Abstract:
In order to provide a filter press which operates especially reliably and free of wear, a membrane for a membrane plate has a membrane surface enclosed by a membrane margin which is free of perforations. Furthermore, a membrane plate has such a membrane. Moreover, a chamber plate has a number of sludge inflows, each with an inflow orifice spaced apart from the chamber plate margin. Finally, a plate stack has a number of membrane plates and/or a number of chamber plates and also a corresponding filter press.

Description:
CROSS-REFERENCE TO RELATED APPLICATION  
       [0001]    This application is a continuation of copending International Application No. PCT/EP03/04635, filed May 2, 2003, which designated the United States. 
     
    
     
       BACKGROUND OF THE INVENTION  
         [0002]    1. Field of the Invention  
           [0003]    The invention relates to a membrane for a membrane plate, to a membrane plate and to a chamber plate for a filter press. The invention relates, furthermore, to a filter press.  
           [0004]    Membrane filter presses with an exchangeable membrane for solid/liquid separation are known from the prior art. Filter presses of this type can be employed in many different fields of use, for example sewage, chemistry, foodstuffs, metallurgy, pharmacy, etc. Chamber filter presses have filtration chambers that are formed by specially shaped plates. In this case, each chamber is provided at least on one side with a membrane. Every second plate can thus be configured as a membrane plate covered on both sides with membranes. If, then, a suspension flows under pressure into the closed filter press, a filter cake builds up on the filter, until the two cake layers have coalesced and the chambers have filled completely with solid. This first step of pressure filtration is followed by a second step, press filtration. In press filtration, the elastic membranes are inflated by a pressure medium, so that they expand and narrow the cake space. In this case, the cake embedded there is compressed, with the result that the residual moisture in the cavities of the cake is further reduced. By the use of press filtration, extremely high filtration pressures can be avoided during pressure filtration, thus leading to a saving in terms of investment costs and energy costs.  
           [0005]    To seal off the membrane in the membrane carrier plate, the membrane is provided with a peripheral bead that is introduced into and held in a likewise peripheral groove of the carrier plate. Under pressures of above 15 bar, however, the bead may be deformed in such a way that sealing no longer takes place and the pressure medium, for example air or water, can escape outward.  
           [0006]    In the known membrane plates, the membrane has an orifice, through which the sludge enters the filtration chamber. The membrane is in this case sealed off and fastened around the sludge bore. It has a sealing bead at this point and, furthermore, is connected to the membrane carrier plate by a flange or a clamping ring or clamping tube. In the region around the sludge inlet point, no cake or only a thin soft cake is formed during filtration. In the subsequent pressing operation, the membrane is then pressed into this depression in the cake and further on into the sludge bore. The fastening of the membrane in this region may cause the membrane to be overstretched at this point under pressures of above 15 bar and to tear apart after a short operating period or else be pulled out of the fastening.  
         SUMMARY OF THE INVENTION  
         [0007]    It is accordingly an object of the invention to provide a membrane, a membrane plate and a chamber plate for a filter press that overcome the above-mentioned disadvantages of the prior art devices of this general type, which operate particularly reliably and free of wear.  
           [0008]    With the foregoing and other objects in view there is provided, in accordance with the invention, a membrane for a membrane plate of a filter press. The membrane contains a membrane surface without perforations and having a plurality of supporting elements being ribs or bosses. The supporting elements each have a given surface. A membrane margin encloses the membrane surface. At least one planar region is disposed spaced apart from the membrane margin and has a surface larger than the given surface of one of the supporting elements and is positioned disposed opposite to a sludge inflow in a final mounting state with the membrane plate.  
