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Publication numberUS2311813 A
Publication typeGrant
Publication dateFeb 23, 1943
Filing dateAug 2, 1939
Priority dateAug 2, 1939
Publication numberUS 2311813 A, US 2311813A, US-A-2311813, US2311813 A, US2311813A
InventorsBeck Erich A, Cleveland Ralph E
Original AssigneeBeck Erich A, Cleveland Ralph E
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Paper pulp screen
US 2311813 A
Abstract  available in
Images(2)
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Claims  available in
Description  (OCR text may contain errors)

PAPER PULP SCREEN Filed Aug. 2, 1939 2 Shuts-Sheet 1 E. A. BECK "ETAL 2,311,813.

Feb.'23., 1943. BECK ETAL 2,311,813

- PAPER PULP SCREEN gned Aug. 2, 19:9 2; Shaets-Sheet 2 INVENTOR ATTORNEY Patented Feb. 23, 1943 march mom PAPER PULP SCREEN Erich A. Beck, New York, N. Y., and Ralph E. Cleveland, Waterbury, Conn.

Application August 2, 1939, Serial No. 288,018

1 Claim.

This invention relates to paper pulp screens; and it comprises a screen for screening paper pulp and the like, provided with a plurality of parallel slots with a plurality of undulations running substantially perpendicular with respect to said slots, said undulations being of such shape as to cause liquids passed across said plates to impinge against said slots by cascading and/or rippling in passing over said undulations, said screen plates being adapted to be placed in the usual pulp screens at or above the average levels of the liquid in the discharge chambers with streams of pulp passing across their surfaces in a direction substantially parallel to said slots; all as more fully hereinafter set forth and as claimed.

Early in the history of paper making it was discovered that it was necessary to screen the stock in order to remove dirt, knots and other impurities as well as oversize fibers. Since that time a large number of different methods of screening have been devised. In one of the early methods a slotted or perforated pulp screen was totally submerged within the liquid in the screening vat, the screen being reciprocated in the liquid in order to assist in the screening action. When submerged screens of this type are used, a forward and backward motion of the stock is produced but there is no continuous motion of the stock alon the surface of the screen. In this method various forms of screens were employed, in some of which flat plates were placed in a saw-tooth arrangement in order to work the unscreened stock forward when subjected to the shaking movement. In such "submerged screens" such saw-tooth arrangements were necessarily of large dimension. For example, the depressions would have a depth of 4 inches to 12 inches, in order to accomplish the above described action when submerged in a stationary liquid of considerable depth. The base line, or general direction of the screen arrangement, sloped upwardly to the end of the screen where unscreened material was discharged.

A later development involved the use of slotted screen plates which were mounted above the surface of the screened liquid in discharge chambers that contained air except for the screened stock that passed out sidewise, transversely to the direction of flow of stock above the plates, diaphragms being provided at the bottoms of the discharge chambers, which diaphragms were vibrated in order to produce alternate suction and pressure beneath the screens. The resultant intermittent forcing of air and water through the slots tended to prevent the slots from being clogged. In both of these types of screens slots were sometime placed cross-wise and sometimes length-wise of the screen. In more recent practice, flat pulp screens have become more or less standardized, being of this latter non-submerged" type. In this type. the surface of the plate is not submerged below the average level of the liquid in the screening vat. The flash boards, which control the levels of the stock in the discharge chambers, are set with their upper edges either at or just below the level of the screen. The slope of the base line of the screen is downward to the end where unscreened material is discharged.

This modern pulp screen, which is conventionally used in large scale production, has a flat screening surface and is composed of from about 12 to screen plates provided with slots usually running parallel to the flow of stock. The general plane of the screen is inclined to the horizontal about 3 to 10 degrees in such direction as to assist in the flow of stock across its surface. Diaphragms are operated under each pair of screen plates so as to force a mixture of air and water up through the slots to clean them, and to draw stock down through the slots during the suction action. The stock screened in this manner usually consists of from about 0.5 to 1 per cent of dry paper fiber suspended in water. This stock is passed over the screen in a layer which varies in thickness from about 4 inches at the upper end down to zero at the lower end. It will be noted that, with this type of screen, there is a continuous flow of stock along the surface of the screen in the direction of its base line. The relative motion of stock and screen is uni-directional.

