A METHOD IN PRIMARILY SO-CALLED ROTATING FILTERS, AND A FILTER

Abstract: A method for application in conjunction primarily with so-called rotating filters of the kind which include a substantially cylindrical filter tube (1) which is provided with a permeable wall and which is sealingly journalled at preferably two axially spaced locations, preferably at the ends of the tube, and which is arranged for rotation about its longitudinal axis in a filter jacket (2), wherewith material to be filtered, the so-called feed, is supplied to a space or chamber (11) located between the filter jacket and the filter tube, and the filtered substance, the filtrate, being tapped-off from the interior of the filter tube. The method is particularly characterized by sealing and journalling the filter tube (1) in a manner adapted to substantial changes in temperature in the filter tube and that facilities are provided for sterilizing the filter. When applicable, the bearings and seals can be sterilized and lubricated and cooled by means of sterilizing media, and, when applicable, the filter tube (1) is caused to rotate at relatively high speeds. The invention also relates to a device for carrying out the method.

Description: A method in primarily so-called rotating filters, and a filter. The present invention relates to a method in primarily so- called rotating filters of the kind which include a sub¬ stantially cylindrical filter 2 which has a permeable tube wall and which is journalled sealingly at preferably two axially spaced locations, preferably at the ends of the tube, for rotation about its longitudinal axis in a filter jacket, in which method material to be filtered, the feed, is fed to a space between the filter jacket and the filter tube, and in which the filtered material, hereinafter called the filtrate, can be removed from the interior of the filter tube. The invention also relates primarily to a so-called rotating filter for carrying out the method. Methods and filters of essentially the aforementioned kind are known to the art. The prior art techniques, however, are encumbered with such drawbacks as high costs, relatively limited capacities with regard, e.g., to the dry solids con¬ tents that can be achieved therewith, and the relatively small possibility of mantaining flexibility with regard to conditions of use and maintenance and the fulfillment of high sterile requirements. The present invention provides a method and filter which are not encumbered with such drawbacks. Thus, the cost of each unit of filtrate is low. Moreover, the invention enables beneficially high rotational speeds to be used. Flexibility with regard to use is also high. The method and filter according to the invention are particularly suited for use in biotechnical applications where demands on sterility are high. The word sterilization is used here as a common desig¬ nation for processes which are intended to reduce or elimi- nate the risk of spreading infection. It will be understood that the invention also pertains to such processes as pas¬ teurization and the like. The rotational motion is utilized, inter alia, to increase capacity and to improve journal and sealing functions. Thus, the invention relates to a method for application in conjunction with primarily so-called rotating filters of the kind in which the filter includes a substantially cylindrical filter tube which has a permeable tube wall and which is sealingly journalled at preferably two mutually spaced axial locations, preferably at the tube ends, for rotation about its longitudinal axis in a filter jacket; in which material to be filtered, the feed, is fed to a space between the fil¬ ter jacket and the filter tube; and in which filtered ma¬ terial, the filtrate, can be tapped from the interior of the filter tube. The method is particularly characterized by sealing and journalling the filter tube in a manner adapted to substan¬ tial temperature changes of the filter tube and in a steril- izible or like manner; by sterilizing and lubricating and cooling bearings and seals when applicable with the aid of sterilizing media; and by rotating the filter tube, when applicable, preferably at a relatively high speed. The invention also relates to a filter of primarily the so- called rotating kind which includes a substantially cylin¬ drical filter tube which has a permeable tube wall and which is journalled at preferably two axially spaced locations, preferably at the ends of the tube, for rotation about its longitudinal axis in a filter jacket; and with which filter material to be filtered, so-called feed, is intended to be fed to a space between the filter jacket and the filter tube, and the filtered material, the filtrate, is intended to be tapped from the interior of the filter tube. The filter is particularly characterized in that seals and bearings are arranged to take-up axial displacement movements and forces caused and created by substantial temperature changes in the filter tube; in that means are provided for sterilizing or similarly treating the filter tube; in that means are provided for sterilizing and for lubricating and cooling bearings and seals when applicable; and in that the filter tube is arranged for rotation at relatively high speeds. The invention will now be described in more detail with reference to exemplifying embodiments thereof and to the accompanying drawings; in which Figure 1 illustrates schematically and partially in axial section a first