METHOD AND APPARATUS FOR OPERATING A SCREENING WHEEL FILTER

Abstract

A method and an apparatus for operating a screening wheel filter for high-viscosity melts with pressures of >10 bar and temperatures of >90° C., wherein a screening wheel (1) is rotationally driven step by step, and screening inserts (2) arranged in the screening wheel (1) are successively subjected to a stream of cleaning agent produced by a cleaning agent drive (9) in a backflushing cleaning station, are to be optimized in such a way that less cleaning agent is used, better cleaning of the screening inserts takes place and a saving of energy is ensured. For this purpose it is proposed that the cleaning backflushing in the backflushing cleaning station takes place during the rotation of the screening wheel (1), wherein an open-loop or closed-loop control device (7) assigned to the cleaning agent drive (9) is used to set the amount of cleaning agent and/or the pressure of the cleaning agent and/or the flow rate of the cleaning agent in dependence on the rotational speed of the screening wheel (1) and/or in dependence on a differential pressure prevailing at the screening inserts (2) located in the melt channel (4) and the effective opening of the slot die normal to the radial is less than the distance covered by the screening wheel (1) during a driving step.

Description

The invention relates to a method of operating a sieve-wheel filter for high-viscosity melts with pressures of >10 bar and temperatures of >90° C., the sieve wheel being rotated in steps and mesh inserts arranged in the sieve wheel in a back-flushing station being successively traversed by a stream of cleaning agent generated by a cleaning-agent supply, as well as to a sieve-wheel filter for executing the method.

Sieve-wheel filters with a corresponding back-flushing station belong to the prior art as presented, for example, by DE 103 26 487 [U.S. Pat. No. 7,411,163]. In such sieve-wheel filters, mesh inserts located in the melt conduit are rotated away from the melt conduit via a drive that acts on the sieve wheel and switched with cleaned mesh inserts. The back-flush cleaning station lies as close as possible upstream of the melt conduit in the direction of rotation; during filter operation in the back flush cleaning station, i.e., when the sieve wheel is stationary, the mesh insert located in the back-flushing station is traversed with cleaning agent by a stream generated in the cleaning-agent supply.

The back-flushing station is operated during down times of the filter wheel. Here, a portion of clean melt from the already-cleaned melt flow is fed to the cleaning-agent supply, here a shootback plunger, in the back-flushing station. Upon actuation of the shootback plunger, the melt—which acts as a cleaning agent—is forced through the mesh insert. The mesh insert is traversed by the cleaning agent counter to the usual sieve-flow direction, taking contaminants that have collected on the mesh insert along with it and then guiding them toward an outlet. After cleaning of the mesh insert, it can be rotated a step further and moved to alignment with the melt conduit.

To enable complete cleaning of the mesh insert when the sieve wheel is at a standstill, the size of the back-flush nozzle corresponds at least to the angular dimension of a single rotation step.

In this regard, it is disadvantageous that, given the required size of the back-flush nozzle, large quantities of cleaning agents are required in order to saturate the mesh insert over the required width with the cleaning agents. Particularly at edges of the mesh inserts, insufficient cleaning often occurs because the melt pressure of the back-flushing station is often no longer sufficient there.

DE 39 02 061 [U.S. Pat. No. 5,090,887] discloses a screening device for cleaning plastic melts in which, during rotation of the sieve wheel, cleaning is performed of the mesh inserts located in the back-flushing station. Advanced by the pressure prevailing in the melt conduit, the already cleaned melt flows through the mesh inserts counter to the usual filter-flow direction. A cleaning-agent supply is not proposed. Effective, melt-saving cleaning is not possible.

According to CH 593 786, the already cleaned melt flows constantly through the mesh inserts as a result of the pressure prevailing in the melt conduit. Here, too, no actively functioning cleaning-agent supply is provided. As a result of the continuous cleaning process, an especially large amount of the cleaning agent, i.e. the melt, is wasted.

It is the object of the invention to optimize the back flushing and cleaning of mesh inserts in such a way that less cleaning agent is wasted, better cleaning of the mesh inserts occurs, and energy savings is ensured.

To achieve this object, according to the method the back flushing in der back-flushing station is carried out during rotation of the sieve wheel, the quantity and/or the pressure and/or the flow speed of the cleaning agent being adjusted via a controller working with or without feedback and connected to the cleaning-agent supply as a function of the temporal course of the rotation of the sieve wheel and/or as a function of the rotational speed of the sieve wheel and/or as a function of a differential pressure across the mesh insert in the melt conduit.

