Patent Application
20190388809
The present disclosure relates generally to rotary drum washers used to dewater sludge or other suspensions in any industry and more particularly to recausticizing drums used in the chemical recovery processes in the pulp and paper industry, specifically for the recovery of lime mud or dregs.
It is possible to produce pulp on an industrial scale in several ways. Producers tend to classify these methods into one of three general categories: chemical pulping, mechanical pulping, and hybrid pulping. Hybrid pulping involves different aspects of both chemical and mechanical pulping. Briefly, mechanical pulping often involves feeding lignocellulosic material (e.g. wood chips, bagasse, corn stover, recycled paper, or other material comprising the protein lignin and cellulosic polymers) through a series of mechanical refiners. Successive refining grinds the lignocellulosic material to the desired pulp grade. Mill operators may further process this pulp into a number of pulp-based products (e.g. paper, packaging material, absorbent filler, etc.); or the mill operators may sell the pulp wholesale.
In chemical processes, mill operators treat lignocellulosic material with either strong acids or strong bases to disassociate the lignin from the cellulosic fibers. Operators may then separate, wash, and further process the cellulosic fibers into pulp or other pulp-based products. Chemical process examples include: the Kraft process (also known as the “sulfate process”), sulfite process, soda pulping process, and the sulfite semi-chemical pulping process.
While the processing chemicals for each type of chemical process may vary, mill operators frequently recover and recycle these process chemicals to operate the mill economically. In the Kraft process for example, mill operators cook the lignocellulosic material with “white liquor” in large pressurized digesters. The white liquor comprises sodium hydroxide, NaOH, and sodium sulfide, Na2S. After cooking, a slurry of spent chemical liquor and rough pulp, exits the digester. The spent chemical liquor is commonly known as “black liquor” and comprises organic and inorganic compounds left over from the cooking process.
While downstream pulping equipment continues to process the rough pulp, the chemical recovery process begins with isolating, concentrating, and then transferring the black liquor into a chemical recovery boiler. The chemical recovery boiler evaporates excess moisture and the inorganic compounds in the black liquor undergo pyrolysis. These inorganic compounds accumulate as molten salts (“smelt”) at the bottom of the recovery boiler and eventually flow into an adjacent dissolving tank. The dissolving tank typically contains “weak wash” comprising the liquors used to wash lime mud and other precipitates. Upon contacting the weak wash, the smelt reacts and mixes with the weak wash to become “green liquor.” The green liquor contains the first component of white liquor: sodium sulfide, Na2S, and the byproduct sodium carbonate, Na2CO3.
Operators then clarify and feed the green liquor into an agitator and add calcium oxide, CaO, and water. Calcium oxide is commonly known as “quicklime.” The quicklime exothermically reacts with the water to produce calcium hydroxide, Ca(OH)2. The calcium hydroxide then reacts with the sodium carbonate in the green liquor to produce the other component of white liquor: sodium hydroxide, NaOH, and the byproduct calcium carbonate, CaCO3. Calcium carbonate is commonly known as “lime mud.”
At this stage, the lime mud precipitates out of the white liquor solution. Operators then clarify and transfer the white liquor to a storage tank to await reuse in the Kraft process. Meanwhile, operators wash, filter, and transfer the lime mud to a lime kiln for conversion back into quicklime (calcium oxide, CaO). With the recycled quicklime, the mill operators may continue to treat green liquor and recover white liquor cost effectively.
To wash and filter the lime mud prior to feeding the lime mud into the lime kiln, operators may process the lime mud on a rotary drum filter. These filters typically consist of a cylindrical drum that is partially submerged in a vat of lime mud. A fabric, plastic, or metal mesh covers the outer surface of the drum and serves as a filter medium. The drum rotates around a center drainage channel that connects to a vacuum system at one end of the drum. Air flowing through the drop leg creates a vacuum. Conduits connect drainage holes in the drum to the center drainage channel. The vacuum allows lime mud to accumulate on a submerged sector of the drum. As the drum sector rotates out of the vat, filtrate flows through the filter medium, drainage holes, conduits, center drainage channel, and vacuum system. Before the sector rotates back down into the vat, a doctor blade shears off the dewatered lime mud. Operators then collect this dewatered lime mud and may store it before feeding it into a lime kiln.
