a sleeve-like part 18 and a conical part 19. The sleeve part 18 surrounds the column 14 below said openings 17. An annular gasket seals between the sleeve part 18 and the column 14. The conical part 19 abuts against said upper end wall of the rotor. Radial recesses in the conical part 19 form between this part and the rotor end wall several passages 20 which connects the openings 17 with the separation chamber 13. A set of frusto-conical separation discs 21 is arranged between the conical part 19 and the lower rotor part 11 in the separation chamber 13, coaxially with the rotor axis. The outer edges of the separation discs 21 are situated substantially at the same radial level as the outer edge of the conical part 19. The inner edges of the separation discs 21 are situated at some distance radially outside the sleeve part 18, so that a central space is formed in the separation chamber 13 radially inside the separation discs 21. This space is divided into parallel axial channels by radially and axially extending wings supported by the sleeve part 18. The conical part 19 has a number of, e.g. three, axially through channels 22 and supports on its upper side an equal number of tubular members 23, the interiors of which communicate with respective channels 22. The rotor part 12 has an equal number of axial through channels 24 which are situated such that they communicate through the tubular members 23 with the respective channels 22. An annular gasket is arranged to seal between the tubular members 23 and the rotor part 12 around each of the channels communicating defined therethrough. Upon the rotor part 12 there is arranged an annular member 25, which together with the rotor part 12 forms a chamber 26 into which the channels 24 through the rotor part 12 open. The chamber 26 has one or several peripheral outlets 27. In the lower part of the separation chamber 13 there is placed an annular member 28 which seals radially inwards and axially downwards against the rotor part 11 and which extends radially outwards in the separation chamber 13 beyond the separation discs 21. On its underside the annular member 28 has a number of radial grooves which form channels 29 extending between the separation chamber 13 and an equal number of central radial channels 30 in the rotor part 11. The radial channels 30 communicate with a number of axial channels 31 in which axial tubes 32 are inserted. The tubes 32 extend through aligned holes in the separation discs 21, holes in the previously mentioned conical part 19, holes in the rotor part 12 and holes in the annular member 25. Sealing gaskets are arranged around said holes and around the tubes 32, between the rotor part 12 and each of the conical part 19 and the annular member 25. The interiors of the tubes 32, which communicate through the channels 29-31 with the separation chamber 13, open into a radially inwardly open groove 33 in the annular member 25. The upper edge of the groove 33 forms an overflow outlet 34 therefrom. From the radially innermost part of each channel 30 a draining channel 35 extends through the rotor part 11 to the outside of the rotor. A shielding member 36 is connected with the drive shaft 2 and arranged to prevent liquid leaving the rotor through the draining channels 35 from flowing down into the housing 4 of the driving device. The rotor housing 5 has a separate outlet 37 for such liquid. Fig. 2 shows from above the partition member which comprises the conical part 19. Apart from the previously mentioned three tubular members 23, another three tubular members 38 are shown and through the openings of which the tubes 32 (fig. 1) are passed. As seen most evidently from fig. 2 the tubular members 38 are situated at a larger radius than the tubular members 23. Radially and axially extending ridges 39 on the upper side of the conical part 19 define the previously mentioned recesses forming together with the rotor part 12 the passages 20 in fig. 1. Around its periphery the conical part 19 has a number of recesses 40, the function of which will be described later. Corresponding recesses axially aligned with the recesses 40 are present in all of the separating discs 21 in the separation chamber 13. Fig. 3 shows a section through a somewhat modified partition member comprising a conical part 19a, a sleeve-like part 18a and tubular members 23a and 38a. The partition member shown in fig. 3 is intended to be made entirely of plastic and, as can be seen, the tubular members 23a and 38a have been formed in a way to enable a firm connection with the rotor part 12. Sleeve-like extensions 41 and 42 having small external annular end flanges 43 and 44, respectively, are dimensioned and are resilient so that they will engage with a snap fit when inserted into the holes in the rotor part 12 intended therefor. Fig. 4 shows the upper part of a rotor according to fig. 1 comprising a partition member according to fig. 3. The tubular members 23a and 38a are inserted into through channels in the rotor part 12a. The walls of these channels have annular grooves for taking up the annular end flanges 43 and 44 (fig. 3). The partition member thus is connected with the rotor part 12a by means of a so-called snap-lock connection. A further so called snap-lock connection is present between the rotor part 12a and the annular member 25a. The latter has an internal