WO1998045044A1 - Separateur centrifuge dote de disques de separation et d'un moyen de transport des boues - Google Patents

Separateur centrifuge dote de disques de separation et d'un moyen de transport des boues Download PDF

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Publication number
WO1998045044A1
WO1998045044A1 PCT/SE1998/000552 SE9800552W WO9845044A1 WO 1998045044 A1 WO1998045044 A1 WO 1998045044A1 SE 9800552 W SE9800552 W SE 9800552W WO 9845044 A1 WO9845044 A1 WO 9845044A1
Authority
WO
WIPO (PCT)
Prior art keywords
rotor
sludge
separation
centrifugal separator
conveyor screws
Prior art date
Application number
PCT/SE1998/000552
Other languages
English (en)
Swedish (sv)
Inventor
Ingvar HÄLLGREN
Hans Martin
Berndt NYSTRÖM
Original Assignee
Alfa Laval Ab
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Alfa Laval Ab filed Critical Alfa Laval Ab
Priority to AU67548/98A priority Critical patent/AU6754898A/en
Publication of WO1998045044A1 publication Critical patent/WO1998045044A1/fr

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B11/00—Feeding, charging, or discharging bowls
    • B04B11/04—Periodical feeding or discharging; Control arrangements therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/04—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls
    • B04B1/08—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls of conical shape