The rate at which filtrate exits the sector can be limited by the rate of rotation and the number of drainage holes in each sector. With current rotary drum filter designs, there is a point at which increasing the rate of rotation will not further increase filtration. To compensate, one might think to add more drainage holes, but adding more drainage holes presents its own problems. Adding too many drainage holes reduces the pressure differential between the drum and lime mud, thereby decreasing the drum's ability to develop an initial mud layer. This initial mud layer acts as a primary filter medium and allows additional mud to accumulate on top of the initial layer. Furthermore, existing rotary filter drums may have structural components at locations desirable for an additional drainage hole. Increasing the number of drainage holes may also weaken the structural integrity of the rotary filter drum. Accordingly, there is a long felt and unresolved need to increase the rate of filtration without weakening the structural integrity of the rotary filter drum.
The problem of unrealized production in rotary filter drums due to undirected filtrate flow through the sectors is mitigated by a rotary drum filter comprising: a drum shell having areas defining a plurality of drainage holes, and a divider plate disposed on an outer surface of the drum shell and extending longitudinally and laterally along the drum shell, wherein the divider plate has a first end and a second end, and wherein the first end is disposed near a drainage hole and is thereby configured to direct a filtrate into the drainage hole.
An exemplary rotary drum filter may further comprise grid holders having multiple slots disposed along the length of the grid holders, wherein the grid holders extend longitudinally on an outer surface of a drum shell at arcuate intervals to define multiple arcuate drainage sectors. Divider plates may be disposed between the drainage sectors.
In still other exemplary embodiments, a divider plate may extend from one or more grids disposed around the drum shell.
In another exemplary embodiment, the problem of unrealized production in rotary filter drums due to undirected filtrate flow through the sectors is mitigated by a rotary drum filter comprising: a drum shell having areas defining a plurality of drainage holes, grid holders having multiple slots disposed along the length of the grid holders, wherein the grid holders extend longitudinally on an outer surface of a drum shell at arcuate intervals to define multiple arcuate drainage sectors including a first arcuate drainage sector and a second arcuate drainage sector disposed adjacent to the first arcuate drainage sector, wherein each of the arcuate drainage sectors have a first longitudinal end distally disposed from a second longitudinal end, wherein the first arcuate drainage sector and the second arcuate drainage sector have drainage holes disposed at a first lateral end and at a second lateral end distally disposed from the first lateral end, and divider plates disposed on the outer surface of the drum shell, the divider plates extending longitudinally and laterally within the first arcuate drainage sector and the second arcuate drainage sector, wherein an end of the drainage plate is disposed toward a grid holder, the grid holder being disposed between the first arcuate drainage sector and the second arcuate drainage sector.
An advantage of exemplary embodiments of the present disclosure is that suppliers may retrofit existing rotary filter drums with exemplary slotted grid holders and divider plates.
The foregoing will be apparent from the following more particular description of exemplary embodiments of the disclosure, as illustrated in the accompanying drawings. The drawings are not necessarily to scale, with emphasis instead being placed upon illustrating the disclosed embodiments.
The following detailed description of the preferred embodiments is presented only for illustrative and descriptive purposes and is not intended to be exhaustive or to limit the scope and spirit of the invention. The embodiments were selected and described to best explain the principles of the invention and its practical application. One of ordinary skill in the art will recognize that many variations can be made to the invention disclosed in this specification without departing from the scope and spirit of the invention.