The conventional screen plate is approximately 11 inches to 12 inches wide, 43 inches long and inch thick. Fine slots about 2 inches to 4 inches in length are sawed into the plate, these slots being usually arranged in from two to four rows which run from one end of the plate to the other, leaving uncut longitudinal sections in between which serve as strengthening bars. To make a pulp screen a number of these screen plates are placed transversely in an elongated, sloping screening vat having a width corresponding to the length of the plates. Holding members are provided between the plates, forming a flat but sloping screening surface across which the stock flows smoothly toward the lower end of the screen. Screening vats are usually adapted to hold from five to seven pairs of screen plates, but several of these vat are usually placed in series so as to constitute a practically continuous screen with from about 30 to 70 screen plates in all.

The screen plates of the present invention are particularly adapted for use in screening vats of the type just described in which the plates are supported at or above the level of the screened stock in the discharge chambers under each pair of plates, and the stock is passed in a stream across the plates, the slots in the plates being usually parallel to the line of flow of the stock.

We have found that, if the usual paper stock is forced to impinge repeatedly against a slotted screening surface by being cascaded on to these surfaces or by being forced to change its direction of fiow as it passes over the surfaces in such manner that the momentum of the stock tends to force it through the slots, a much more efficient screening action is secured. This result is produced by undulating the surface of the screen plate in a direction perpendicular to the flow of stock. Of course, such undulations must be of suitable size in order to produce this action without blocking the flow of stock. This may be accomplished by providing step in the plate over which the stream of pulp is forced to cascade upon a row of slots or at least to provide undulations of sufiicient size to cause the stream of stock to ripple in passing over the undulations, the plate being slotted at the points where its surface is concave or where the surface rises into the stream of flow.

We have found that, when a stock stream is caused to cascade or to ripple in the manner described, a two-fold effect is produced. First, the stock is forced to change its direction of flow in such manner that a force, usually a centrifugal force, is developed tending to make it pass through the slots, this force being added to the usual force of gravity as well as to the suction produced by the diaphragms. The total force tending to make the stock pass through the slots is substantially increased. The second effect is that the cascades or ripples, caused by passing over the undulations in our screen plates effectively mix the pulp with the water. When the stock passes over a conventional fiat plate, a thin layer of pulp collects adjacent the surface of the plate which impede the passage of both the water and the fibers through the slots. This layer further tends to clog the slots. But if the stock is caused to ripple or to cascade this layer of pulp is mixed with the thinner stock above and a substantially increased rate of screening results.

Surprisingly we have found that a considerable increase in screening capacity can be produced in the manner described above. Further we have found that a better screening is produced owing to the fact that less dirt and coarse fibers pass through our screens. The exact cause for this latter effect is not known but it is probably due to the repeated mixing of the stock when passing over the undulations of our screen plates; this action preventing particles of dirt from being forced through the slots by the pressure of the fibers above them. It may also be explained by the fact that satisfactory production can be obtained with less forcing of the diaphragms in the fiat screens, or of the agitating mechanism in the rotary screens.

Owing to the increased screening capacity of our screen plates we have found that it is usually possible to produce adequate screening by the use of fewer screens. The number of our plates, required to produce the same quality of screening produced by up to 0 of the fiat plates of the prior art, may sometimes be as low as 28. The total number of screen plates required in a given case may therefore be reduced by about one-half to one-third by the use of the present invention. When our screen plates are introduced into the conventional screening vat it is possible to discard the lower plates which are then unnecessary, or these may be left in service in order to collect a larger percentage of the screenable stock.