embodiment of a filter constructed in accordance with the invention; Figure 2 is an enlarged view of the right-hand part of Figure 1 ; Figure 3 illustrates schematically a second embodiment of end journal means intended for the same purpose as in the Figure 2 embodiment and seen as in Figure 2; Figure 4 is a schematic illustration of the filter shown in Figure 1, seen from the right in said Figure; Figure 5 illustrates schematically an embodiment of end journal means provided with a pump impeller, essentially in accordance, e.g., with Figure 2 and seen as in Figure 2; Figure 5a illustrates schematically a centrifugal pump impeller for use essentially in accordance with Figure 5; Figure 6 illustrates schematically a third embodiment of end journal means seen as in Figure 2; Figure 7 illustrates schematically and in axial section a filter which comprises a conical filter jacket; Figure 8 illustrates schematically and in axial section a filter having an internal suction box for back flushing, an end view being shown in Figure 8b; Figure 9 illustrates schematically and in axial section a filter having a back flushing section box, an end view being illustrated in Figure 9b; and Figure 10 illustrates schematically a fourth embodiment of end journal means seen as in Figure 2. In Figure 1 the reference 1 identifies a substantially cylin¬ drical filter tube which is provided with a liquid permeable wall and which in the illustrated embodiment is sealingly journalled at two axially separated locations, in this case at the tube ends. The tube is journalled for rotation about its longitudinal axis in a filter jacket 2. In the illus¬ trated embodiment, the filter jacket 2 is sealingly attached by means of flanges 2' at two end-cover parts 3 1 , 3", sealing rings 4 being provided peripherally between the flanges 2 ' and the end-cover parts 3 ' , 3". The one end- cover part 3 1 forms an attachment for a drive means, e.g. an electric motor 5 by means of which the filter tube 1 is ro¬ tated via a journal and sealing unit. The filter tube of this embodiment is connected to a shaft 6 to which torque is transmitted via a resilient coupling 7 and which is jour¬ nalled by means of ball bearings 8. The shaft 6 is passed sealingly through the end-cover 3 1 , the seal of the illus¬ trated embodiment being a double, mechanical plain seal 9. Located between the substantially large sealing surfaces of the double seal 9 is a space 10 to which a cooling and lu¬ bricating medium is supplied through channels not shown. The journalling and sealing unit is sterilized by means of ■ heat, e.g. by means of steam, via, inter alia, the space 10. The space 11 located between the filter tube 1 and the filter jacket 2 is intended to receive material to be filtered, so- called feed. Subsequent to passage through the wall 1 of the filter tube, the filtrate is tapped from the interior 12 of the tube. The space 11 can be placed under pressure to this end. The other end-cover part 3" carries attachment means for attachment of the end 1 ' of the tube 1 remote from the drive motor. The tube 1 is sealingly journalled to a non-rotatable shaft 13, which is connected to the end-cover 3" and jour¬ nalled for movement in the direction of the longitudinal axis of the shaft while maintaining the shaft sealed. The em¬ bodiment illustrated in Figure 1 is provided to this end with a journalling and sealing unit which comprises a double, mechanical plain seal 14 and includes a first part 15 which is sealingly journalled to the shaft 13 and includes an external, substantially cylindrical part 15', and further includes a second part 16 which is sealingly connected to the filter tube 1 and, when seen in the direction of the tube radius, is arranged essentially between the filter tube and said first part and includes an internal, substantially cy¬ lindrical part 16' which is sealed and axially displaceable in co-action with the external cylindrical part 15' of the first part 15, the filter tube 1 at said end 1 ' being seal¬ ingly fitted to said non-rotatable shaft 13. The reference 17 identifies sealing means intended for cooperation in said co-action. In the Figure 1 embodiment the journal means comprises two ball bearings 18. The reference 19 in Figures 1 and 2 identifies an impeller or like device which is in¬ tended to rotate with the filter tube about said axial di¬ rection and is herewith arranged in an existing cooling and lubricating system for cooling and lubricating the bearings of the journalling and sealing unit, and is here¬ with arranged to circulate coolant and lubricant for, inter alia, temperature equalizing purposes. The impeller 19 may be constructed in a number of ways, for example, may have a T-shaped cross-sectional profile as illustrated in Figure 1 , including grooves in the flange-like part facing the shaf 13, said grooves forming a given angle to said longi¬ tudinal axis. In the Figure 3 embodiment, the said first part 15 of the journalling and sealing unit for the tube end 1 * is arranged between axially sprung sealing devices 21, via sealing sur¬ faces 20. The two parts 15, 16 of this embodiment also in¬ clude substantially cylindrical parts 15', 16'. According to one preferred embodiment, the aforesaid non- rotatable shaft is provided with at least one axially ex¬ tending channel 22, Figure 4, which connects the interior 12 of the filter tube 1 with the outer surroundings of the fil¬ ter jacket. Thus, there is conveniently provided