This way, during the back-flushing process, the back-flush nozzle is always facing new regions of the mesh insert to be cleaned, thus enabling better cleaning even at the edges of the mesh insert.

What is more, in the known sieve-wheel filters, the sieve wheel must always be rotationally driven against the pressure that has built up in the melt conduit. That is, the sieve wheel is pressed by the melt against an inner face of the housing of the sieve-wheel filter, whereby adhesions and/or tilting of the sieve wheel in the sieve wheel housing can occur, and the frictional resistance between sieve wheel and sieve wheel housing inner surface is increased substantially in any case.

According to the invention, counterpressure against the sieve wheel occurs during rotation of the sieve wheel as a result of the simultaneous back-flushing process, whereby less force is required to drive the sieve wheel. Even in the case of poorly lubricating melts, the resistance between sieve wheel and housing wall of the sieve-wheel filter is reduced substantially, thus avoiding blockages. By adjusting the quantity and/or the pressure and/or the flow speed of the cleaning agent, which can be varied individually or in combination during rotation, optimum and resource-saving cleaning can be performed.

Depending on what materials are being processed, it is possible according to the invention to react to their specific characteristics and desired rotational speeds of the sieve wheel in a trouble-free manner.

In order to possibly achieve an even better cleaning result depending on the melt being used, according to the invention the back flushing occur in the back-flushing station not only during rotation of the sieve wheel, but rather at least also occasionally during standstill of the sieve wheel.

As a result, it is possible, for example, to continue back flushing or to already perform back flushing shortly after completion of the rotation or before commencement of rotation in order to thus achieve even more optimum cleaning of the mesh inserts during transition between two rotation steps.

It is advantageous if the controller increases at least the cleaning-agent pressure relative to the pressure profile during the rotation of the sieve wheel (1) parallel to the start-up process for the rotation of the sieve wheel (1).

In this way, freeing of the sieve wheel that is sticking or tilting in the housing as a result of the preceding standstill is facilitated. The peak load of the rotary drive is reduced as a result of the freeing during starting of rotation, and a lower-performance, more cost-effective rotary drive can be used that is also more cost-effective to operate.

The object underlying the present invention is achieved in terms of the apparatus by a sieve-wheel filter for high-viscosity melts with pressures of >10 bar and temperatures of >90° C., with a sieve wheel holding mesh inserts, and a drive associated with the sieve wheel, as well as with a back-flushing station and a back-flush nozzle embodied as a slit nozzle downstream from a cleaning-agent supply in the direction of flow of the cleaning agent, in that a controller is provided that is capable of adjusting the quantity and/or the pressure and/or the flow speed of the cleaning agent via the cleaning-agent supply as a function of the temporal course of the rotation of the sieve wheel and/or as a function of the rotational speed of the sieve wheel and/or as a function of a differential pressure prevailing on or in the mesh insert located in the melt conduit, and that the effective opening of the slit nozzle is at least equal in its radial dimension to that of a mesh insert located in the back-flushing station, and that the effective angular width of the slit nozzle normal to the radial is smaller than the path traveled by the sieve wheel during an operation step.

By virtue of the inventive construction of the slit nozzle, all of the regions of a mesh insert along its radial extent are passed over by the nozzle, whereas the dimension normal to the radial dimension is formed narrow so that the pressure of the cleaning agent built up in the cleaning-agent supply ensures optimum cleaning of the filter insert.

In this regard, it is worthy of emulation if the slit nozzle has a radial length corresponding to the radial dimension of the mesh inserts to be cleaned and an angular width of 5 mm, or an angular width that corresponds to <7% of the radial length of the slit nozzle. Upon rotation of the filter insert, new regions of the filter insert are always moved upstream of the slit nozzle, thus enabling optimum cleaning during rotation.

It has proven advantageous for a pawl drive that engages on the periphery of the sieve wheel to be associated with the sieve wheel.

For one, the sieve wheel can be driven quickly via the pawl drive. For another, relatively large angles of rotation per drive segment can be achieved, and optimum cleaning of the mesh inserts is ensured despite the quick exchanging of the mesh inserts in the melt conduit. This also enables an especially good response to surge contaminants occurring in the melt conduit. A quick exchange of the fouled mesh inserts with simultaneous optimum cleaning of the mesh inserts to be rotated into the melt conduit ensures a highly variable operation of the sieve-wheel filter that is capable of reacting to all possible contamination situations.