Definitions

  • a centrifugal separator having separation discs and sludge transporting means
  • the present invention relates to a centrifugal separator for freeing a liquid from solid particles suspended therein and having a density larger than that of the liquid.
  • centrifugal separators for this purpose are known, being arranged during operation to discharge continuously or intermittently sludge, which contains separated solid particles. Each one of the various types is intended for treatment of liquid containing particles in a certain amount and/or of a certain kind.
  • An ordinary decanter centrifuge has a normally elongated rotor, in the separation chamber of which only one single conveyor screw is arranged to rotate around the same rotational axis as the rotor but with a different speed than that.
  • Separated particles in this way may be transported by the conveyor screw axially within the rotor up to normally constantly open so-called sludge outlets.
  • a decanter centrifuge of this kind is shown for instance in
  • a decanter centrifuge of a somewhat different kind is shown in US-A-3,685,721.
  • This decanter centrifuge has several conveyor screws arranged in the centrifuge rotor separation chamber evenly distributed around the rotational axis of the centrifugal rotor. Each of the conveyor screws is arranged to transport separated particles to and out through a sludge outlet at one end of the separation chamber.
  • a centrifugal separator reminding of an ordinary decanter centrifuge, i.e. having only one conveyor screw, but having an intermittently openable so called sludge outlet, is shown in US-A-4,508,530.
  • this centrifugal separator which is intended for freeing a liquid from both solid particles heavier than the liquid and from liquid drops dispersed/emulgated in the liquid and being lighter than the carrying liquid, there is used for the separation also a set of conical separation discs which are arranged in the separation chamber radially inside the conveyor screw.
  • a decanter centrifuge as a rule has a large rotor volume and, thereby, a relatively large capacity, i.e. a large flow of a liquid containing a large amount of solid particles can be treated.
  • the elongated rotor is normally journalled at both its ends and is adapted to rotate about a horizontal rotational axis. This means that a decanter centrifuge requires a relatively large floor area for its rotor, its driving means and its gear box, the last mentioned being needed for operation of the sludge transportation device within the rotor.
  • Decanter centrifuges having centrifugal rotors rotatable around vertical axes are also known, however, for instance through US-A-2, 862,658. The rotor of such a decanter centrifuge is journalled either at its lower end or at its upper end.
  • Centrifugal separators of the kinds described so far are, as mentioned before, intended above all for treatment of large flows of liquid containing relatively large amounts of particles. For this purpose they have been given a construction which does not make large rotational speeds of the centrifugal rotor possible and which, therefore, are not suitable when there are requirements of substantial cleanliness of the separated liquid. For such requirements of substantial cleanliness of the separated liquid there are other types of centrifugal separators. These are so formed, however, that they are not suitable for treating large flows of liquid having a large content of solid particles. Thus, there are so called nozzle separators of a kind shown for instance in US-A-2,321 ,918.
  • the rotor of a centrifugal separator of this type normally has a set of conical separation discs in its separation chamber and a rotor body the radial extension of which is in the same order as its axial extension.
  • the reason for this form of the rotor body is that particles being separated from a liquid in the separation chamber should be able to move by themselves, i.e. slide on the surrounding wall of the separation chamber, without assistance from separate sludge transportation means, to sludge outlet nozzles situated at the surrounding wall of the rotor and being open or intermittently openable.
  • the surrounding wall of the separation chamber in this case is constituted mainly by two conical rotor end walls, which are united with each other along their surrounding edges.
  • a rotor having a design like this is expensive to produce and gets by necessity a rather large diameter without for this reason being usable for treatment of large amounts of sludge.
  • centrifugal separators the centrifugal rotors of which in addition to conical separation discs in the separation chamber have equipment for intermittent discharge of particles from the separation chamber through separate openings or a slot extending all around the rotational axis of the rotor.
  • the rotors for centrifugal separators of this kind are even more expensive to produce than rotors for nozzle separators and are even less suitable for freeing of liquids from large amounts of particles suspended therein.
  • a centrifugal separator of the last mentioned type is shown in US-A-4,698,053. Centrifugal separators of the last mentioned types, i.e.
  • centrifugal separators fulfilling requirements of very good cleanliness of the separated liquid, normally have their rotors arranged with a vertical rotational axis. Hereby, they need a relatively small floor space for their installation. However, as mentioned above, they have in comparison with decanter centrifuges a relatively small capacity as to treatment of liquids containing large amounts of solid particles.
  • the object of the present invention is to provide a centrifugal separator, which may be used for treatment of liquids having a small as well as a large content of particles and which may fulfil requirements of very good cleanliness of the separated liquid.
  • centrifugal separator which, like the centrifugal separator according to US-A-3,685,721 , comprises
  • a rotor which has a centre axis and comprises two axially spaced end walls and a surrounding wall that is arranged axially between the end walls and together therewith surrounds a separation chamber, the axial extension of which is substantially larger than the radial extension of it, the rotor further having at least one inlet for introduction of said liquid into the separation chamber, at least one liquid outlet for discharge of liquid having been freed from particles and at least one sludge outlet for discharge of particles having been sepa- rated from the liquid,