a channel 22 through which the filtrate can be tapped-off. Suitably a multiple of channels are provided, in Figure 4 illustrated as outlet openings in a connecting piece 23 arranged adjacent the shaft 13, such as a further channel 22, e.g., for supply¬ ing flushing and washing liquid and/or gas such as an inert shielding gas, to the interior of the filter tube, and channels 22", e.g., for measuring pressure, circulating coolant and lubricant for bearings, seals etc. In accordance with preferred embodiments the filter tube 1 has provided therein scavenger pipes, scavenger plates or the like for removal of filtrate from the interior 12 of the filter tube as the filter rotates, said rotational movement in the correct direction being capable of generating feed pressure. An embodiment which incorporates a scavenger pipe or tube 24 is illustrated schematically in Figures 1 , 2 and 4. When using scavenger plates, not shown, there is employed an impeller principle in which the impeller/plate is stationary and the liquid is imparted a rotational move¬ ment and is fed towards the centre of the impeller/plate. In the illustrated embodiment, in which the scavenger pipe 24 extends through the shaft 13, the discharge of filtrate can be adjusted by means of the pipe 24, which includes a part 24 ' which extends substantially in the direction of the longitudinal pipe axis and a further part 24" which is con¬ nected to said part 24 ' and extends at least partially ra¬ dially in the filter tube (1) , said further part 24" in¬ corporating at its free end 25 a filtrate inlet 26 which faces substantially tangentially in the filter tube and in which said axially extending part 24 ' is eccentrically lo¬ cated in the filter tube, so that the radial position in the filter tube of the filtrate inlet 26 adjacent said free end 25 can be adjusted by rotating the axially extending part about the longitudinal axis of said part, thereby displacing the inlet 26 in towards a plane extending essentially at right angles to said longitudinal axis, by pivoting the ra¬ dially extending part 24" about an eccentrically located longitudinal axis. A scavenger plate can be adjustably arranged in an essentially corresponding manner, by arranging for the diameter of the vane-plane of the plate or the like to be varied. The scavenger pipe of the illustrated embodi¬ ment is rotatable in the shaft 13 and protrudes therefrom and terminates in a knob or handle 13" and can be locked against rotation by means of a clamping device 27 or the like. - -o— According to one preferred embodiment, an impeller 28 or the like, Figures 2 and 5, is arranged at the end of the filter tube 1 journalled for axial displacement, and is capable of being rotated about said longitudinal axis by means of the tube 1 , the impeller or the like being intended to lower the pressure in central parts so as to relieve the pressure, either totally or partially, in the location of the seal 14 in the filter jacket. The impeller 28 is preferably a centrifuge-type impeller, although other kinds of impeller can be used of course. An impeller 28 is illustrated highly schematically in Figures 2 and 5. Figure 5a is a view of an impeller seen in the direction of its long axis and provided with vanes 28' or the like. Preferably the aforesaid impeller 28 or like device is also provided with vanes 29 or the like for advancing material axially in the filter jacket, such as the discharge of sludge or slime. When the vanes 28' and 29 are intended for similar feed functions the feed is effected subsequent to reversing the impeller, i.e. changing the direction of rotation. The reference 30 identifies fastener screws for an impeller 28 , which are shown arranged in a part 16 by way of example. Preferably, the filter jacket has arranged therein adjacent the inlet end of the tube 1 an impeller 31 or the like, referenced in Figure 1, i.e. adjacent the existing inlet 32 for material to be filtered, this impeller 31 or the like being intended to increase the pressure at said inlet so as to improve the feed of said material into the filter jacket 2 (i.e. the flow of the unfiltered liquid both along the filter tube and in a direction tangentially thereto) , and preferably for relieving, either totally or partially, the pressure prevailing in the vicinity of the journalling and sealing unit located adjacent said inlet in the filter jacket, in this case that part of the plain seal 9 located nearest the filter tube. In this case, the impeller may, e.g., be of the centrifuge type, and may also be arranged for axial feed in a direction away from the inlet 32. The reference 33 identifies an attachment in the end-cover of the tube 1 for an impeller 31. In the embodiment illustrated in Figure 6 journalling is effected with the aid of slide bearings. The aforementioned parts 15 and 16 are arranged essentially in the manner de¬ scribed with reference to Figure 1. The parts 15 and 16 of this embodiment are connected by means of a locking pin which prevents relative rotation between the locking parts 15 and 16. The locking pin 34 is constructed such that the tube 1 is journalled for axial movement in the aforedescribed' manner. The plain seals illustrated symbolically in Figure 6 can take-up a part of the aforesaid displacement movement. The construction of plain seals 20, 21 which are capable of tak- ing-up such axial displacement is illustrated in Figure 3. The reference 35 in Figure 3 identifies a scavenger pipe