We have discovered another surprising result which is caused by the use of our undulating screen plates. We have found that the pulsating air pressure produced by the diaphragms tends to concentrate at the highest points of the under surfaces of the screen plates. But if the slots of the screen plate extend up the undulating slope to or just beyond the high point of the undulations, as in our preferred embodiment, particles of stock which are just too large to pass through the slots also tend to collect on the screen surface at these downstream ends of the slots. We find as a result of thi circumstance that the clogging stock fibers are expelled much more completely than is the case with fiat plates where no such localized concentration of air pressure is possible. This effect cannot be produced, of course, in the obsolete type of screen, the plate of which was submerged in the stock in the screening vat.

In making our plates the sections of the screening surface which are concave or which rise in the direction of the flow of stock should be slotted. The convex or downwardly sloping portions are not necessarily slotted. These unslotted portions form strengthening ribs, providing stiffness in the direction of the length of the plate. Where these unslotted portions are substantially vertical, or have a large vertical dimension as compared with their horizontal dimension, the stiffening effect is increased. An additional advantage accruing from this disposition of the stiffening portion of the screen plate is that less of the width of the plate is required to produce stiffness, and hence more width is available for slotting. In this way, the screening capacity is increased. Moreover, the slots, being set at an inclination to the horizontal, are longer than if they had been et in the horizontal surface of the conventional flat screen plate.

In view of the above, it is clear that the material of which the screen plate is to be made, or the manner in which it is to be formed, are secondary in importance. It has, however, been found that, because of the shape of the new plate, it is considerably stiffer lengthwise than the conventional plate for equal thicknesses of material and that therefore the thickness can be materially decreased without loss in rigidity. Not only is a saving in material so obtained but substantial economies in construction are made possible. For example, in conventional plates, it is necessary to mill grooves into the under side of a cast, machined plate, and then to saw slots from these grooves into the upper face. By using a thin material, the milling of the grooves can be eliminated. Moreover, because of the decreased thickness of the material, rolled sheet can be used, instead of a cast plate, and surface machining can be omitted. If flat sheet is used, it can be bent into shape or stamped or rolled. If desired, the required blanks can be made by extrusion, during which operation reinforcing ribs can be formed on the plates. Extruded sections can also be formed with the desired contour from the start. While the conventional fiat plates are fabricated from east bronze having a thickness of from inch to inch, we have found that the additional strength resulting from the undulations in our new plate, enables the use of plates ranging from about 1 inch to inch in thickness and which, as mentioned, can be made by less expensive methods than casting and from less expensive materials than bronze.

The wide variety of forming methods suitable for the making of our plates enables us to choose the material most suitable, either for easy construction, or for resistance to wear or corrosive action of the'stock, or for the deposition thereon of resistant coatings, such as, for example,

chromium. Such suitable materials may include stainless steel, Monel metal, bronze, brass or steel among others.

The longitudinal stiffness of our plates effectively maintains the slot size and there is no danger of breathing to be feared. The lateral stiffness is generally less than the longitudinal stiffness, so that our plates have a certain degree of flexibility, with the result that in case of shock, as for example by water hammer, they will flex rather than break. If a greater lateral rigidity is desired, this can be obtained by fastening braces to the underside of the plate by any convenient means, as, for example, by riveting, bolting, welding, brazing or soldering.

Our invention can be described in more detail by reference to the accompanying drawings which show, more or less diagrammatically, several embodiments of our screen plates which may be used in our process. The stock is assumed to be flowing from left to right in the several figures. In this showing,

Fig. 1 is a transverse vertical section through a screen plate, showing slotted and unslotted sections, as well as the contour of the screening surface,

Fig. 2 is a similar showing of a modification provided with strips of felt to collect dirt,

Fig. 3 is a similar showing of a modification having a wave-like contour,

Fig. 4 is a similar showing of a plate having a screening surface with sinuous contour,

Fig. 5 is a similar showing of a plate having reinforcing ribs,

Fig. 6 is a similar showing of a plate built in sections,

Fig, 7 is a diagrammatic sectional view showing, on an enlarged scale, the action of a stream of stock passing over a plate having a contour similar to that shown in Fig. 1, and

Fig. 8 is a partial, longitudinal, vertical section through a screening vat, showing the mounting of our novel plates, as well as the mechanism for producing suction and pressure beneath the plates etc.

