KR19990075886A - Downflow fluidized bed yarn filter - Google Patents

Abstract

The downflow fluidized bed sand filter of the present invention is composed of a housing, a filtration layer, a supply chamber, a washing chamber, a filtration chamber, a filtration nozzle, and a suction pipe. The filter layer is composed of a first filter medium and a second filter medium having a larger particle diameter than the first filter medium. The first filter medium circulates inside the housing, and serves to discharge impurities to the outside. This first filter medium is transferred to the cleaning chamber through the suction pipe together with the impurities. The first filter medium moved to the cleaning chamber is separated from the impurities, washed, and moved back to the filter bed by gravity. The supply chamber is connected with a first port for supplying liquid from the outside. A second port is connected to the filtration chamber for discharging the filtered liquid to the outside. The filtration nozzle is formed to be located along the periphery of the bottom of the filtration layer, and is located between the bottom of the filtration layer and the filtration chamber, allowing the liquid filtered in the filtration layer to enter the wash chamber. The suction tube connects the lower surface of the filtration layer and the cleaning chamber to allow the liquid to flow to convey the first filter medium.

Description

DOWNFLOW SAND FILTER WITH CONTINUOUS BACKWASHING

The present invention relates to a downflow fluidized bed yarn filter.

Many filters and methods have been proposed or realized for limiting the filtration of suspended and colloidal solids from wastewater. Such filters and methods are described in USP NO. As shown in 4,126,546 and 4,197,201, the liquid is filtered by flowing the liquid through a layer of fine filter media such as sand.

USP NO. By Stevens. The filter described in 5,454,959 uses filtration nozzles and washboxes. Moreover, the filtration layer which consists of a thin sand and a coarse sand filter medium is used. There is a liquid inlet at the top of the filter and an outlet of the filtered liquid at the bottom. The lower part of the filter has a manifold connected to the outlet. The liquid supplied through the inlet is configured to be received by the manifold through the filtration layer. At this time, the liquid filtered while passing through the filter medium is introduced into the manifold through the filtration nozzle. On the other hand, the fine sand from the filter medium constituting the filter layer is introduced into the wash box to be washed. The fine sand is washed in the wash box to separate from suspended solids and / or contaminants such as colloids from the liquid.

However, such a conventional filter takes a long time to obtain a filtered liquid by supplying the liquid, there is a problem that the liquid is introduced into the manifold in the unstable filtered state. In addition, the filter medium was not completely washed in the wash box, causing a problem of contaminants such as suspended matter and / or colloids remaining inside the filter. See, eg, USP NO. In the strainer disclosed in 5,454,959, the filtration nozzle, which allows the filtered liquid to flow into the manifold, is configured in the form of a rod. Thus, several filtration nozzles are installed around the manifold. This filtration nozzle has limitations in receiving the filtered liquid. That is, in order to increase the capacity of a liquid, many filtration nozzles must be provided. In addition, since the filtration nozzle is relatively close to the portion where the liquid flows in, unfiltered liquid may flow in. In addition, the filtration nozzle is a factor that prevents the filter medium from moving to the washbox. On the other hand, the washbox has a structure to be moved to the lower part of the filter again by gravity in the state that the filter medium is simply moved. Thus, contaminants such as suspended solids and / or colloids attached to the filter medium may not be effectively separated.

The present invention solves this conventional problem, the object of which is to filter a large amount of liquid in a relatively short time and to prevent the liquid from being discharged to the outside in an unstable filtered state and from the filter medium To provide a new type of downflow fluidized bed filter that can effectively remove contaminants such as suspended solids and / or colloids.

1 is a cross-sectional view of a downflow fluidized bed yarn filter in accordance with an embodiment of the present invention;

2 is an enlarged view of the filtration nozzle in FIG. 1;

3 is an enlarged view of the cleaning chamber in FIG. 1.