for complete scavenging of the filter tube, where the filter is intended to be used in a position in which its longitudinal axis extends substantially vertically, not shown in Figure 3, there being arranged in the tube 1 a similar space 36 in the vicinity of the lower end of the tube, this space being the last region to be rendered dry when emptying the filter tube, where the inlet opening 35' of the scavenger pipe 35 is lo¬ cated in the bottom part of the space 36 in order to enable the filter tube to be scavenged to a substantially dry state, the inlet opening of the scavenger pipe preferably having a small dimension and suitably combined with a scavenger pipe of standard dimensions. The space 11 may have arranged therein one or more baffles, /01899 _ -, n _ not shown, for creating turbulence and vigorous agitation in said space. Each baffle forms a gap with the filter tube, this gap being narrower than the radial distance be¬ tween the filter tube and the filter jacket. The use of baffles enables the turbulence in the space 11 to be in¬ creased, with subsequent increase in the capacity of the filter. A corresponding effect can be obtained by de¬ creasing the distance between the filter tube 1 and the filter jacket 2. This will also reduce the volume of un- filtered liquid. The filter jacket 2 of the filter embodiment illustrated in Figure 7 has a conical configuration, and therewith widens outwardly towards the end 2 ' at which the sludge or slime outlet is located and from where said sludge or slime Is removed. This filter jacket configuration facilitates sludge discharge. The method according to the invention and also the manner in which the filter according to the invention operates will be apparent in all essentials from the aforegoing. Thus, the material to be treated is fed through an inlet 32 to the space 11 located between the filter tube and the filter jacket, there being maintained in said space a pres¬ sure which deviates from the pressure prevailing in the filter tube. The filtrate entering the space 11 passes through the wall of the tube 1 under the influence of an overpressure relative to the pressure in the filter tube. A given variable through flow of material is maintained in the space 11, and a concentrate outlet 32 ' is preferably provided at the end of the filter opposite said inlet end. The filter tube is rotated at a suitable speed. The axially displaceable journal means enables a sealed journal to be maintained even when substantial changes in temperature etc. occur. The journal means, which can be sterilized, thus satisfy the high requirements placed on such seals and, when appropriate, the journals and seals are sterilized and lubricated and cooled by means of a sterilizing agent, such as steam. So-called back flushing or back washing, i.e. the passage of, e.g., filtrate through the wall of the filter tube from the interior 12 of the tube 1 out to the space 11 be¬ tween the tube 1 and the filter jacket 2, can be achieved through suitable facilities and is effected for the purpose of, inter alia, cleansing the active part of the filter and for removing unsuitable coatings, impurities, etc. liable to lower capacity, and, when appropriate,to cooperate in creating an effective filtering layer or cake on the filter tube 1 , such a cake being referred to as a so-called dynamic membrane. Back flushing can be effected by changing the pressure in the filter unit so as to decrease the pressure differential available for filtering across the filter, i.e. primarily the pressure differential between the spaces 11 and 12, the pressure in the space or chamber 11 being greater than the pressure in the space or chamber 12. When this pressure differential is decreased sufficiently, filtered liquid is forced by centrifugal force back through the wall of the rotating filter tube and into the space. 11. The back flushing thus effected flushes away particles and/ or loosens particles which would otherwise tend to block the filter and therewith lower the filtering capacity. Back flushing can be achieved at a given, relatively low pressure difference, by increasing the rotational speed of the tube 1. Furthermore, as the filter tube 1 rotates, and also the liquid forced through the tube 1 by back flushing, together with the liquid located externally of the tube, those particles which are nominally heavier than the medium, which may be liquid and/or gas, surrounding the tube 1 are propelled outwards in a direction towards the cylindrical surface of the filter jacket 2. The pressure differential can also be reduced by decreasing the pressure on the in¬ coming material to be filtered and/or on the outgoing un- filtered material, i.e. the concentrate, or by increasing the pressure and/or the quantity in the filter tube. i.e. the pressure in the space or chamber 12 τ This increase can be effected by supplying gas and/or liquid under suitable pressure through e.g., a flushing or washing pipe 22. Back flushing can also be effected by connecting the interior of the filter tube or the outer cylindrical surface thereof to a "suction box" 45. In the Figure 8 embodiment the suction box is arranged against the inner cylindrical surface of the tube 1 , and against the outer surface in the Figure 9 embodiment. Back flushing is effected once with each turn of the tube wall in each case. When scavenging pipes, scavenging plates or like devices are used, the amount of liquid available for back flushing purposes