Device and method for filtering a fluid, in particular for plastics processing plants
View Patent ↗The invention relates to a device for filtering a fluid, in particular a liquefied plastic, with a housing with backflush channel and screen carrier and filter element whereby, in order to accelerate and improve the backflush effect, one or more displacement cylinders are provided that guide material removed from the production at adjustable high pressure and speed to the screen to be cleaned from the clean screen side to the dirty screen side, whereby an additional pressure generator ensures constant process pressure.
1. A device for filtering a liquefied plastic, comprising:
a housing;
a supply channel;
a discharge channel;
backflush channels;
two screen carriers slidably supported crosswise to a flow direction;
at least two filter elements each of which are arranged in corresponding screen chambers and linked to the supply channel and the discharge channel;
at least two displacement pistons being inserted in a corresponding partial channel leading from the screen chamber to the discharge channel, the at least two displacement pistons feed a mass free of contaminants out of the corresponding partial channels through the at least two filter elements to a corresponding backflush channel of the backflush channels when at least one of the two screen carriers is in a backflush position; and
a pressure generator arranged in the supply channel, the pressure generator being structured to maintain a constant process pressure at the discharge channel and downstream equipment during a production phase.
2. The device according to claim 1 , wherein the pressure generator is a pump.
3. The device according to claim 1 , wherein the screen carriers are displacable such that the at least two filter elements can be removed from the screen chambers.
4. The device according to claim 1 , further comprising connection plates attached to the housing and accommodating the screen carriers.
5. The device according to claim 1 , wherein at least one of the displacement pistons are activated hydraulically.
6. The device according to claim 1 , wherein at least one of the displacement pistons is activated mechanically.
7. The device according to claim 1 , further comprising a flow divider arranged in the supply channel in front of the screen chambers.
8. The device according to claim 1 , further comprising a flow diverter arranged in the discharge channel.
9. The device according to claim 1 , wherein the operating pressure for the displacement pistons is adjustable.
10. The device according to claim 1 , wherein at least one of the two displacement pistons is structured to load a clean screen side with purified plastic melt when a respective of the two screen carriers is in the backflush position.
11. The device according to claim 1 , wherein the pressure generator is arranged so that the constant process pressure at the discharge channel is maintained when the at least one of the at least two filter screen carriers is in the backflush position and while the filter element associated with the at least one filter screen carrier is backflushed.
12. A device for filtering a liquefied plastic, comprising:
a housing accommodating a screen carrier, a supply channel and a discharge channel;
backflush channels provided in the housing which remain open, without valves, to the atmosphere;
partial channels arranged between the supply channel and the discharge channel;
displacement pistons arranged in the respective partial channels; and
a pressure generator arranged in the supply channel, the pressure generator being structured to maintain a constant process pressure at the discharge channel and downstream equipment during a production phase.
13. The device according to claim 12 , further comprising a mechanical tappet device structured to activate the displacement pistons.
14. The device according to claim 12 , further comprising a connection plate connecting to a side of the screen carrier facing downstream.
15. The device according to claim 12 , wherein the pressure generator is a pump.
16. The device according to claim 12 , wherein the pressure generator is structured such that regardless of a backflush a process pressure in an area of the discharge channel always is kept constant.
17. The device according to claim 12 , further comprising filter elements structured and arranged as screens in screen chambers in the screen carrier.
18. The device according to claim 12 , further comprising a flow divider in the supply channel.
19. The device according to claim 12 , wherein an end face of the displacement pistons is always flowed around by material so that no dead zones occur in which the material can decompose.
20. The device according to claim 12 , wherein one of the displacement pistons is in a position in which a screen in the screen carrier produces a connection between the supply channel and the discharge channel.
21. The device according to claim 12 , wherein the screen carrier is structured to carry at least two filters, and the pressure generator is arranged so that the constant process pressure at the discharge channel is maintained when a backflush flows through one of the two filters.
22. A method for backflushing a liquefied plastic, comprising:
loading a clean screen side of a filter element with purified plastic melt after a screen carrier is slidably moved cross-wise to a displacement direction of the piston into a backflush position by plunging a displacement piston into a partial channel leading from a supply channel to a discharge channel when the screen carrier is in the backflush position and forcing the plastic melt out of the partial channel through the filter element in the backflush position, whereby the filter element is acted on with a pressure that is higher than an operating pressure prevailing on a production side of the filter element and a backflush portion is guided through a backflush channel that remains open to the atmosphere without a valve; and
maintaining a constant melt pressure at the discharge channel via a pressure generator arranged in the supply channel.
23. The method according to claim 22 , wherein the backflush pressure is adjustable.
24. The method according to claim 22 , further comprising controlling the melt pressure depending on a pressure value measured at the discharge channel.
25. The method according to claim 22 , wherein the maintaining the constant melt pressure is achieved through a pressure generator arranged in the supply channel so that the constant melt pressure at the discharge channel is maintained while the filter element is acted on with a pressure that is higher than the operating pressure prevailing on the production side of the filter element.