  • a driving means for rotation of the rotor around the centre axis at least two sludge conveyor screws arranged in the separation chamber in the vicinity of the surrounding wall of the rotor, which sludge conveyor screws are separated from each other in the circumferential direction of the rotor and rotatable relative to the surrounding wall of the rotor during rotor rotation for substantially axial transportation of separated particles along the surrounding wall to said sludge outlet, and
  • centrifugal separator which centrifugal separator is characterized in that several separation discs are arranged in the separation chamber at small distances from each other for accomplishing small separation distances for the particles to be separated from the liquid.
  • centrifugal separator which has a large separation efficiency and, simultaneously, a large flow capacity independent of whether the suspension to be treated contains a large or a small amount of suspended particles.
  • centrifugal separator for taking up forces in its circumferential direction, caused by rotor rotation, has a circular- cylindrical portion which surrounds the separation chamber and the sludge conveyor screws. Since the sludge conveyor screws, thus, do not extend as in the known centrifugal separator according to US-A-3,685,721 in and along axial grooves formed in the surrounding wall of the rotor, this may be given a substantial strength in the circumferential direction of the rotor, so that the rotor can be subjected to very high rotational speeds.
  • the centrifugal separator according to the invention may have separation discs of any suitable kind.
  • a small or large number of discs may extend axially as well as helically from an area close to the rotational axis of the rotor towards the surrounding wall of the rotor, the discs between themselves forming separate, substantially axial through-flow channels for the treated liquid.
  • the separation discs may be conical and stacked upon each other coaxially with the rotor. Different types of separation discs are shown for instance in DE 48 615.
  • the separation discs extend radially out into the spaces formed between said sludge conveyor screws, seen in the circumferential direction of the rotor. If the separation discs are conical, this means that the separation discs have axially aligned holes or recesses, which form axial channels through the stack of separation discs close to the surrounding wall of the rotor, the sludge conveyor screws extending through respective axial channels.
  • those parts of the separation chamber which are situated between the sludge conveyor screws, seen in the circumferential direction of the rotor may be used for effective separation.
  • the separation discs extend so far out into the spaces between the sludge conveyor screws that they can obtain support from the surrounding wall of the rotor during operation of the rotor.
  • the separation discs may be made from a relatively light material, such as plastic, which makes possible a form of the rotor such that it can be rotated at a very high speed.
  • each filler piece may be arranged in the spaces between the sludge screws.
  • Each filler piece is preferably tapering in the direction towards the centre axis of the rotor.
  • the separation discs form at least parts of these filler pieces.
  • each of the separation discs may be formed with a central, relatively thin part, which forms a wall between two separation spaces, formed between adjacent separation discs, and several relatively thick portions, which constitute parts of said filler pieces between the sludge conveyor screws.
  • the conical separation discs extending up to and being supported radially by the ridges.
  • Figure 1 shows in a longitudinal section a centrifugal separator according to a preferred embodiment of the invention.
  • Figure 2 shows a section along the line ll-ll in figure 1.
  • Figure 3 shows an enlarged part of figure 1.
  • Figure 4 shows a cross-section through the centrifugal rotor shown in figure 1 , taken between two adjacent separation discs.
  • Figure 5 shows a separation disc of the kind shown in figure 4.
  • Figure 6 shows a cross-section, similar to that in figure 4, of a somewhat modified embodiment of the invention.
  • Figure 7 shows a cross-section, similar to that in figure 4, of a further modified embodiment of the invention.
  • Figure 8 shows a separation disc of the kind included in the modified embodiment of the invention according to figure 7.
  • Figure 9 shows in a longitudinal section part of a centrifugal separator having separation discs of the kind shown in the figures 7 and 8.
  • FIG. 1 shows a centrifugal separator for freeing a liquid from solid particles suspended therein and having a density larger than that of the liquid.
  • the centrifugal separator comprises a frame 1 , a rotor 2 that is rotatably supported by and within the frame 1 and a motor 3 that is also supported by the frame but on its outside and that is adapted for rotation of the rotor 2 about a vertical rotational axis 4 coinciding with the centre axis of the rotor.
  • the motor 3 supports on its drive shaft a belt pulley 5 and the rotor supports at its lower part a belt pulley 6.
  • a drive belt 7 surrounds both the belt pulleys 5 and 6.
  • the motor 3 supports on its drive shaft a further belt pulley 8, which together with an annular transmission member 9 arranged coaxially with the rotor 2 and rotatable relative thereto is surrounded by a further drive belt 10.
  • the rotor 2 which is rotatably suspended in the frame by means of a lower bearing 11 and an upper bearing 12, comprises a lower end wall 13 and an upper end wall 14.
  • the lower end wall 13 is formed in one piece with a shaft 15 that extends all the way from the area of the lower bearing 11 past the lower end wall 13 up to the upper end wall 14 and through a central opening therein.
  • a locking member 16 the upper end wall 14 is fixed relative to the shaft 15 at least in a way such that it cannot move in a direction away from the lower end wall 13.
  • the end wall 14 is also fixed relative to the shaft 15 in its circumferential direction.
  • the rotor further comprises a circular-cylindrical surrounding wall 17, which extends axially between the end walls 13 and 14, coaxially surrounding the shaft 15 spaced therefrom.
  • the surrounding wall 17 shall not transfer any substantial axial force and, therefore, is not firmly connected with the end walls 13 and 14. Instead, the surrounding wall 17 abuts at its ends through annular gaskets 18 and 19 radially against the respective end walls 13 and 14.
  • the surrounding wall 17 is formed such that it can take up very large forces in its circumferential direction and, therefore, is reinforced by carbon or glass fibres extending substantially in said circumferential direction.