can be varied, inter alia, by adjust¬ ing the rotational position of the tube or by adjusting the diameter of the scavenging plate and therewith the amount of liquid in the filter tube. It will be understood, however, that the amount of available liquid can also be varied in other ways, e.g. by creating back pressure, rotational changes, etc. , and also through the amount of filtrate in scavenger pipes etc . and connecting systems. The filter is preferably sterilized with the aid of pressur¬ ized steam, which is introduced through the inlet 32. Steam, sterile hot oil, or the like, is also passed through the seals 9, 14 etc., the spaces 9*, 10* 13', 14' etc., forming part of the cooling and lubricating system being used to this end. In this regard a given overpressure is maintained in the sealing system filled with sterile medium, in order to prevent the unintentional ingress of undesirable media. For the purpose of avoiding underpressure, sterile medium, such as air or water, must be supplied, particularly when cooling the filter unit. Figure 3 illustrates an embodiment in which cooling and lubricating liquid, such as water, is supplied to one side of the journal means, as indicated by the arrows 20, and removed at the other side in a system which, by flushing clean at an overpressure, holds the bearing means shielded from the filtrate and concentrate, thereby avoiding, e.g., taste impairments as a result of oil impurities in the filtrate. An arrangement essentially according to Figure 3, in which the spaces are located, e.g., on both sides of the ball bearing 21 ', means and spaces can be arranged for, with the aid of a suitable medium, preferably when washing and/or sterilizing, heating the journal means for the purpose of de-watering lubricating grease. Means and spaces can also be provided for subjecting the bearing means to an under¬ pressure for the purpose de-watering lubricating grease. The filter is particularly constructed and suitable for forming and utilizing an additional filtering membrane in addition to the filter tube, with an external coating of filter fabric, filter net, or filter membrane of a kind suitable for the process concerned with regard to perme¬ ability (mesh size, pore size, etc.) , sensivity to tempera¬ ture and chemicals (sterilization etc.) , etc. Dynamic membranes can be formed with the aid of filter auxiliaries which can be supplied in various ways, e.g. with sterilizing medium, filtrate or feed, and maybe of varying kind, such variables as particle size, particle form, density, etc. being of significance. Filter auxiliaries, which may also comprise a constituent of the material to be filtered, can be fractionated into suitable fractions and orientated, by utilizing the rotational movement and varying the speed and/ or direction of said movement and/or varying the flow direc¬ tion of the material to be filtered, i.e. the through flow of material and/or the aforesaid back flushing. Unsuitable fractions which are less suitable for subse¬ quent filtration, can be removed, e.g., flushed away, upon completion of the fractioning process, by rotation, through- flow and/or back flushing. A suitable fraction or suitable fractions, rotects, or protect, the filter cloth or membrane and facilitates (facilitate) cleaning while reducing con¬ tamination with less suitable particles and also decrease the apparent average pore size or average mesh size in the filter, so as to render subsequent filtration more effective i.e. to provide a better filtrate with smaller particles with regard to both number and size. Examples of such less suitable particles are particles which tend to adhere, which are slimy or tacky and which therefore tend to block the filter cloth or the like and which may be difficult to remove when cleaning the filter. As beforementioned, a multiple of different types of particles can be used. By using filter auxiliaries of elongated form, such as thread form, and by varying the flow directions and flow rates between the connection 32 and 32', the rotational speeds and rotational directions of the filter tube 1 etc. , it is possible to weave a mat-like layer structure comprising various layers in which the layers have mutually different orientation. By utilizing available forces for activation by fractionation and orientation of such filter auxiliaries, it is also possible to "equalize" the filter fabric or the like, by blocking large holes or pores so as to obtain a smaller spread in hole size. Those forces available are mainly - forces which result from the flow through the filter, i.e. cross-flow from the feed inlet 32 to the concentrate outlet 32' - forces created by rotation of the filter tube 1, i.e. cross-flow perpendicular to the cross-flow mentioned above - forces deriving from a combination from the aforesaid flows caused by, e.g. the impeller 31 - centrifugal force created by rotation - forces created as a consequence of the density of the particle in relation to the liquid in which it is present, i.e. forces which impart to the particle the impulse to sink, hover or rise to the surface - forces resulting from cross-flow when a particle fastens in the filter surface and accompanies the tube 1 essentially circumferentially of the tube. It will be apparent from the aforegoing that the present invention provides a particularly flexible filtering process while fulfilling the extremely high demands placed in steril¬ ity. Although the invetion has been described