Nonetheless, commensurately large angles of rotation can also be achieved by a toothed wheel of a motor engaging on the periphery of the sieve wheel or through gearing coupled therewith or a freewheel driven by a lifting cylinder.

The invention is described in further detail with reference to a drawing.

The FIGURE is a schematic view of a sieve wheel 1 in which two mesh inserts 2 and 2′ are shown to represent a large number of mesh inserts. The mesh inserts 2 are set between bars 3, 3′, 3″ resting against the inner wall of a sieve-wheel filter housing. The mesh insert 2 is aligned with a melt conduit 4, and the mesh insert 2′ is aligned with a cleaning slot 5 of the back-flushing station. It can clearly be seen that the cleaning slot 5 has a substantially greater radial length than the mesh insert 2′ but a substantially smaller angular width perpendicular to the radial direction than the mesh insert 2′ and than an angular travel 6 per rotational step.

A controller 7 working with or without feedback has an input 8 for loading parameters and on the other hand receives via a data connection 10 input such as differential pressure, rotational speed, charge state of the cleaning-agent supply 9, etc. The controller 7 can influence the rotary drive 12 and/or the cleaning-agent supply 9 through a control port 12 in a manner according to the invention.

OVERVIEW OF REFERENCE NUMBERS

1 sieve wheel 7 controller

2 mesh insert 8 input

3 bars 9 cleaning-agent supply

4 melt conduit 10 data connection

5 back flushing slot 11 control port

6 angle of rotation 12 rotary drive

Claims

1. A method of operating a sieve-wheel filter for high-viscosity melts with pressures of >10 bar and temperatures of >90° C., the method comprising the steps of: rotating a sieve wheel in steps such that mesh inserts set in the sieve wheel are successively passed through a back-flushing station and through a filtering station aligned with a melt conduit;forcing a stream of cleaning agent from a cleaning-agent supply during rotation of the sieve wheel through the inserts when in the back-flushing station;adjusting by a controller connected with the cleaning-agent supply the quantity and/or pressure and/or flow speed of the cleaning agent as a function of the temporal course of the rotation of the sieve wheel and/or as a function of the rotational speed of the sieve wheel and/or as a function of a differential pressure across the mesh insert in the melt conduit; andduring start-up of rotation of the sieve wheel, setting at least the cleaning-agent pressure higher than the pressure during rotation of the sieve wheel.

2. The method of operating a sieve-wheel filter defined in claim 1, wherein the back flushing in the back-flushing station is carried out during rotation of the sieve wheel and at least occasionally during standstill of the sieve wheel.

3. (canceled)

4. A sieve-wheel filter for high-viscosity melts with pressures of >10 bar and temperatures of >90° C. for carrying out the method defined in claim 1, the filter comprising: a sieve wheel holding mesh inserts;a rotary drive associated with the sieve wheel for rotating the wheel;a back-flushing station having a back-flush slit nozzle;a cleaning-agent supply connected to the slit nozzle for feeding cleaning agent thereto; anda control means for adjusting the quantity and/or the pressure and/or the flow speed of the cleaning agent via the cleaning-agent supply as a function of the temporal course of the rotation of the sieve wheel and/or as a function of the rotational speed of the sieve wheel and/or as a function of a differential pressure across the mesh insert in the melt conduit, the effective opening of the slit nozzle having a radial length at least equal to a radial dimension of a mesh insert in the back-flushing station, an angular width of the slit nozzle normal to the radial being smaller than an angular distance traveled by the sieve wheel during a drive step.

5. The sieve-wheel filter defined in claim 4, wherein the radial length of the slit nozzle corresponds to the radial dimension of the mesh inserts to be cleaned and the angular width is <5 mm.

6. The sieve-wheel filter defined in claim 4, wherein the radial length of slit nozzle corresponds to the radial dimension of the mesh inserts to be cleaned and a width that corresponds to <7% of the radial length of the slit nozzle.

7. The sieve-wheel filter defined in claim 4, wherein a pawl drive engaging on the periphery of the sieve wheel or a toothed wheel of an engine or of gearing coupled therewith or of a freewheel driven by a lifting cylinder engaging on the periphery of the sieve wheel is associated with the sieve wheel as a rotary drive.