  • the end walls 13, 14 and the surrounding wall 17 surrounds a separation chamber 20 within the rotor.
  • the separation chamber 20 surrounds the shaft 15 and has an axial extension substantially larger than its radial extension.
  • Within the separation chamber 20 coaxially with the rotor a stack of frusto- conical separation discs 21 is arranged between the end walls 13, 14. By means of spacing members the separation discs are maintained at some axial distance from each other.
  • the upper end wall 14 on its outside is connected with an inlet member 22 forming a central, vertical inlet channel 23.
  • This inlet channel 23 communicates at its upper end with an inlet 24 for liquid to be treated within the rotor, and it branches off at its lower end in several branch channels 25.
  • the branch channels 25 which are formed partly in the inlet member 22 and partly in the upper end wall 14 open into the upper part of the separation chamber 20 radially about half-way between the central rotor shaft 15 and the surrounding wall 17.
  • the lower end wall 13 has a number of branch channels 26 intended for liquid having been treated in the rotor.
  • the branch channels 26 start from the lower part of the separation chamber 20 and extend to a common outlet channel 27 which in its turn extends further centrally in the rotor shaft 15 to and out through the lower end thereof.
  • the rotor For solid particles having been separated from said liquid in the separation chamber 20 the rotor has several outlet channels 28 extending from the uppermost part of the separation chamber axially through the upper end wall 14 at the radially outermost portion thereof.
  • the rotor For transportation of particles separated in the separation chamber 20 to the outlet channels 28 the rotor comprises a conveyor screw device including several conveyor screws 29. These extend axially through the separation chamber 20 close to the surrounding wall 17 and are evenly distributed around the rotor shaft 15.
  • Each conveyor screw 29 is journalled at its ends in the respective end walls 13, 14 and is rotatable around its centre axis relative to the rotor walls during the rotation of the rotor around its rotational axis 4.
  • the rotor shaft 15 supports immediately below the lower end wall 13 the above said annular member 9.
  • This member 9 surrounds the rotor shaft 15 and is adapted by means of the motor 3 through the driving belt 10 to be rotated around the rotational axis 4 of the rotor at a speed different than that of the rotor.
  • the annular member 9 has on its outside axially above the driving belt 10 a gear ring 30 engaging several bearing members 31 evenly distributed around the rotor shaft 15.
  • Each bearing member 31 is connected with a conveyor screw 29 and forms part of a slide bearing through which the conveyor screw 29 is journalled in the lower end wall 13.
  • the bearing member 31 and its co-operation with the gear ring 30, the end wall 13 and the conveyor screw 29 is described more in detail below with reference to figure 3.
  • each conveyor screw 29 is journalled in the upper end wall 14 by means of a pin 32.
  • a space or a pocket 33 which extends radially outwardly from said end portion of the conveyor screw to a level radially outside the inside of the surrounding wall 17.
  • Figure 2 shows a section through the upper end wall 14, taken along the line ll-ll in figure 1.
  • the rotor For closing and intermittent uncovering of the outlet channels 28 the rotor is provided with an axially movable slide 34.
  • springs 35 arranged between the inlet member 22 and the slide 34 the slide 34 is kept pressed against the outside of the upper end wall 14, axial protuberances of the slide 34 abutting sealingly against the end wall around the openings of the respective outlet channels 28.
  • a so called opening chamber 36 which via channels through the inlet member 22 and the rotor shaft 15 communicates with the interior of a narrow tube 37 extending axially upwardly through and out of the inlet member 22 to an upper pressure source of air (not shown).
  • an upper pressure source of air not shown.
  • Figure 3 shows in an enlarged scale part of figure 1. It can thus be seen from figure 3 that the bearing member 31 is supported by a transmission shaft in the form of a short tap 38 extending within a bore 39 in the end wall 13 and connected with the conveyor screw 29.
  • the bearing member 31 with its tap 38 as well as the conveyor screw 29 may be made of plastic.
  • a sealing device 40 is arranged in the bore 39 and is adapted to seal between the tap 38 and the end wall 13.
  • the bearing member 31 has a tubular surrounding part 41 , which on its outside is provided with cogs 42 and on its inside has a slide bearing surface 43.
  • the cogs 42 engage the gear ring 30 of the annular member 9, and the slide bearing surface 43 co-operates with a corresponding slide bearing surface 44 formed on an annular protuberance 45 on the outside of the end wall 13.
  • the protuberance 45 which may have a surface layer of a ceramic material provided with said slide bearing surface 44 surrounds the opening of the bore 39 in the end wall 13, and the two co-operating slide bearing surfaces 43, 44 thus have a substantially larger circum- ference than the bore 39.
  • annular further wall 46 On the outside of the rotor end wall 13 there is mounted an annular further wall 46. This confines between itself and the outside of the end wall 13 an annular transmission chamber 47, which is closed radially outwardly but open radially inwardly towards the rotor shaft 15.
  • the chamber 47 during operation of the rotor may be filled with liquid, e.g. water, trough a supply pipe 48 and is intended always to be filled during operation of the rotor.
  • a radially inner edge 49 of the further wall 46 may serve as an overflow outlet for liquid being supplied to the chamber 47.
  • FIG 3 a substantial part of the bearing member 31 will be present during operation of the rotor in liquid present in the chamber 47.
  • This liquid has two purposes; firstly, it shall operate as a lubricator between the slide bearing surfaces 43 and 44, when the con- veyor screw 29 rotates relative to the rotor, and secondly it shall create an hydraulic force acting on the bearing member 31 in a direction towards the rotational axis 4 of the rotor.
  • the hydraulic force counteracts the centrifugal force to which the bearing member is subjected during its rotation around the rotational axis 4 of the rotor and, thereby, acts unloading on the slide bearing formed by the bearing member 31 and the protuberance 45 on the rotor end wall 13.
  • Figure 4 shows a cross section through the rotor 2 in figure 1. The section is taken between two adjacent conical separation discs 21.