with reference to embodiments thereof, it will be understood that other em¬ bodiments and minor modifications are conceivable within the scope of the inventive concept. For example, a conceivable embodiment is one in which, by selection, inter alia, of the direction of rotation, the filter cloth, membrane or the like can be firmly locked to the filter tube, applying overlapping ends in the circumferential direction. Embodiments are also conceivable in which the pressure ob¬ tained by scavenging pipes, scavenging pla_es or the like is utilized for supplying medium, e.g. the filtrate, to the system used for cooling and lubricating a journalling and sealing unit and in which the pressure differential across the seals is measured,in certain instances adjusted accordingly. Scavenging pipes or scavenging plates 46 can be arranged _ 1 , _ -16- within the journalling or bearing unit according to Figure 2 and 3, for pumping out any liquid which might have collected, so as not to subject (ball) bearings to such unsuitable liquids. The scavenging pipe or scavenging plates are preferably placed in the space or chamber 13 ' or adjacent the ball bearings 21 ' . Discharge is effected via the stationary shaft 13. One embodiment is illustrated in Figure 10. As Illustrated schematically in Figure 5, it may be con¬ venient in some instances to supply clean liquid when sealing in the space 14", this liquid being mixed with the concentrate by means of the impeller 28, via an additional seal 28" adjacent the end-cover 3". The clean liquid cleanses and protects the seal, and also facilitates dis¬ charge of the concentrate. Correspondingly, liquid can be admixed with the feed supplied to the inlet end. This mixture of liquid with the feed or the concentrate is facilitated by rotation of the filter tube and also by baffles, impellers, etc., when such devices are present. Embodiments are also conceivable in which the power con¬ sumption is measured, there being obtained a measurement of the concentration achieved, this measurement being used to control the process and to adjust, e.g., the viscosity of the concentrate. One or more impellers can be used in this case, in order to amplify the measuring signal. Suitable filter auxiliaries, particles, are often of a nature which will enable them to readily dissolve during a cleaning operation as a result of changes in temperature, pH or other parameters . Particles which will readily dis¬ solve in a suitable washing liquor or which can be readily flushed away may also be chosen. The permeable filter tube 1 can be arranged in a number of different ways. Thus, the tube may comprise a tubular body, which may be made of metal, a plastics material or some other material, and which has a perforated tube wall, or may com¬ prise a tube manufactured from a sinter material, such as metal sinter, metal ceramics or the like. According to one preferred embodiment, the tubular body is made of sintered stainless steel. The embodiment in which the tubular body is made of sintered metal, metal ceramic or ceramic affords important advantages with regard to stability and robustness. Such a filter tube can be cleansed from particles deriving from, inter alia, feed, and withstands high temperatures, chemicals, such as acid, etc. The tubular body is pre¬ ferably covered externally with at least one layer of filter net, filter fabric, filter membrane or filter paper. Several such layers may be placed on the tubular body ' . According to one embodiment the tubular body has provided thereon a filter support layer which forms a suitable support for a superimposed layer, which also functions as a draining ma¬ terial so that filtered liquid or backflushing liquid can flow laterally to suitable holes or suitable pores in the tubular body. One or more layers of filter fabric or the like can be placed on the drainage support layer. Said layer or layers can be coated externally with additional membranes such as dynamic membranes or precoats of filter auxiliary material or particles taken from the material to be filtered, or a combination of such particles, precoat and/or material for constructing a dynamic membrane, e.g. Zr- or Si- com¬ pounds or alcohols. In the aforegoing there has been described an embodiment which comprises an elastic, direct coupling between motor and drive shaft 6 for the filter tube. Embodiments are conceiv¬ able, however, in which a magnetic coupling, not shown, is provided between drive motor shaft and filter tube or a shaft connected to the filter tube. One advantage afforded here¬ by is that motor shaft and filter tube or filter shaft can be arranged in spaces which are totally separated from one another. One important drawback, however, is that relatively long displacement between the shafts can only be accepted for short periods of time when the transferable torque decreases as respective magnetic parts move from their intended mutual positions . A channel 22 may, as mentioned, be used for supplying gas, whereby the filtered liquid in the'interior 12 of the tube may be varied both regarding pressure and quantity. (Changes regarding back pressure, as discussed earlier In connection to back flushing may be performed by means of chang at the filtrate outlet outside the filter or inside the filter tube 1 via channel 22. Thus, the invention shall not be considered to be limited to the aforedescribed embodiments , since modifications can be made within the scope of the following claims.