           [0009]    The membrane according to the invention for the membrane plate, for insertion in a filter press, has a membrane surface which is enclosed by a membrane margin and which is free of perforations. The membrane is thus held solely by the press closing force of the opposite plate. No additional fastening elements, such as, for example, screws, flanges, rings or clamps, are provided for fixing the membrane to the membrane carrier plate. The opposite plate serves in this case as a stay. A more rapid mounting and dismounting of the membrane are thus possible. Owing to the simple geometry of the effective membrane surface, a homogeneous cake buildup is achieved. When the filter cake is washed out after filtration, a more uniform washing out can be achieved, since, due to the homogeneous cake buildup, channel or crack formations in the filter cake are avoided. The membrane material used is, for example, special polyethylene (PE), polypropylene (PP) or polyvinylidenefluoride (PVDF) materials, with the result that a good chemical resistance of the membrane, even at high temperatures, is achieved. Other special elastomers, such as EPDM, NBR, SBR, VITON, etc., may, however, also be used. During filtration, the highly elastic membrane adapts to the method-related unevennesses of the cake surface and to the different packing densities in the cake easily, without any permanent deformations, with the result that a uniform and more intensive expressing of the cake takes place.  
           [0010]    The membrane has a multiplicity of supporting elements. These supporting elements, configured in the manner of ribs or bosses, lead to a channeling of the membrane surface, the channeling serving for supporting the filter cloth formed preferably of felt or textile fabric and allowing the filtrate to flow out. The membrane surface is in this case preferably inert and hydrophobic. Since it also has a dirt-repelling action, a clogging of the outflow ducts is delayed or prevented. Furthermore, the surface of the supporting elements is relatively smooth, so that the load on the filter cloth due to friction between the filter cloth and the membrane surface is low.  
           [0011]    In a preferred embodiment, the membrane has a substantially planar region, the surface of which is larger than the surface of a supporting element. The planar region is in this case disposed so as to be spaced apart from the membrane margin. In the final mounting position of the plate stack, the planar region serves, inter alia, for distributing uniformly in all directions the sludge admitted into the filtration chamber and, for this purpose, in the final mounting position, is disposed opposite a sludge inflow.  
           [0012]    In the embodiment of the invention, the planar region has a reinforcement. This serves primarily for ensuring that the membrane, in its operating position, is not pressed into the sludge inflow during press filtration.  
           [0013]    Preferably, the reinforcement is a reinforced cross section of the membrane material, that is to say a thickening, in this region. The reinforcement of the membrane may be achieved alternatively or simultaneously in that a reinforcing material, formed of, for example, a plastic, metal or fabric, etc., is introduced into the membrane material. In both instances, the reinforcement of the membrane is preferably dimensioned such that, together with the supporting elements, a substantially plane membrane surface directed toward the filtration chamber and intended for supporting the filter cloth is formed.  
           [0014]    In a further preferred embodiment of the invention, the membrane has a peripheral bead for engagement into a groove of a membrane carrier plate, the bead having integrally formed on it a sealing lip, the sealing lip material of which has a lower Shore hardness than the bead material. The bead in this case serves both for fixing the membrane in the membrane carrier plate and as a sealing bead for sealing off the plate stack. The preferably peripheral sealing lip, attached as a kind of sealing ring to the bead, serves in this case, in particular, for sealing off the pressure chamber between the membrane underside and the membrane carrier plate. The lip is connected in one piece to the bead. If plastics are used as the sealing lip material and the bead material, the sealing lip is preferably fused together with the bead.  
           [0015]    The bead preferably serves at the same time as a support and therefore also as a seal between the membrane carrier plate and an adjacent plate, in particular a chamber plate.  
           [0016]    It is advantageous, furthermore, to provide the membrane margin with respect to the membrane surface with a sealing strip. The sealing strip is preferably integrally formed in one piece on the bead material and serves for additionally sealing off the filter cloth lying on the membrane surface, in particular for the elimination of leakages between the membrane and the filter cloth.  
           [0017]    Preferably, the bead material is identical to the membrane material. Therefore, the bead can be produced in a simple way together with the membrane. The bead and the membrane are in this case preferably produced in one piece.  
           [0018]    In a particularly preferred embodiment, the bead material has a Shore hardness of about 90° ShA. Owing to this high hardness, the bead is not deformed, even under high pressures, thus leading to a particularly reliable functioning of the membranes. By contrast, the sealing lip material has a lower Shore hardness than the bead material. The Shore hardness of the sealing lip material preferably amounts to 70±5° ShA. The Shore hardness of the sealing lip material therefore differs from the Shore hardness of the bead material (90±5° ShA) by 10 to 25° ShA. The thus substantially softer sealing lip, when acted upon by pressure, is pressed onto the gap between the bead and the groove wall of the membrane carrier plate, thus leading to particularly reliable sealing off.  