Similar reference characters (e.g. 140, 240, 340, 440) indicate corresponding parts throughout the several views unless otherwise stated. Although the drawings represent embodiments of various features and components according to the present disclosure, the drawings are not necessarily to scale and certain features may be exaggerated in order to better illustrate embodiments of the present disclosure, and such exemplifications are not to be construed as limiting the scope of the present disclosure.
Except as otherwise expressly stated herein, the following rules of interpretation apply to this specification: (a) all words used herein shall be construed to be of such gender or number (singular or plural) as to circumstances require; (b) the singular terms “a,” “an,” and “the,” as used in the specification and the appended claims include plural references unless the context clearly dictates otherwise; (c) the antecedent term “about” applied to a recited range or value denotes an approximation within the deviation in the range or values known or expected in the art from the measurements; (d) the words “herein,” “hereby,” “hereto,” “hereinbefore,” and “hereinafter,” and words of similar import, refer to this specification in its entirety and not to any particular paragraph, claim, or other subdivision, unless otherwise specified; (e) descriptive headings are for convenience only and shall not control or affect the meaning or construction of any part of the specification; and (f) “or” and “any” are not exclusive and “include” and “including” are not limiting. Further, the terms, “comprising,” “having,” “including,” and “containing” are to be construed as open-ended terms (i.e., meaning “including but not limited to”).
References in the specification to “one embodiment,” “an embodiment,” “an exemplary embodiment,” etc., indicate that the embodiment described may include a particular feature, structure, or characteristic, but every embodiment may not necessarily include the particular feature, structure, or characteristic. Moreover, such phrases are not necessarily referring to the same embodiment. Further, when a particular feature, structure, or characteristic is described in connection with an embodiment, it is submitted that it is within the knowledge of one skilled in the art to affect such feature, structure, or characteristic in connection with other embodiments whether or not explicitly described.
To the extent necessary to provide descriptive support, the subject matter and/or text of the appended claims is incorporated herein by reference in their entirety.
Recitation of ranges of values herein are merely intended to serve as a shorthand method of referring individually to each separate value falling within the range of within any sub ranges there between, unless otherwise clearly indicated herein. Each separate value within a recited range is incorporated into the specification or claims as if each separate value were individually recited herein. Where a specific range of values is provided, it is understood that each intervening value, to the tenth or less of the unit of the lower limit between the upper and lower limit of that range and any other stated or intervening value in that stated range or sub range hereof, is included herein unless the context clearly dictates otherwise. All subranges are also included. The upper and lower limits of these smaller ranges are also included therein, subject to any specifically and expressly excluded limit in the stated range.
It should be noted that some of the terms used herein are relative terms. For example, the terms “upper” and “lower” are relative to each other in location, i.e. an upper component is located at a higher elevation than a lower component in a given orientation, but these terms can change if the device is flipped. The terms “inlet” and “outlet” are relative to a fluid flowing through them with respect to a given structure, e.g. a fluid flows through the inlet into the structure and flows through the outlet out of the structure. The terms “upstream” and “downstream” are relative to the direction in which a fluid flows through various components, i.e. the flow of fluids through an upstream component prior to flowing through the downstream component.
The terms “horizontal” and “vertical” are used to indicate direction relative to an absolute reference, i.e. ground level. However, these terms should not be construed to require structure to be absolutely parallel or absolutely perpendicular to each other. For example, a first vertical structure and a second vertical structure are not necessarily parallel to each other. The terms “top” and “bottom” or “base” are used to refer to locations/surfaces where the top is always higher than the bottom/base relative to an absolute reference, i.e. the surface of the Earth. The terms “upwards” and “downwards” are also relative to an absolute reference; an upwards flow is always against the gravity of the Earth.
Rotary drum filters 100 are used in several industries and for several applications. For example, in the pulp and paper industry, rotary drum filers can be used to filter lime mud, in brown stock washing, and in pulp bleaching. Rotary drum filters 100 are also used in other industries that require large-scale separation of solids from liquids, for example in the mining industry.