Claims: CLAIMS 1. A method for application with primarily so-called ro¬ tating filters of the kind comprising a substantially cy¬ lindrical filter tube which is provided with a permeable wall and which is sealingly journalled, preferably at two axially separated location, preferably at the ends of the tube, for rotation about its longitudinal axis in a filter jacket, in which method material to be filtered, so-called feed, is supplied to a space located between the filter jacket and the filter tube, and in which filtered material, the filtrate, can be tapped from the interior of the filter tube, characterized by sealing and journalling the filter tube ( 1 ) in a manner adapted to substantial temperature changes of the filter tube; sterilizing and lubricating and cooling bearings and seals, when applicable, with the aid of sterilizing media; and by rotating the filter tube (1) , when applicable, at relatively high speeds. 2. A method according to Claim 1, characterized by utiliz¬ ing the rotational movement for discharging filtrate with the aid of a so-called scavenging pipe (24, 35) , scavenging plate or the like, it being possible to adjust said dis¬ charge by means of said scavenging pipe or the like. 3. A method according to Claim 1 or 2 , characterized by utilizing rotational movement for generating , by means of an impeller (19,28,31) or the like, pressure intended for feeding, pressure relieving, circulating, cross-flow, discharging of concentrate or like purposes. 4. A method according to Claim 3, characterized by in¬ creasing the infeed pressure of the material to be filtered by means of an impeller (31) . 8/01899 _ n _ -20- 5. A method according to Claim 3 or 4, characterized by generating pressure for relieving, either totally or parti¬ ally,pressure on seals (9, 14, 20) located adjacent a bear¬ ing. 6. A method according to Claim 3, 4 or 5, characterized by generating pressure for the discharge of concentrate, the filter jacket (2) preferably having a conical shape for facilitating said discharge, and said rotary movement being preferably used also for feeding concentrate mechanically, by means, e.g., of discharge vanes, both past the surface of the filter tube (1) and out of the filter unit. 7. A method according to Claim 1, 2, 3, 4, 5 or 6, charac¬ terized by utilizing scavenger pipe (24) or the like for varying the amount of filtrate in the filter and/or the amount of so-called backflushing liquid available, the shaft about which rotation takes place being eccentrically located, the tube opening (20) being capable of taking different radial positions in the filter tube (1) . 8. A method according to Claim 1, 2, 3, 4, 5, 6 or 7, characterized in that washing and cleansing are effected by backflushing,liquid being supplied from within the filter tube (1) in the filtrate through scavenger pipe, scavenger plate and/or separate flushing pipe and/or via the filter tube (1 ) through rotation. 9. A method according to Claim 1, 2, 3, 4, 5, 6, 7 or 8, characterized in that backflushing is effected by varying the pressure conditions volume ratio and/or rotation with regard primarily to speed. 10. A method according to Claim 1, 2, 3, 4, 5, 6, 7, 8 or 9, characterized by utilizing rotational movement in combi- nation with the flow from the inlet (32) to the outlet (32 ') of material to be filtered in the space between the filter tube and the filter jacket and/or the flow in the circumferential direction of the filter tube (1) resulting from said rotation and/or backflushing and/or particle density. 11. A filter primarily of the so-called rotating kind comprising a substantially cylindrical filter tube which has a permeable wall and which is sealingly journalled, preferably at two axially spaced locations, preferably at the ends of the tube, for rotation about its longitudinal axis in a filter jacket, material to be filtered, the so- called feed, being supplied to a space located between the filter jacket and the filter tube, and the filtered material, the filtrate, being tapped from the interior of the filter tube, characterized in that the seals (9, 14, 20, 21) and bearings of the filter tube (1) are constructed so as to take-up axial displacement movements and forces resulting essentially from changes in the temperature of the filter tube and are further constructed so as to enable said seals and bearings to be sterilized and lubricated and cooled by means of a sterilizing media; and in that the filter tube is preferably arranged for rotation at a relatively high speed. 12. A filter according to Claim 11, characterized in that when the filter tube is sealingly journalled at the tube ends, the filter tube is journalled at its one end (1 1 ) for axial displacement on a non-rotatable shaft (13) , while maintaining the sealing function, said shaft preferably being carried by an end-cover part (3") of the filter jacket (2) . 13. A filter according to Claim 12, characterized in that the tube end (1 r ) journalled for axial displacement has located adjacent thereto a journalling and sealing unit which comprises a first part (15) , which is sealingly journalled at said shaft (13) and includes an external, substantially cylindrical part (15') , and further comprises a second part (16) which is connected to the filter tube (1) and, when seen in the direction of the tube radius, is located essentially between the filter tube and said first part (15) , and in that the external second part includes an internal, substantially cylindrical part (16') which is sealed and axially displaceable and which co-acts with the external, cylindrical part (15') of said first part (15) , said end of the filter tube being sealingly fitted co saiu fixed shaft (13) . 