           [0019]    For particularly effective sealing off, the bead is configured in the manner of a U-shaped holding projection formed of a solid material, the sealing lip being integrally formed on the outer lower edge of the holding projection. In other words, the sealing lip is located in the gusset between the U-bottom and the U-leg, facing the margin of the membrane carrier plate, of the holding projection.  
           [0020]    The sealing lip material and the bead material are in this case preferably configured differently in terms of color. As a result, it can easily be detected, both during the production of the membrane and during the maintenance of the membrane, whether the sealing lip is integrally formed on the bead, as desired, or whether an exchange of the membrane becomes necessary.  
           [0021]    The membrane plate according to the invention has a membrane carrier plate with a carrier plate margin for contacting at least one chamber plate. When the membrane plate, preferably formed of a thermoplastic, such as PP, PE, PVDF or the like, or of a metal, in particular aluminum, contacts an adjacent chamber plate, a filtration chamber is formed between the membrane topside and the chamber plate. Furthermore, the membrane plate according to the invention has a membrane as described above. The margin of the membrane in this case ends in front of the carrier plate margin of the membrane carrier plate, the carrier plate margin serving as the actual sealing surface. The membrane is in this case inserted into a peripheral groove provided on the membrane carrier plate. The groove and bead in this case preferably form an uninterrupted holding or sealing ring. The groove or the bead may, however, also be interrupted by transverse elements, for example inflows or outflows. In other words, preferably, there is no firm connection by screwing or welding between the membrane and the membrane carrier plate in the region of the sealing margin. During press filtration, the pressure of the after-pressing medium can be maintained only with the filter press closed. If a membrane internal pressure prevails when the press is open or is opening, the membrane moves out of the groove, a safe release of pressure taking place, without the membrane being destroyed. The outlay for safety precautions is thereby considerably reduced.  
           [0022]    The membrane plate according to the invention ensures a particularly reliable operation of the filter press due to the use of the membrane according to the invention that is exchangeable inside or outside the press. Since the membrane is not interrupted by a sludge inlet, during pressure filtration it can come to bear with its entire membrane underside onto the surface of the membrane carrier plate. This makes it possible to have an especially uniform buildup of the filter cake. Owing to the especially simple configuration both of the membrane and of the fixing of the membrane on the membrane carrier plate, the membrane plate can be produced particularly robustly and cost-effectively. The membrane plate is in this case suitable for all pressure media, such as, for example, air, water or oil.  
           [0023]    A membrane plate that is constructed mirror-symmetrically about its longitudinal center axis, is especially advantageous. A membrane can thus be held on both sides of the membrane carrier plate, so that the membrane plate has two operative sides.  
           [0024]    The chamber plate for a filter press, which, like the membrane plate, has a plate margin for contacting at least one adjacent plate, possesses a number of sludge inflows for introducing the sludge into the filtration chamber. According to the invention, at least one sludge inflow is provided for each chamber plate. However, a plurality of sludge inflows may also be disposed in a chamber plate. This is expedient especially where large plate sizes are concerned. The sludge inflow in this case has an inflow orifice that is disposed so as to be spaced apart from the chamber plate margin. Like the membrane plate, too, the chamber plate is formed of a thermoplastic or metal. The sludge inflow in the form of a duct or of a bore can therefore be worked into the chamber plate simply by machining. The filter cloth bearing on the chamber plate surface is advantageously fixed to the preferably round inflow orifice by a holding flange or a similar fastening element. It is advantageous, furthermore, that the filter cloth for the chamber plate can be produced particularly simply. Special machining of the orifice margins of the filter cloth orifice in the region of the inflow orifice is not necessary.  
           [0025]    It is particularly advantageous if an individual connection is provided for each sludge delivery line on each chamber plate. For example, for supplying sludge to the individual filtration chambers, an external connecting line may be provided, to which the chamber plate is connected by releasable hoses. This affords a simple possibility of checking whether all chambers are filled with sludge. A reliable and uniform filling of the chambers is important, especially in the case of high pressures, so that uniform deflection of the membrane over the entire filter surface and consequently the least possible load on the membrane are ensured.  