In the depicted embodiment, grid holders 120 extend longitudinally on an outer surface 112 of the drum shell 110 and are disposed at arcuate intervals 123 to define multiple arcuate drainage sectors 125. The grid holders 120 may be welded or otherwise affixed to the outer surface 112 of the drum shell 110. In the depicted exemplary embodiment, each grid holder 120 has a number of slots 127 disposed along a length L of each grid holder 120. In other exemplary embodiments, the grid holders 120 may be disposed slightly above the outer surface 112 of the drum shell 110 to permit filtrate 130 to flow underneath the grid holder 120. In such embodiments where the grid holder 120 is disposed above the drum 110, the grid holders may lack the slots 127.
Grid segments 126 are disposed between two adjacent grid holders 120 and over a divider plate 140. A filter medium 128, which may be a fabric, plastic, or wire mesh screen, is disposed over the grid segments 126 around the rotary drum filter 100.
A divider plate 140 is disposed on the outer surface 112 of the drum shell 110 and extends longitudinally and laterally within the arcuate drainage sector 125. The divider plate 140 may cut from a flat sheet of plate and then rolled and formed to conform to the curve of the outer drum surface 112. The divider plate 140 comprises a first end 141 and a second end 143. In the depicted embodiment, both the first end 141 and the second end 143 are disposed near separate drainage holes 115. The divider plate 140 is disposed at an angle θ relative to the adjacent grid holder 120a. In other exemplary embodiments, a divider plate 140 may extend along two or more adjacent drainage sectors 125.
As
On the second drainage sector 225y, the first end 241ay of a first divider plate 240ay is disposed closer to the second drainage sector's second lateral end 238y and first longitudinal end 232y. Compared to the divider plate's first end 241ay, the second end 243ay of the first divider plate 240ay is disposed closer to the second drainage sector's first lateral end 236y and the second longitudinal end 234y. In this manner, as the eye moves left to right, the first divider plates 240az, 240by appear to converge toward a middle grid holder 220z disposed between the first drainage sector 225z and the second drainage sector 225y and may be described as “converging divider plates.”
In the depicted embodiment, the first end 241bz of a second divider plate 240bz in the first drainage sector 225z is disposed closer to the first drainage sector's second lateral end 238z and first longitudinal end 232z. Compared to the second divider plate's first end 241bz, the second end 243bz of the second divider plate 240bz is disposed closer to the first drainage sector's first lateral end 236z and second longitudinal end 234z.
The first end 241by of a second divider plate 240bz in the second drainage sector 225y is disposed closer to the second drainage sector's first lateral end 236y and first longitudinal end 232y. Compared to the second divider plate in the second drainage sector's first end 241by, the second end 243by of the second divider plate 240by is disposed closer to the second drainage sector's second lateral end 238y and second longitudinal end 234y. In this manner, as the eye moves left to right, the second divider plates 240bz, 240by appear to diverge away from a middle grid holder 220z disposed between the first drainage sector 225z and the second drainage sector 225y and may be described as “diverging divider plates.”
It will be understood that a particular drainage sector 225 may have both converging and diverging divider plates and that “convergence” and “divergence” will change depending upon which grid holder 220 serves as the middle grid holder 220z for a particular set of adjacent drainage sectors (see 225, 225z, 225y). In the depicted embodiment, the drum shell 210 defines a drainage hole 215 near each end of the divider plates 240.
In the depicted embodiment, the converging and diverging divider plates 240 create a hexagonal shape 255 between adjacent drainage sectors 225, 225z. It will be understood that in other exemplary embodiments, the converging and diverging divider plates 240 among adjacent drainage sectors 225 may create shapes that are generally ovoid, circular, rhombic, oblong, octagonal, or other polygonal shape configured to direct filtrate 230 to a drainage hole 215 oriented closer to the nadir N of rotation. As such, although the straight diagonally oriented divider plates 240 are considered to be the most useful embodiment, it will be understood that this disclosure also covers divider plates 440 that are generally concave, convex, curved, segmented, and comprised of smaller straight elements, but generally curved overall.