* Explanation of symbols for the main parts of the drawings

10 filter 12 housing

13: 1st filter medium 14: 2nd filter medium

16: filtration layer 18: first port

20: second port 22: supply chamber

24 filtration chamber 26 suction tube

28: baffle 30: washing chamber

32: passage 40: filtration nozzle

42: home opening 50: valve controller

52: valve 54: sensor

56: pollutant discharge port 58: overflow

According to a feature of the present invention for achieving the above object, the downflow fluidized bed yarn filter comprises a housing; A filtration layer located inside the housing and composed of at least one filter material, the filter layer having an upper surface and a lower surface; A first port for supplying a liquid for filtration to the inside of the housing from the outside; A second port for discharging the filtered liquid inside the housing to the outside of the housing; A supply chamber connected with the first port to flow liquid supplied from the first port, the supply chamber having a top surface and a side surface through which liquid does not pass and an open bottom surface located below the filter layer; A cleaning chamber located inside the housing and above the filtration layer, separated from the second port by the filtration layer, for regenerating the first filter material in a flow in a direction opposite to the flow direction of the filtrate Wow; A suction pipe positioned inside the housing for transporting the first filter medium, the suction pipe connecting the lower surface of the filter layer and the cleaning chamber to allow liquid to flow; The inclined surface formed at an angle from a predetermined height of the side surface of the housing to a bottom surface of the housing so as to support the filtering layer in the housing, the liquid filtered in the filtering layer is accommodated, and the contained liquid is discharged to the outside. A filtration chamber connected to the second port; A filtration nozzle which is formed to be located along a circumference of the lower surface of the filtration layer, and is positioned between the lower surface of the filtration layer and the filtration chamber, and allows the liquid filtered in the filtration layer to flow into the cleaning chamber; And a plurality of holes formed on an inclined surface of the filtration chamber in which the filtration nozzle is located, and allowing the liquid passing through the filtration nozzle to flow into the filtration chamber.

The filtration nozzle of the downflow fluidized bed yarn filter according to the present invention is formed in a conical shape having an open top and bottom surfaces, and a plurality of slotted openings are formed so as to be perpendicular to the filtration layer with respect to the installed state. Can be. The cleaning chamber may have a pleated passageway with respect to the direction in which the first filter medium is moved.

Since the downflow fluidized bed sand filter of the present invention can smooth the flow of the filter medium, it is possible to effectively remove impurities to keep the inside of the filter clean. In particular, a pleated passageway in the cleaning chamber allows for effective separation of the filter media and impurities. On the other hand, the filtration nozzle is able to obtain a filtered liquid while reducing the filtration time of the liquid.

Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to FIGS. 1 to 3. In addition, in these drawings, the same reference numerals are denoted together for components that perform the same function.

1 is a cross-sectional view of a downflow fluidized bed yarn filter in accordance with an embodiment of the present invention.

Referring to FIG. 1, the filter 10 includes a housing 12, a filtration layer 16, a first port 18, a second port 20, a supply chamber 22, a filtration chamber 24, and a suction pipe ( 26), the cleaning chamber 30, and the filtration nozzle 40. The filter layer 16 is composed of a first filter medium 13 and a second filter medium 14 having a larger particle diameter than the first filter medium 13. The performance of the filter 10 is often determined by the filter media 13, 14. The filter media 13 and 14 may use sand or the like, in particular, high quality multi-grade silica sand. If the particle diameters of the filter media 13 and 14 are smaller, a better filtering effect can be obtained, but the pressure applied to the filter layer is increased. The first filter medium 13 is located close to the side of the housing 12. The second filter medium 14 is located at the center of the housing 12 surrounded by the first filter medium 13. Various types of materials of the housing 12 may be used. For example, fiberglass reinforced plastic, carbon steel, stainless steel, or the like may be used. The side of the housing 12 is as cylindrical as possible. This is to minimize the corners. This is because the corners cause dead zones in the filtration layer.

Liquid for filtration is supplied through the first port 18. The first port 18 is connected to the supply chamber 22 so that liquid flows. The supply chamber 22 has an upper surface and a side surface through which liquid does not pass and has an open bottom surface. The liquid supplied from the first port 18 is filtered while flowing through the filtration layer 16 through the supply chamber 22. This filtered liquid flows through the filtration nozzle 40 into the filtration chamber 24. The filtration chamber 24 is formed to support the filtration layer 16 in the housing 12. The filtration chamber 24 has an inclined surface formed at a predetermined angle from the predetermined height of the side surface of the housing 12 to the bottom surface of the housing 12. The filtration chamber 24 is connected to the second port 20 so that the liquid filtered in the filtration layer 16 is received and the contained liquid is discharged to the outside. On the other hand, a plurality of holes 25 are formed on the inclined surface of the filtration chamber 24. These holes 25 are formed in the portion where the filtration nozzle 40 is located. These holes 25 allow the liquid passed through the filtration nozzle 40 to enter the filtration chamber 24. The filtration nozzle 40 is formed to be located along the circumference of the lower surface of the filtration layer 16. This filtration nozzle 40 is located between the lower surface of the filtration layer 16 and the filtration chamber 24. As shown in Fig. 2, the filtration nozzle 40 is formed in a conical shape with the top and bottom surfaces open, and a plurality of slotted openings are perpendicular to the filtration layer 16 with respect to the installed state. 42 is formed. The liquid contained in the filtration chamber 24 through the filtration nozzle 40 is filtered out of contaminants such as suspended solids and / or colloids. This liquid is discharged from the housing 12 through the second port 20. The discharge of the liquid is regulated by the control of the valve 52. The valve 52 is alternately controlled by the valve controller 50. For example, the valve controller 50 detects the water level in the housing 12 by the sensor 54, opens and closes the valve 52, and adjusts the water level in the housing 12. The sensor 54 is a level sensor such as an ultrasonic level sensor. The filter 10 is provided with an overflow 58 in order to adjust the internal water level in case of malfunction or failure of the controller 50.