           [0026]    Preferably, the inflow orifice adjoins an inflow duct which serves as a sludge duct and which extends from the chamber plate margin into the chamber plate interior. The inflow duct in this case runs from the outside of the chamber plate margin as far as the inflow orifice and may in this case be disposed both parallel to the longitudinal direction of the chamber plate and at an angle thereto. An oblique configuration of the inflow duct leads, especially in conjunction with a conical cross-sectional run of the inflow duct, to an especially reliable filling of the filtration chamber with the sludge. The length of the inflow duct is dimensioned according to the size of the filtration chamber. The inflow duct is preferably dimensioned in such a way that the inflow orifice is at a sufficient distance from the margin of the filtration chamber to ensure a sufficiently uniform filling of the filtration chamber. On the other hand, too long an inflow duct is to be avoided, so as to avoid unnecessary contamination of the inflow duct and therefore the susceptibility of the latter to faults.  
           [0027]    In a further preferred embodiment of the invention, an outlet duct extends, in the region of the inflow orifice, substantially perpendicularly to the longitudinal direction of the chamber plate. This ensures that the sludge emerging from the inflow orifice impinges substantially perpendicularly onto the opposite membrane of the membrane plate, in order to ensure a uniform distribution of the suspension in the filtration chamber.  
           [0028]    Preferably, the sludge inflow has a non-return element, which is especially advantageous. The non-return element, which is preferably configured in the form of a non-return flap or a non-return valve, serves for shutting off the inflow orifice in the direction of the inflow duct. The sludge located in the filtration chamber or a soft filter cake therefore cannot escape through the inflow duct during expressing in the course of press filtration, with the result that a blockage is prevented. The membrane is likewise prevented from being pressed into the inflow orifice during press filtration.  
           [0029]    The chamber plate is preferably constructed mirror-symmetrically about its longitudinal center axis. Therefore the inflow duct that is disposed centrally in the chamber plate has adjoining it two outlet ducts which at their ends form two inflow orifices into adjacent filtration chambers.  
           [0030]    A plate stack according to the invention for a filter press has a number of membrane plates as mentioned above and a number of chamber plates also as mentioned above. The individual, mostly square plates are disposed alternately next to one another. The plate stack obtained as a result is preferably clamped on its entire circumference in a filter press frame between a fixed headpiece and a movable endpiece by a closing device. In this case, the plates are preferably disposed vertically.  
           [0031]    Preferably, the inflow orifice in the chamber plate is disposed opposite to the planar region of the membrane. The planar region is in this case configured and disposed in such a way that it completely covers the inflow orifice. In other words, the planar region overlaps the orifice margins of the inflow orifice in the chamber plate when the outlet duct is viewed perpendicularly to the longitudinal direction of the chamber plate. During expressing in the course of press filtration, the membrane is therefore laid with the reinforcement onto the sludge inflow or into the region of the incompletely formed filter cake. The membrane is likewise prevented from being pressed into the inflow orifice during press filtration. The holding flange fixing the filter cloth to the chamber plate serves in this case additionally as a supporting surface for the membrane.  
           [0032]    A filter press according to the invention ensures a particularly safe and reliable work sequence.  
           [0033]    Since critical points are avoided with the perforation-free membrane, the membrane has a substantially higher load-bearing capacity and is consequently more reliable. A filter press according to the invention can therefore operate in a pressure range of up to at least 50 bar pressing pressure, without the membrane being subject to excessive load. Due to the high pressing pressure, the filtration time can be reduced considerably. However, even when a lower expressing pressure, for example up to 15 bar, is used in press filtration, the membrane according to the invention can be employed. All the individual parts of the invention can therefore be used both in the case of low pressures and in the case of extremely high pressures, thus ensuring universal use.  
           [0034]    The membrane according to the invention can be employed both with a membrane plate according to the invention and with other membrane plates which allow this membrane to be used. The membrane plates according to the invention can likewise be employed both with the chamber plates according to the invention and with other chamber plates suitable for this purpose. The membrane plates and chamber plates according to the invention may also be employed in conventional filter presses, for example using deflection or adapter plates. Overall, a membrane chamber filter press with an uncomplicated construction, which is simple to maintain and has high functional reliability, is obtained.  