It will be further understood that the configuration of drainage holes 215 shown in
The exemplary rotary drum filter 300 comprises drainage sectors 325 and divider plates 340 as discussed with reference to
On the second drainage sector 325y, the first end 341cy of a third divider plate 340cy is disposed closer to the second drainage sector's second lateral end 338y and first longitudinal end 332y compared to the third divider plate's second end 343cy. Likewise, compared to the third divider plate of the second drainage sector's first end 341cy, the second end 343cy of the third divider plate 340cy is disposed closer to the second drainage sector's first lateral end 336y and the second longitudinal end 334y. As in
After a point on a given drainage sector 325 passes the apex A of rotation, the second section 353 of the hexagonal shape 355 will be oriented closer to the nadir N of rotation than the first section 356. Upon passing the nadir N, the first section 356 will again be disposed closer to the nadir N than the second section 353, thereby starting a new cycle. It will be understood that whichever of the first or second sections 356, 353 is disposed closer to the nadir N at any given point of rotation will be referred to as the “lower section” relative to the other section. Likewise, whichever of the first or second sections 356, 353 is disposed closer to the apex A at any given point of rotation will be referred to as the “upper section” relative to the other section. It will be further understood that in other exemplary embodiments a given grid holder 320 may not bisect the shape formed by the divider plates 325 and that the first section 356 and second section 353 may not be equal in area.
As can be visualized with reference to
After the drainage sector 325 rotates past the apex, the filtrate 330 begins to flow downwardly toward the second lateral end 338 of the drainage sector 325. The second section 353 of the hexagonal shape 355 on the ascent now become closer to the nadir N on the descent. The second section 353 thereby directs the filtrate 330 to drainage holes 315 disposed near the second lateral end 338 of the drainage sector 325. Filtrate 330 may reverse course and flow back through the slots 327 in the grid holder 320 before encountering the second section 353 of the hexagonal shape 355 in a downwardly adjacent drainage sector 325z.
Without being bound by theory, Applicant believes that the combination of divider plates 340 configured to direct filtrate 330 to drainage holes 315 disposed near a lateral end 336, 338 of a drainage sector 325 while further comprising adjacent drainage sectors (see 325z, 325y) that are configured to fluidly communicate with each other (e.g. through slots 327 or the absence of an obstructions between the lateral sides 336, 338 of adjacent drainage sectors (see 325z, 325y)) effectively increases the available drainage area for the filtrate while maintaining the structural integrity of the outer drum assembly. This, and the arrangement of the divider plates 340, can allow operators to effectively increase the drainage capacity of rotary drum filters 300 that are approaching or that are at their maximum effective rotational velocity (i.e. the velocity at which increased rotation will not result in increased filtration). It is contemplated that the divider plates 340 may be fabricated from steel, such as 304 stainless steel, 316 stainless steel, carbon steel, titanium, or other materials having the structural rigidity and durability to support the outer drum assembly while withstanding the caustic nature of the filtrate. For example, in lime mud rotary drum filters, the filtrate may comprise residual sodium hydroxide (NaOH), a highly caustic compound. By way of another example, it is contemplated that manufacturers will typically select titanium divider plates 340 for rotary drum filters used in the pulp bleaching process.
In operation, the rotary drum filter 410 may rotate in direction R. As a drainage sector 425 exits the suspension vat 450, the suspension 445 adheres to the filter medium 428 and rotates toward the apex A of rotation. In the figure, the suspension 445 is depicted at about the 1:00 position to avoid too many intersecting lines, but it will be understood that the suspension begins adhering to the filter medium 428 below the 3:00 position. The references to “1:00” and “3:00” refer to the hours on an analog clock face and are used herein to reference a position on the circle. On the ascent, the vacuum system (see 311) and gravity pull filtrate 430 through the filter medium 428 and into a drainage sector 425. Before the drainage sector 425 rotates back into the vat 450, a doctor blade 466 shears off the “dewatered” solids (see 445) that remain after filtration. When the solids are lime mud, operators may then feed this lime mud to a lime kiln.