On the other hand, the suction pipe 26 is installed inside the housing 12. The suction pipe 26 is configured to transport the first filter medium 13. The suction pipe 26 connects the lower surface of the filtration layer 16 and the cleaning chamber 30 to allow liquid to flow. The first filter medium 13 is moved to the cleaning chamber 30 through the suction pipe 26. At this time, the first filter medium 13 is moved with contaminants such as suspended matter and / or colloid. In the cleaning chamber 30 the first filter medium 13 is separated from contaminants such as suspended solids and / or colloids. Contaminants such as suspended matter and / or colloids are discharged to the outside through the contaminant outlet 56. The first filter medium 13 is moved to the cleaning chamber 30 through the suction pipe 26 by a gas such as air supplied from the outside. The gas is supplied into the suction pipe 26 through a gas supply line (not shown). The gas supply line is connected to a gas source part (not shown). When the gas is supplied, the first filter medium 13 is moved to the cleaning chamber 30 through the suction pipe 26. As shown in FIG. 3, the first filter medium 13 is separated from the suspended solids and / or contaminants such as colloid in the cleaning chamber 30. This is because the first filter medium 30 is moved to the bottom of the housing 12 by gravity, and contaminants such as suspended matter and / or colloids are lifted up in the cleaning chamber 30. In addition, the first filter medium 30 is formed in the lower portion of the cleaning chamber 30, and passes through the passage (shirred passageway) 32 having a corrugated shape with respect to the direction in which the first filter medium 30 is moved. Done. This passage 32 further enhances the cleaning effect of the first filter medium 30. The first filter medium 30 passing through the passage 32 is moved under the filter layer 16 along the baffle 28 by gravity.

Applying the present invention, it is possible to smooth the flow of the filter medium, it is possible to effectively remove impurities to keep the inside of the filter clean. In particular, a pleated passageway in the cleaning chamber allows for effective separation of the filter media and impurities. On the other hand, the filtration nozzle is able to obtain a filtered liquid while reducing the filtration time of the liquid.

Claims (3)

In a downflow fluidized bed yarn filter, A housing; A filtration layer located inside the housing and composed of at least one filter material, the filter layer having an upper surface and a lower surface; A first port for supplying a liquid for filtration to the inside of the housing from the outside; A second port for discharging the filtered liquid inside the housing to the outside of the housing; A supply chamber connected with the first port to flow liquid supplied from the first port, the supply chamber having a top surface and a side surface through which liquid does not pass and an open bottom surface located below the filter layer; A cleaning chamber located inside the housing and above the filtration layer and separated from the second port by the filtration layer and for regenerating the filter medium in a flow in a direction opposite to the flow direction of the filtrate; A suction pipe positioned inside the housing for transporting the filter medium and connecting the lower surface of the filter layer and the cleaning chamber to allow liquid to flow; The inclined surface formed at an angle from a predetermined height of the side surface of the housing to a bottom surface of the housing so as to support the filtering layer in the housing, the liquid filtered in the filtering layer is accommodated, and the contained liquid is discharged to the outside. A filtration chamber connected to the second port; A filtration nozzle which is formed to be located along a circumference of the lower surface of the filtration layer, and is positioned between the lower surface of the filtration layer and the filtration chamber, and allows the liquid filtered in the filtration layer to flow into the cleaning chamber; And a plurality of holes formed on the inclined surface of the filtration chamber in which the filtration nozzle is located, and allowing the liquid passing through the filtration nozzle to enter the filtration chamber. The method of claim 1, The filtration nozzle is formed in a conical shape of the upper surface and the lower surface, the downflow fluidized bed yarn filter characterized in that a plurality of grooved opening (slotted opening) is formed to be perpendicular to the filter layer with respect to the installed state. The method of claim 1, And said washing chamber has a shredred passageway with respect to the direction in which said filter medium is moved.