14. A filter according to Claim 11, 12 or 13, characterized in that the journalling and sealing unit includes sealing parts which are mechanically displaceable in the axial di¬ rection and herewith arranged to take-up at least parts of said axial displacement. 15. A filter according to Claim 12, 13 or 14, characterized in that said fixed shaft (13) is provided with at least one axially extending channel (22) , which is arranged to connect the Interior (12) of the filter tube with the outside of the filter jacket (2) . 16. A filter according to Claim 12, 13, 14 or 15, charac¬ terized in that a pump impeller (28) or the like is arranged at the tube end (1 r ) journalled for axial displacement, and can be rotated about said axial direction by the tube; and in that the impeller or like device is arranged to lower the pressure at several parts for the purpose of relieving pressure, either fully or partially, adjacent the journalling and sealing unit in the filter jacket (2) . 17. A filter according to Claim 16, characterized in that the impeller (28) or like device is provided with vanes (29) or the like, for feeding material axially in the filter jacket (2) , such as discharging sludge or slime. 18. A filter according to Claim 12, 13, 14, 15, 16 or 17, characterized in that a pump impeller (31) or like device is arranged in the filter jacket (2) adjacent an inlet (32) for the material to be filtered; and in that the impeller (31) or like device is intended to increase the pressure at said inlet and to relieve the pressure, either fully or partially, in connection with journalling and sealing unit in the filter jacket (2) adjacent said inlet. 19. A filter according to Claim 11, 12, 13, 14, 15, 16, 17, or 18, characterized in that a scavenger pipe (24) , scavenger plate or the like is provided in the filter tube (1) for discharging filtrate from said tube, while utilizing the rotational movement thereof; and in that said scavenger tube, scavenger plate or the like is effective in adjusting the discharge of filtrate, such as the filtrate pressure. 20. A filter according to Claim 19, characterized in that discharge by means of the scavenger pipe (24) is control¬ lable by means of a scavenger pipe (24) which includes a part (24') which extends essentially parallel with the di¬ rection of the longitudinal axis of the filter tube (1) and a part (24") which extends at least partially in the direc¬ tion of the filter tube radius and which is connected to the first mentioned part (24') and the free end (25) of which part (24") includes the substantially tangential filtrate inlet (26) of the scavenger pipe, where said axially ex¬ tending part is located eccentrically in the filter tube so that the prevailing radial position of the filtrate inlet in the filter tube at said free end can be adjusted by pivot- ing the radially extending part (24") about an eccentrically located axially extending plane, preferably by pivoting said axial extending part about the longitudinal axis of said part. 21. A filter according to Claim 19 or 20, characterized in that in addition to the filtrate tapping pipe (22) , which connects the interior (12) of the filter tube with the out¬ side of the filter jacket, there is provided a flushing pipe (22) through which, e.g., flushing and washing liquid or gas, e.g. an inert protective gas, is supplied to the filter tube, and in that, when applicable, said connections between the filter tube and the outside of the filter jacket extend via a fixed shaft (13) on which one end (1) of the filter tube is sealing journalled. 22. A filter according to Claim 19, 20 or 21, characterized in that said scavenger pipe, scavenger plate or the like for discharging filtrate from the filter tube is adjustably arranged in a manner to enable the amount of filtrate in the filter tube to be controlled. 23. A filter according to Claim 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21 or 22, characterized in that turbulence in the space (11) located between the filter tube (1 ) and the filter jacket (2) is intended to be increased by decreasing the effective gap between the filter tube and the filter jacket, by providing in said space at least one so-called baffle and/or by making the radial distance between the filter tube and the filter jacket relatively small. 24. A filter according to Claim 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22 or 23, characterized in that a similar space (36) is arranged in the filter tube at a location ad¬ jacent the lower end of the tube, said filter tube being intended for use with its longitudinal axis extending essen¬ tially vertically, said similar space (36) being the last space to be rendered dry when emptying the filter tube; in that the inlet opening (35) of the scavenger pipe (35) is located in the bottom part of said similar space (36) in order to enable the filter pipe to be brought to an essen¬ tially dry state; in that the inlet opening of the scavenger pipe is preferably of small dimensions; and in that the inlet opening of the additional scavenger pipe is preferably connected to a pipe of normal dimensions . 25. A filter according to Claim 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23 or 24, characterized in that the filter jacket (2) has a substantially conical configuration and widens out towards the outlet end, such as to facilitate the discharge of e.g., sludge or slime. 26. A filter according to Claim 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24 or 25, characterized in that the body of the filter tube (1) is made of a sintered material, such as sintered metal, for example stainless steel.

Inventors: ALLSING KARL J, ALLSING, KARL, J.
Applicants: ALLSING KARL J, ALLSING, KARL, J.
Application year: 1987
Main classification: B01D33
IPC codes: B01D33