  • Figure 5 shows a single separation disc 21 of the kind also shown in figure 4.
  • the centre shaft 15 of the rotor has axial grooves 50 forming axial flow paths radially inside the separation discs 21 for liquid which has been freed from solid particles in the separation chamber 20.
  • the separation discs 21 are supported radially in all directions by the shaft 15.
  • Figure 4 also shows that the separation discs 21 are provided with several conventional spacing members 51 which are evenly distributed around the shaft 15 and keeps the separation discs at a desired distance from each other.
  • the separation discs 21 have several through-holes 52, each being placed between two adjacent spacing members 51 , the holes being axially aligned with corresponding holes in the other separation discs 21.
  • the holes 52 form axial so called distribution channels 53 (fig 1 ) through the stack of separation discs axially aligned with the openings of the previously mentioned branch channels 25 in the upper rotor end wall 14.
  • a filler piece 54 extends inside the surrounding wall 17 around the stack of separation discs 21 and the conveyor screws 29.
  • This filler piece has recesses for the conveyor screws 29 and extends in the areas between the conveyor screws radially inwardly forming axially extending ridges which have contact with the separation discs 21.
  • the separation discs which are relatively thin and may be made of plastic receive during operation of the rotor, therefore, radial support from the said ridges of the filler piece 54. Between the conveyor screws the filler piece is so formed that solid particles which during operation of the rotor are separated from the liquid and move radially outwardly between the separation discs will slide on the hills 55 of said ridges in a direction towards the conveyor screws and in between their threads.
  • FIG. 5 shows that each separation disc has both recesses 56 for the conveyor screws 29 and recesses 57 for the filler piece 54.
  • the filler piece 54 may be formed in one piece, suitably from plastic or some other relatively light material. Alternatively, it may be composed of several annular elements having the cross-sectional form shown by the filler piece 54 in figure 4, or from several straight axially extending elements, which are evenly distributed around the rotational axis of the rotor. For covering of the interspaces which may remain between annular or straight elements of this kind a lining 58 of plastic or other material, as shown in figure 6, may be arranged on the inside of the filler piece 54.
  • a further alternative for the forming of the filler piece 54 is that the conical separation discs are formed so that they form together said filler piece. This alternative is illustrated in the figures 7-9.
  • a separation disc 21 in this case has an entirely circular circumference and extends into contact with the surrounding wall 17 of the rotor around the whole of its circumference.
  • the separation disc has through-holes 59 intended for the conveyor screws 29.
  • the separation disc in figure 8 has spacing members 51 formed on its underside.
  • these spacing members 51 are formed in one piece with the separation disc 21 , this has a certain thickness in the areas of the spacing members 51 and a smaller thickness in the areas 60 situated between the spacing members 51. In the areas 60 there is thus created, when two separation discs abut against each other in a stack, a space in which liquid may flow between the separation discs.
  • the filler piece 54 is that this is created around the whole of the rotor radially inside the circular-cylindrical surrounding wall 17, which is formed to take up large forces in the circum- ferential direction of the rotor. It is thus important that the surrounding wall of the rotor has a circular-cylindrical strong portion that surrounds the separation chamber 20 and the sludge conveyor screws 29.
  • centrifugal separator described above with reference to the figures 1-9 operates briefly in the following manner.
  • a suspension of liquid and particles dispersed therein and having a density larger than that of the liquid is supplied through the inlet 24.
  • the suspension is conducted through the channels 23 and 25 to the distribution channels 53 in the stack of separation discs 21. From respective holes 52 in the separation discs 21 the suspension flows out into the spaces between the separation discs 21 and is conducted between adjacent spacing members 51 to the axial channels 50 at the rotor shaft 15 (see fig 4).
  • each conveyor screw 29 extends through a short cylindrical bore which opens into a pocket 33 (see figures 1 and 2).
  • the sludge formed in the separation chamber 20 is thus transported through these bores and out into the pockets 33. From here the sludge is discharged intermittently through the outlet channels 28 in that these are uncovered by means of the slide 34 at desired time intervals.
  • the slide can be actuated by supply of pressurised air to the opening chamber 36.
  • sludge is supplied through said bore to a pocket 33, displaced liquid is conducted away from the pocket 33 to the separation chamber 20 in the part of the bore that is situated closest to the centre axis 4 of the rotor, where a narrow slot is formed between the threads of the conveyor screw 29 and the wall of the bore.
  • the liquid having been freed from particles is conducted out of the rotor below the lower end wall 13 through the channels 26 and 27.
  • the slide 34 alternatively may be adapted automatically to uncover the outlet channels 28, when a predetermined resistance against turning of the conveyor screws 29 is obtained, indicating that a certain amount of sludge has been collected in the separation chamber.
  • the inlet for suspension is arranged at one end and the outlet for liquid at the opposite end of the separation chamber 20, and the outlet for sludge is arranged at the inlet end of the separation chamber, good prerequisites are obtained for liquid leaving the separation chamber to be substantially free from particles.
  • the conical separation discs are arranged in a way such that they face with their apex ends upwardly. If desired, they may instead be arranged with their apex ends facing downwardly towards the outlet for cleaned liquid. Then, the end walls 13 and 14 are suitably formed in a corresponding way, the lower end wall 13 then forming an upwardly open funnel which with its apex portion forms the central outlet for cleaned liquid. If the lower end wall 13 is formed in this way a complete emptying of the separation chamber 20 is facilitated after a finished separating operation.