In other exemplary embodiments, the divider plates 440 may all be oriented in the same direction such that the filtrate may flow (for example) from left to right and downwardly along the outer surface of the rotary drum filter toward a drainage hole. In certain exemplary embodiments, the angle θ may be 90 degrees. By way of example, the angle θ may have a range between about 25 degrees and 90 degrees.
In other exemplary embodiments, the grid holders 120220, 320, 420 may be omitted. In such embodiments, the grids 126, 226, 326, 426 are configured to engage the divider plates 140, 240, 340, 440. Fasteners secure the grids 126, 226, 326, 426 to the divider plates 140, 240, 340, 440. In other exemplary configurations, the divider plates 140, 240, 340, 440 are an integral part of the grid 126, 226, 326, 426. The grids 126, 226, 326, 426 themselves may be made of any material sufficiently durable to withstand the environment within the vat housing 151 for prolonged periods. However, the grids are typically plastic and are made through an injection molding process. An exemplary grid injection mold will have a negative space capable of being filled with liquid plastic to define a divider plate 126, 226, 326, 426. When an exemplary grid is disposed on the drum shell 110, 210, 310, 410 the divider plate 126, 226, 326, 426 extends from the bottom of the grid 126, 226, 326, 426.
The lack of grid holders 120220, 320, 420 may be advantageous because the lack of grid holders 120220, 320, 420 would obviate the need for slots 127 and thereby increase the area through which filtrate 440 may flow from the second section (353) of the of the hexagonal shape 355 of an ascending section of the drum shell 410 to the first section (356) of the hexagonal shape 355. The orientation of the divider plates 440 further directs the filtrate 440 to the drainage hole 415 disposed at the first lateral section 436 of the sector 425. In this manner, the exemplary embodiments described herein use gravity, open spaces between adjacent drum sectors (see 325z and 325y) and divider plates 126, 226, 326, 426 extending longitudinally and laterally across the drum's outer surface 112 and leading to drainage holes 115, 215, 315, 415 to increase the rate of filtration over conventional rotary drum filters.
An exemplary embodiment rotary drum filter in accordance with this disclosure comprises: a drum shell having areas defining a plurality of drainage holes, a divider plate disposed on an outer surface of the drum shell and extending longitudinally and laterally along the drum shell, wherein the divider plate comprises a first end and a second end, and wherein the first end is disposed near a drainage hole.
Such an exemplary embodiment may further comprise a rotary support structure disposed around a center axis of rotation and a central drainage channel, wherein an end of the central drainage channel fluidly communicates with a vacuum system, drainage conduits fluidly communicating with the drainage holes and the central drainage channel, a grid disposed between two adjacent grid holders and over the divider plate, and a filter medium disposed around the rotary filter drum. In certain exemplary embodiments, the first ends of two or more of the multiple divider plates are adjacently disposed to separate drainage holes.
The exemplary embodiment may further comprise grid holders extending longitudinally on an outer surface of the drum shell and disposed at arcuate intervals to define multiple arcuate drainage sectors disposed around the drum shell, wherein a grid holder of the multiple grid holders comprise multiple slots disposed along a length of the grid holder. In certain exemplary embodiments, the rotary drum filter may further comprise grids disposed around the outer surface of the drum, wherein the divider plate engages a bottom of the grid disposed around the outer surface of the drum. In still other exemplary embodiments, the divider plate extends from a bottom of the grid disposed around the outer surface of the drum.