annular flange 45 engaging into an external groove in the rotor part 12a. Instead of a fixed end wall the annular member 25a has a removable and, thus, exchangeable annular end wall 46, the inner edge of which forms an overflow outlet corresponding to the overflow outlet 34 in fig. 1. Also the end wall 46 is secured to the annular member 25a by means of a so-called snap-lock connection. The centrifugal separation in fig. 1 is intended to operate in the following manner after the rotor 1 has been put in rotation by means of a driving device 3. Through the pipe 6 a mixture of two liquids with different densities and solid particles suspended therein is supplied into the central inlet chamber 16. The mixture flows through the openings 17 and the passages 20 to the separation chamber 13. Mainly through the recesses 40 in the conical part 19 and the corresponding recesses in the separation discs 21 the mixture is distributed between the separation discs. In the passages 20 a pre-separation of the three components of the supplied mixture takes place. A large part of the suspended solids and part of the heavier one of the liquids move along the rotor part 12 out to the surrounding wall of the separation chamber 13 without disturbing the further flow of the liquid mixture into the separation chamber. The liquid mixture with possibly remaining solids is then distributed between the separation discs 21. Between the separation discs the two liquids of different densities are separated, the lighter liquid flowing radially inwards and being conducted through the channels 22 and 24 to the chamber 26, whereas the heavier liquid flows radially outwards. Outside the separation discs 21 the latter liquid flows axially downwards in the separation chamber and out thereof through the channels 29. It is conducted further through the channels 30 and 31 and by the tube 32 to the annular groove 33. While the separated heavy liquid is discharged over the overflow outlet 34, the separated light liquid leaves through the outlet 27 of the chamber 26. The outlet 27 is so large that the chamber 26 during normal operation is only partly filled. This means that the tubular members 23 and the radially outer walls of the channels 22 and 24 form overflow outlets from the separation chamber 13 for the separated light liquid. The position of the interface layer formed in the separation chamber during operation between the the two separated liquids is determined by the positions of the two said overflow outlets from the separation chamber. The position of the interface layer may be changed by exchange of the annular member 25 for another one, the overflow outlet 34 of which is situated at a different radial level. Of course, alternatively, an exchangeable so called gravity disc may be arranged in either of the chamber 26 and the groove 33. If desired, conventional distribution channels extending axially through the separation discs 21 and the conical part 19 may be located at any desired distance from the rotor axis. If and when required the annular member 28 at the bottom of the separation chamber may be exchanged for another one having a larger or smaller radial extension. For the removal of separated solids from the separation chamber the locking member 15 has to be removed and the rotor parts 11 and 12 have to be separated. Since the channels 22 and 24 during operation will serve as overflow outlets from the separation chamber 13, a free liquid surface will be formed in the separation chamber radially outside the sleeve part 18 around the central column 14. Any leakage past the gasket between the column 14 and the sleeve part 18 will therefore be directed from the inlet chamber 16 to the separation chamber 13. Since the lower portion of the sleeve part 18 is situated at a substantial axial distance from the overflow outlet 24 for separated light liquid, any such leakage of small magnitude will not influence the separation in the rotor. In a preferred embodiment of the invention the components 11, 12 and 32 are made of metal, whereas the component parts 18, 19, 25 and 28 are made of plastic. Thereby, instead of separate sealing members, such as gaskets, placed between the tubular members 23, 38 and the rotor part 12, the tubular members 23 and 38 by being made of plastic may themselves accomplish the sealing. Preferably this is achieved by forming the members in question such that a firm connection, e.g. a so-called snap-lock connection, is obtained between these and the rotor part 12 (fig. 4). This avoids the important seal between the tubular members 23, 38 and the rotor part 12 having to be broken every time the rotor is disassembled; in other words the sealing function will be more reliable and will not be jeopardised by wear or damage. Furthermore, dismantling and reassembly of the rotor are simplified by the fact that the rotor will consist of a smaller number of parts. Even the uppermost annular member 25 may be formed such that a firm connection may be obtained between this part and the rotor part 12 (fig. 4). The tubes 32 preferably are fixed in the rotor part 11, so that they can maintain the separation discs 21 in fixed positions when the rotor part 12 is removed. The tubes 32 thus serve as guiding means for separation discs 21 and prevent these from being turned relative to each other during rotation of the rotor.