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  • Centrifugal Separators (AREA)

Abstract

L'invention concerne un séparateur centrifuge permettant de libérer un liquide de particules en suspension dont la densité est supérieure à celle du liquide. Ce séparateur a un rotor (2) qui entoure une chambre de séparation (20) dont la longueur axiale est sensiblement supérieure à la longueur radiale. Le rotor (2) possède, dans sa chambre de séparation (20), au moins deux vis sans fin (29), destinées au transport axial des particules solides séparées, et des disques de séparation (21) permettant de créer de petites distances de séparation pour les particules.
PCT/SE1998/000552 1997-04-04 1998-03-26 Separateur centrifuge dote de disques de separation et d'un moyen de transport des boues WO1998045044A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU67548/98A AU6754898A (en) 1997-04-04 1998-03-26 A centrifugal separator having separation discs and sludge transporting means

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE9701227A SE9701227D0 (sv) 1997-04-04 1997-04-04 Centrifugalseparator med separeringsskivor och slamtransportorgan
SE9701227-2 1997-04-04

Publications (1)

Publication Number Publication Date
WO1998045044A1 true WO1998045044A1 (fr) 1998-10-15

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Application Number Title Priority Date Filing Date
PCT/SE1998/000552 WO1998045044A1 (fr) 1997-04-04 1998-03-26 Separateur centrifuge dote de disques de separation et d'un moyen de transport des boues

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AU (1) AU6754898A (fr)
SE (1) SE9701227D0 (fr)
WO (1) WO1998045044A1 (fr)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2862658A (en) * 1952-05-28 1958-12-02 Separator Ab Method and apparatus for centrifugal separation of a mixture of solids and two liquids
US3685721A (en) * 1970-06-22 1972-08-22 Mashiro Kohama Centrifugal separation apparatus for sewage
US4698053A (en) * 1985-07-05 1987-10-06 Alfa-Laval Separation Ab Centrifugal separator

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2862658A (en) * 1952-05-28 1958-12-02 Separator Ab Method and apparatus for centrifugal separation of a mixture of solids and two liquids
US3685721A (en) * 1970-06-22 1972-08-22 Mashiro Kohama Centrifugal separation apparatus for sewage
US4698053A (en) * 1985-07-05 1987-10-06 Alfa-Laval Separation Ab Centrifugal separator

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Publication number Publication date
SE9701227D0 (sv) 1997-04-04
AU6754898A (en) 1998-10-30

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