           [0035]    It may be gathered from the foregoing that the present invention not only relates to the corresponding devices, but also to a method for operating a filter press.  
           [0036]    Other features which are considered as characteristic for the invention are set forth in the appended claims.  
           [0037]    Although the invention is illustrated and described herein as embodied in a membrane, a membrane plate and a chamber plate for a filter press, it is nevertheless not intended to be limited to the details shown, since various modifications and structural changes may be made therein without departing from the spirit of the invention and within the scope and range of equivalents of the claims.  
           [0038]    The construction and method of operation of the invention, however, together with additional objects and advantages thereof will be best understood from the following description of specific embodiments when read in connection with the accompanying drawings. 
       
    
    
     BRIEF DESCRIPTION OF THE DRAWINGS  
       [0039]    [0039]FIG. 1 is a diagrammatic, top plan view of a membrane according to the invention;  
         [0040]    [0040]FIG. 2 is a diagrammatic, sectional view of a membrane plate according to the invention;  
         [0041]    [0041]FIG. 3 is a diagrammatic, sectional view of a chamber plate according to the invention; and  
         [0042]    [0042]FIG. 4 is a diagrammatic, sectional view through the membrane plate according to the invention in contact with the chamber plate according to the invention. 
     
    
     DESCRIPTION OF THE PREFERRED EMBODIMENTS  
       [0043]    Referring now to the figures of the drawing in detail and first, particularly, to FIG. 1 thereof, there is shown a top view of a membrane  1  according to the invention. The membrane  1  is in this case fixed to a membrane carrier plate  2 . In this case, a peripheral bead  4 , illustrated in FIG. 1 by a broken line, which is attached to a membrane underside  3  engages into a correspondingly shaped groove  5  on the membrane carrier plate  2 . A multiplicity of bosses  7  as supporting elements for a non-illustrated filter cloth are attached to a membrane surface  6 . The boss interspaces form outflow ducts  8 , through which the sludge can flow out during filtration. The outflow ducts  8  have adjoining them ducts which correspondingly lead further on and are in the form of outflow bores  9  which finally lead the sludge into corner bores  10  formed in the corners of the essentially square membrane carrier plate  2 . The outflow ducts  8  and outflow bores  9  are dimensioned in such a way that even large filtrate quantities are delivered quickly and clogging or blockage by solids and/or crystallizing out are largely avoided. The bosses  7  are bordered by a membrane margin  11 . Spaced apart from the membrane margin  11 , on the membrane surface  6 , are disposed plane or planar regions  12  which, as compared with an individual boss  7 , have a larger surface that is not interrupted by an outflow interspace  8 .  
         [0044]    [0044]FIG. 2 shows a section through a membrane plate  13  according to the invention that is constructed mirror-symmetrically with respect to its longitudinal center axis  14 . The membrane plate  13  in this case contains the membrane carrier plate  2  and two of the membranes  1  held on opposite sides of the membrane carrier plate  2 . The membrane carrier plate  2  has a thickened membrane plate margin  15 . The membrane plate margin  15  carries, spaced apart from an end face  16 , a peripheral groove  5  having a substantially U-shaped cross section.  
         [0045]    Adjacent to the groove  5  in the direction of the center of the membrane plate  13 , the membrane carrier plate  2  narrows in cross section. As a result, a pressure chamber  17  is formed between the membrane carrier plate  2  and the membrane  1  held on the latter, the membrane underside  3  running substantially parallel to the membrane carrier plate  2  in the non-loaded state of rest. The pressure chamber  17  is connected to the collecting line of a pressure medium by an individual connection by a non-illustrated connecting bush attached to an end face  16  of the membrane carrier plate  2  from outside.  
         [0046]    The peripheral bead  4  closing off the membrane  1  is of a substantially U-shaped configuration, in the final mounting position a U-bottom  18  runs substantially parallel to a bottom  19  of the groove  5  which bears on the U-bottom  18 . Two U-legs  20  of the bead  4  bear simultaneously on groove walls  21 , so that the bead  4  is seated in the groove  5  in the manner of a holding projection. The outer, that is to say end-face lower edge  20  of the holding projection has formed on it a sealing lip  23 . The latter is connected in one piece to the bead material. In the position shown here, the press closing force of a non-illustrated opposite chamber plate prevails, so that the sealing lip  23 , by virtue of its softness, is already pressed completely into the contour of the groove  5 .  