Another exemplary rotary drum filter comprises: a drum shell having areas defining a plurality of drainage holes, grid holders, wherein the grid holders extend longitudinally on an outer surface of a drum shell at arcuate intervals to define multiple arcuate drainage sectors including: a first drainage sector, and a second drainage sector disposed adjacent to the first drainage sector, wherein each of the drainage sectors have: a first longitudinal end distally disposed from a second longitudinal end, and a first lateral end distally disposed from a second lateral end, wherein the first drainage sector and the second drainage sector have drainage holes disposed near the first lateral end and the second lateral end, and divider plates disposed on the outer surface of the drum shell and extending longitudinally and laterally within the first drainage sector and the second drainage sector, wherein an end of the drainage plates in the first drainage sector and the second drainage sector converges toward a middle grid holder disposed between the first drainage sector and the second drainage sector.
In such an exemplary embodiment, the first drainage sector may further comprise at least two divider plates and the second drainage sector may further comprise at least two divider plates, wherein a second divider plate of the at least two divider plates in each drainage sector is longitudinally distally disposed from a first divider plate in each drainage sector, wherein a first end of the first divider plate in the first drainage sector is disposed closer to the first lateral end and the first longitudinal end of the first drainage sector and a second end of the first divider plate in the first drainage sector is disposed closer to the second lateral end and the second longitudinal end of the first drainage sector, wherein a first end of the first divider plate in the second drainage sector is disposed closer to the second lateral end and the first longitudinal end of the second drainage sector and a second end of the first divider plate in the second drainage sector is disposed closer to the first lateral end and the second longitudinal end of the second drainage sector, whereby the first divider plates in the first drainage sector and the second drainage sector define converging divider plates, wherein a first end of the second divider plate in the first drainage sector is disposed closer to the second lateral end and the first longitudinal end of the first drainage sector and a second end of the second divider plate in the first drainage sector is disposed closer to the first lateral end and the second longitudinal end of the first drainage sector, wherein a first end of the second divider plate in the second drainage sector is disposed closer to the first lateral end and the first longitudinal end of the second drainage sector and a second end of the second divider plate in the second drainage sector is disposed closer to the second lateral end and the second longitudinal end of the second drainage sector, whereby the second divider plates in the first drainage sector and the second drainage sector define diverging divider plates.
Such an exemplary rotary drum filter may further comprise at least three divider plates in each of the first drainage sector and the second drainage sector, wherein a third divider plate of the at least three divider plates in each drainage sector is longitudinally distally disposed from the first divider plate and the second divider plate in each drainage sector, wherein a first end of the third divider plate in the first drainage sector is disposed closer to the first lateral end and the first longitudinal end of the first drainage sector and a second end of the third divider plate in the first drainage sector is disposed closer to the second lateral end and the second longitudinal end of the first drainage sector, wherein a first end of the third divider plate in the second drainage sector is disposed closer to the second lateral end and the first longitudinal end of the second drainage sector and a second end of the third divider plate in the second drainage sector is disposed closer to the first lateral end and the second longitudinal end of the second drainage sector, whereby the third divider plates in the first drainage sector and the second drainage sector define converging divider plates.
Yet another exemplary rotary filter drum comprises: a drum shell having areas defining a plurality of drainage holes, divider plates disposed on an outer surface of the drum shell and extending longitudinally and laterally along the drum shell along an upper section of an ascending drainage sector of the drum shell to a lower section of the ascending drainage sector of the drum shell, wherein the divider plate comprises a first end and a second end, and wherein the first end is disposed near a drainage hole and the second end is disposed near a drainage hole.
While the invention has been described in connection with what is presently considered the most practical and preferred embodiment, it is to be understood that the invention is not to be limited to the disclosed embodiment, but on the contrary, is intended to cover various modifications and equivalent arrangements included within the spirit and scope of the invention.
This application claims the benefit under 35 U.S.C. § 119 (e) of the earlier filing date of U.S. Provisional Patent Application No. 62/687,381 filed on Jun. 20, 2018, the entirety of which are incorporated herein by reference.
| Number | Date | Country | |
|---|---|---|---|
| 62687381 | Jun 2018 | US |
