SCREENING APPARATUS FOR REMOVING SOLID MATERIAL FROM FLOWING LIQUID AND ASSOCIATED SCREENING PANEL
20220331722 · 2022-10-20
Inventors
Cpc classification
B01D33/067
PERFORMING OPERATIONS; TRANSPORTING
B01D2201/184
PERFORMING OPERATIONS; TRANSPORTING
B01D33/333
PERFORMING OPERATIONS; TRANSPORTING
B01D33/06
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01D33/067
PERFORMING OPERATIONS; TRANSPORTING
B01D33/11
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A screening panel for an apparatus for removing solid material from a flowing liquid, where the screening panel is mountable to a conveyor of the apparatus for travel around an endless path passing into and out of the flowing liquid. The screening panel is molded from a polymeric material and provided with a plurality of apertures each extending through the screening panel from a first major surface to an opposing second major surface. The apertures each have a tapered hexagonal cross-section.
Claims
1. A screening apparatus for removing solid material from a flowing liquid, comprising: a plurality of screening panels; a conveyor, the screening panels being mounted to the conveyor for travel around an endless path passing into and out of the flowing liquid; each of the screening panels having a first major surface and a second major surface in parallel relation to one another, each of the screening panels being mounted to the conveyor so that the first major surface faces the flowing liquid, and the second major surface faces in a direction of flow of the flowing liquid, and each screening panel being molded from a polymeric material and being provided with a plurality of apertures; and the apertures each extending through each panel from the first major surface to the second major surface to thereby permit liquid flow through the apertures, the apertures each having a hexagonal cross-section in at least one of the first major surface and the second major surface, each of the apertures having a first maximum transverse dimension at the first major surface with a transverse dimension increasing progressively from the first major surface towards the second major surface, each of the apertures having a second maximum transverse dimension greater than the first maximum transverse dimension at the second major surface of the respective screening panel.
2. The apparatus defined in claim 1 wherein the screening panels each have a thickness of approximately 9 mm and wherein the apertures have a taper of 0.3 to 0.5 mm from the second major surface to the first major surface.
3. The apparatus defined in claim 1 wherein each of the apertures has a first maximum transverse dimension of 3.3 mm, vertex to opposing vertex, at the second major surface and a second maximum transverse dimension of 3 mm, vertex to opposing vertex, at the first major surface.
4. The apparatus defined in claim 1 wherein the apertures are equispaced from each neighboring one of the apertures.
5. The apparatus defined in claim 1 wherein the apertures form a honeycomb grid or pattern, each of the apertures internal to the grip or pattern having six angularly equispaced neighbor apertures.
6. The apparatus defined in claim 1 wherein each of the screening panels provides an increase in aggregate flow-through area of 9-16% over a screening panel of equal size having conical or cross-sectionally circular apertures.
7. The apparatus defined in claim 1 wherein the apertures have a hexagonal cross-section along their entire lengths from the first major surface to the second major surface.
8. A screening panel for an apparatus for removing solid material from a flowing liquid, where the screening panel is mountable to a conveyor for travel around an endless path passing into and out of the flowing liquid, the screening panel comprising: a first major surface and a second major surface in parallel relation to one another, said screening panel being molded from a polymeric material and provided with a plurality of apertures, the apertures each extending through said screening panel from the first major surface to the second major surface to thereby permit liquid flow through the apertures, the apertures each having a hexagonal cross-section in at least one of the first major surface and the second major surface, each of the apertures having a first maximum transverse dimension at the first major surface with a transverse dimension increasing progressively from the first major surface towards the second major surface, each of the apertures having a second maximum transverse dimension greater than the first maximum transverse dimension at the second major surface.
9. The screening panel defined in claim 8 wherein said first major surface and said second major surface are spaced by a panel thickness of approximately 9 mm and wherein the apertures have a taper of 0.3 to 0.5 mm from the second major surface to the first major surface.
10. The screening panel defined in claim 8 wherein each of the apertures has a first maximum transverse dimension of 3.3 mm, vertex to opposing vertex, at the second major surface and a second maximum transverse dimension of 3 mm, vertex to opposing vertex, at the first major surface.
11. The screening panel defined in claim 8 wherein the apertures are equispaced from each neighboring one of the apertures.
12. The screening panel defined in claim 8 wherein the apertures form a honeycomb grid or pattern, each of the apertures internal to the grip or pattern having six angularly equispaced neighbor apertures.
13. The screening panel defined in claim 8 wherein said screening panel provides an increase in aggregate flow-through area of 9-16% over a screening panel of equal size having conical or cross-sectionally circular apertures.
14. The screening panel defined in claim 8 wherein the apertures have a hexagonal cross-section along their entire lengths from the first major surface to the second major surface.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0018]
[0019]
[0020]
[0021]
[0022]
[0023]
DETAILED DESCRIPTION
[0024] As depicted in
[0025] The molded apertures 12 occupy 54-58% or more of the total area of each panel 10 and are of hexagonal cross-section. Apertures 12 have a diameter D.sub.1 of about 3 mm in an upstream major surface 13 of panel 10 and, as may be seen in
[0026] Screening panels 10 are mounted as a single row about a periphery 16 of a 5 m diameter rotary conveyor or drum 16′ of screen apparatus 15, so that longer edges 17 of the screening panels 10 extend around a circumference of the conveyor or drum. In some cases, two or more such rows of panels may be preferred. As indicated by arrows 21, 22 in
[0027] Rims 18 of rotary conveyor or drum 16′ are finely sealed against the passage of debris, thereby permitting finer screening. The tapered configuration of apertures or through-holes 12 alleviates clogging. Moreover, the longitudinally continuous hexagonal transverse cross-section of apertures 12 strengthens the screening panels 10, creating a web of stress lines therein and facilitating a maximization of flow throughput per unit area of the screening panels. The tapered configuration of apertures 12 is, of course, particularly suited for use with rotary screen apparatus 16 where the liquid to be screened flows through the screening panels 10 in only one direction. A further advantage of the tapered hole construction is that it facilitates the removal of the panel from the mould.