         [0047]    In the direction toward the end face  16  of the membrane plate  13 , the membrane  1  is closed off by the membrane margin  11  that is seated in a receiving edge  24 , provided for this purpose, of the membrane carrier plate  2 . The membrane margin  11  is closed off toward the membrane surface  6  by a sealing strip  25  that is preferably integrally formed in one piece on the bead material. The sealing strip  25  serves for additional sealing off by a filter cloth  26  resting on the membrane surface  6 , in particular for the elimination of leakages. The filter cloth  26  rests both on the individual bosses  7  of the membrane  1  and on the planar region  12  of the membrane  1 . The planar region  12  is in this case reinforced by a thickening of the membrane material in such a way that the membrane  1  has the same cross-sectional thickness here as in the region of a boss  7 .  
         [0048]    [0048]FIG. 3 shows a chamber plate  27  according to the invention that, like the membrane plate  13  in FIG. 2, is constructed mirror-symmetrically about its longitudinal center axis  28 . The chamber plate  27  has a chamber plate margin  29  that, as in the case of the membrane plate  13 , is thickened in a bead-like manner. In the final mounting position, the plate margins  15 ,  29  running parallel to one another bear in this case on one another and form a filtration chamber for receiving the suspension. The chamber plate margin  29  has adjoining it in the direction of the center of the chamber plate a sealing margin slope  30 , along the run of which the cross section of the chamber plate  27  narrows, so that a filtration space is obtained between the chamber plate  27  and the membrane  1  of a non-illustrated adjacent membrane plate  2 . Furthermore, the chamber plate  27  has disposed in it a sludge inflow that contains an inflow duct  31 . The duct  31  leads from the end face  32  of the chamber plate  27  through the chamber plate margin  29  and the sealing margin slope  30  into an interior of the chamber plate  27 . The duct  31  ends there in a T-shaped end-piece  33  which is closed off by two inflow orifices  34 . The two inflow orifices  34  connect the inflow duct  31  to the two filtration chambers which lie on opposite sides of the chamber plate  27 . The outlet duct  33  in this case extends in the region of the inflow orifice  34  substantially perpendicularly to the longitudinal direction of the chamber plate that runs parallel to the longitudinal center axis  28 . Adjoining the region of the inflow orifice  34  in the direction of the center of the chamber plate  27 , the chamber plate  27  has the bosses  7  which, as already known from the membrane  1 , serve as supporting elements for the filter cloth  26  which covers the entire chamber plate surface. In the region of the inflow orifice  34 , the filter cloth  26  is fixed to the chamber plate  27  by a holding flange  35 . To receive the holding flange  35 , the chamber plate  27  has a receiving region  36  that is obtained by a further narrowing of the cross section of the chamber plate  27 . The holding flange  35  and the receiving region  36  are in this case configured in such a way that the surface of the holding flange  35  seated in the receptacle  36  lies in one plane with the surface of the bosses  7  of the chamber plate  27 .  
         [0049]    Finally, FIG. 4 shows part of a plate stack  37  according to the invention, with the membrane plate  13  according to the invention and with the chamber plate  27  according to the invention bearing on the latter. By a press pressure, the two plates  13 ,  27  contact one another in the region of their plate margins  15 ,  29 , with the result that the bead  4  of the membrane  1  is firmly fixed in the groove  5  of the membrane carrier plate  2 . A filtration chamber  38  is formed between the chamber plate  27  and the membrane  1  of the membrane plate  13 . When, during press filtration, the pressure chamber  17  is filled by a non-illustrated pressure medium connection present in the membrane carrier plate  2 , the membrane  1  presses onto the filter cake in the direction of the chamber plate  27 . The planar region  12  of the membrane  1  is in this case disposed and dimensioned in such a way that, in the case of a sufficiently high pressure, it is laid onto the inflow orifice  34  and at the same time overlaps orifice margins  39  of the latter. A penetration of the membrane  1  into the inlet orifice  34  is thereby ruled out.