Claims: 1. A centrifugal separator for separating two components from a liquid mixture, comprising a rotor body forming a central inlet chamber (16) and a separation chamber (13) having an inlet for the liquid mixture and at least one outlet for a separated liquid component, a set of conical separation discs (21) arranged in the separation chamber (13) coaxially with the rotor body, the base portions of the discs facing towards one end and the apex portions thereof facing towards the other end of the separation chamber, and a partition member (18, 19) arranged between the separation discs (21) and a part of the rotor body to delimit inlet passages (20) connecting the central inlet chamber (16) with the separation chamber at the said other end of the latter, characterised in that the partition member (18, 19) has a number of through holes (22) and said part of the rotor body has corresponding through holes (24), and that tubular members (23) interconnect the partition member (18, 19) and the rotor body around the through holes (22, 24), whereby enclosed outlet channels leading from the separation chamber (13) are formed and intersect the direction of the inlet passages (20) connecting the inlet chamber (16) to the separation chamber (13). 2. A centrifugal separator according to claim 1, wherein the tubular members (23) are formed in one piece with either the rotor body or the partition member (18, 19). 3. A centrifugal separator according to claim 1 or 2, wherein the tubular members (23) are firmly connected with both the partition member (18, 19) and said part of the rotor body for maintaining them together upon disassembly of the rotor body. 4. A centrifugal separator according to any of the preceding claims, wherein the rotor body comprises a first rotor part (11) having a central column (14) and a second rotor part (12) removably connected with the column and connected with said partition member (18, 19) by means of the tubular members (23), and the partition member (18, 19) comprises a central sleeve (18) which sealingly surrounds the central column (14) and is axially movable relative thereto. 5. A centrifugal separator according to claim 4, wherein the separation discs (21) have a frustoconical form and that the central sleeve (18) extends axially past several separation discs (21). 6. A centrifugal separator according to any of the preceding claims, wherein the partition member comprises a conical part (19) the cone angle of which substantially corresponds to that of the separation discs (21). 7. A centrifugal separator according to claim 6, wherein the conical part (19) of the partition member has substantially the same radial extension as the separation discs (21). 8. A centrifugal separator according to any of the preceding claims, wherein separate guiding members (32) are provided for the separation discs (21), the guiding members having their ends connected to the rotor body, and the mid portions of the guiding members extending through axially aligned recesses in the separation discs. 9. A centrifugal separator according to claim 8, wherein said guiding members (32) form channels communicating at the said one end of the separation chamber (13) with an outlet (29) from the separation chamber for a separated relatively heavy liquid component, and communicating at the other end of the separation chamber with an outlet (33, 34) from the rotor for the heavy liquid component. 10. A centrifugal separator according to claim 9, wherein the channels extend through some of said through holes (22, 24) in the partition member and said part of the rotor body, the remaining through holes forming outlets for a separated relatively light liquid component of the liquid mixture.

Inventors: STROUCKEN, KLAUS
Applicants: ALFA-LAVAL SEPARATION AB
Application year: 1988
Main classification: B04B11
IPC codes: B04B11, B04B1