[0028]
[0029] Panel 110 is molded from polypropylene and comprises a rectangular screening face 111 provided with a plurality of hexagonal apertures 112 therein, and two solid edge faces flanges 113 extending perpendicularly away from longer edges 114 of screening face 111, respectively. Panel 110 has a length of about 80 cm, a width of about 20 cm, and a thickness of 9 mm, the edge faces or flanges 113 each having a width of about 12 to 24 mm.
[0030] Apertures or through-holes 112 in screening face 111 are formed during the molding process. Each aperture 112 has a hexagonal cross-section that tapers down continuously from a trailing or downstream side of panel 110 to an upstream or leading side thereof. Apertures or through-holes 112 have dimensions as discussed above with reference to
[0031] As shown in
[0032] During operation of band screen apparatus 115, on an upgoing side 116 of the panel belt, the leading edge faces 113 of panels 110 are caused to move outwardly to form rising steps 117 that lift debris out of the flow. At the top of the screen, those edge faces 113 move inwardly again, causing the debris to be knocked off the panels. The panels 110 are then caused to flatten to form a smooth surface 118, whereupon the panels are brushed and backwashed to remove finer screenings. The panels 110 then move downwardly and re-enter the flow 119 in the reverse orientation.
[0033] Screening panels as disclosed herein, with particular reference to panels 10 and 110, are utilizable with other types of screening apparatus such as Ovivo's center-flow Brackett Green® CF200 and CF100 Band Screens (CF standing for Center Flow). In the center flow pattern of the CF200 Band Screen, liquid enters the center of the screening apparatus and flows radially outwardly through a band of polymer mesh panels moving along an endless path in a screen head section of the apparatus. Screened or filtered material is retained on an inner side of the mesh panel band and discharged by low-pressure water jets at deck level during a cleaning cycle. Water jets are mounted on a jet pipe inside the screen head section. During the cleaning cycle, these jets continuously spray the panels as they pass a discharge station above a debris hopper.
[0034] As depicted in the drawings and described above, a screening apparatus 16 or 115 for removing solid material from a flowing liquid, exemplarily useful in wastewater treatment facilities, includes a plurality of screening panels 10 or 110, and a conveyor 16′ or 115′, the screening panels being mounted to the conveyor for travel around an endless path passing into and out of the flowing liquid. Each of the screening panels has an upstream-facing major surface 13 and a downstream-facing major surface 14 in parallel relation to one another. Each of the screening panels 10 or 110 is mounted to the respective conveyor 16′ or 115′ so that upstream major surface 13 faces the flowing liquid, with downstream major surface 14 facing in a direction of flow of the flowing liquid. Each screening panel 16′ and 115′ is molded from a polymeric material and is provided with a plurality of apertures. Apertures 12 and 112 each extend through a respective panel 10, 110 from upstream major surface 13 to downstream major surface 14 to thereby permit liquid flow through the apertures. Apertures 12 and 112 each have a hexagonal cross-section in at least one of the major surfaces 13 and 14 and preferably through the lengths of the apertures. Each aperture 12, 112 has a first maximum transverse dimension at the upstream major surface 13, the transverse dimension (e.g. width) of the apertures 12, 112 increasing progressively from the upstream major surface 13 towards the downstream major surface and having a second maximum transverse dimension at the downstream major surface 14 greater than the first maximum transverse dimension at the upstream surface of the respective screening panel 10, 110.
[0035] In a particular embodiment, screening panels 10, 110 each have a thickness of approximately 9 mm and the apertures have a decreasing taper of 0.3 to 0.5 mm from the downstream major surface 14 depending on aperture size to the upstream major surface 15, while the apertures in this example each have a first maximum transverse dimension of 3 mm, vertex V.sub.1 to opposing vertex V.sub.2, at the downstream major surface 14 and a second maximum transverse dimension of 3 mm, vertex v1 to opposing vertex v2, at the upstream major surface 13.
[0036] Preferably, apertures 12, 112 are equispaced from each neighboring or adjacent aperture. The apertures 12, 112 form a honeycomb grid or pattern (see
[0037] Each screening 12, 112 panel provides an increase in aggregate flow-through area of 9-16% over a screening panel of equal size having conical or cross-sectionally circular apertures.
[0038] Apertures 12, 112 have a hexagonal cross-section along their entire lengths between upstream major surface 13 and downstream major surface 14. As shown in
[0039] Although the invention has been described in terms of particular embodiments and applications, one of ordinary skill in the art, in light of this teaching, can generate additional embodiments and modifications without departing from the spirit of or exceeding the scope of the claimed invention. Accordingly, it is to be understood that the drawings and descriptions herein are proffered by way of example to facilitate comprehension of the invention and should not be construed to limit the scope thereof.