In the various figures like parts are designated by like reference numerals. It should be noted that all figures in the drawings are section taken through the screening slots and transversely through the plates. The base lines 20 of the plates are shown on the figures, as well as horizontal lines 2|. The lengths of the plates are approximately four times their widths. The slots of the plates are shown at I while the unslotted sections are indicated at 2. Some of the plates shown are provided with bevelled edges 3 which are adapted to be secured in the screening vat by means of bevelled cleats, not shown. Others are provided with flat and squared edges 4 which may be secured by means of countersunk screws, not shown, to the screening vat.

The function of the various structures shown in the figures is believed to be more or less self evident. In Fig. 2 felt strips l5 are shown in the depressions bet-ween the undulations of the plate. These felt strips are placed along the non-slotted sections in such position that the stock passes over these felts just after passing over the undulations. The felt strips collect dirt, sand and other heavy particles, and help to prevent clogging of the slots.

In Fig. 5 a modification is shown which is provided with reinforcing bars l6 between the slotted sections. These reinforcing bars may be cast, extruded, or rolled integrally with the plate. The edges of this plate can be made in the same fashion.

In Fig. 6 the plate shown is made in sections, the ends of these sections being welded or brazed or otherwise secured together. The exposed edges of the plate sections should be bevelled as shown, in order to reduce the resistance to the flow of stock. It is evident that a plate of any desired size can be made by the use of the required number of sections.

The slots in the various embodiments shown can be sawed in the plates after they have received their final shapes but it is obvious that, in the case of some of the modifications, the slots may be sawed in a fiat sheet which then can be bent into the required undulatory form.

It is evident from the showing of Figs. 1 to 6 that the contour of the undulating screening surface used in our invention may be varied widely. It is only necessary to provide a plurality of undulations and screening sections in each plate, these being of such proportions and shape as to cause the stock to impinge against and/or cascade onto the slots without stopping the onward flow of the unscreened stock. The momentum of the flowing stock then tends to force the stock through the slots. This effect is illustrated in Fig. '7.

Fig. 7 shows diagrammatically the different actions which are involved in our invention. In the figure a stream of stock 6 is shown rising into ripples II as it passes over the undulations l of the plate. The continuous arrowed lines 8 indicate the course of flow of the various strata of liquid within the stream 6. It will be observed that the strata adjacent the surface of the plate have components of motion directed toward the slotted sections of the plate as indicated by the discontinuous arrowed lines 9. Obviously there is a tendency for the stock to pass directly through the slots rather than to continue up and over the succeeding undulations. In this drawing the stream of stock 6 is shown as being of considerable thickness, so that the undulations cause the formation only of ripples ll upon th surface of the stream. It is evident that, if the stream were of considerably lessened thickness or if the undulations were of the shape shown in Fig. 6, it would pass over the plate in a series of cascades and impinge directly upon the ends of the slots I.

As the stock passes up the rising slotted sections of the plates, the water passes through the slots somewhat more readily than the pulp, which causes a thin layer of pulp Ill (Fig. 7) to form ad- Jacent the screening surface. When the stock passes over the undulations 1, these layers of pulp become uniformly mixed with the liquid as indicated diagrammatically in the figure which means that the flow of the stock through the slots is no longer impeded by the layers of pulp.

In Fig. 8 our plates are shown mounted in a conventional screening vat. The screen plates are shown generally in this figure at 22. The ends of these plates are secured to supporting cross members 23, usually of wood. Flexible diaphragms 24 are fastened beneath these cross members. These diaphragms are supported in their centers between wooden blocks 25 and plates l5, the diaphragms being operated by means shown diagrammatically at 26. Each diaphragm extends between two screen plates, the latter being supported beneath the center of each diaphragm by means of the intermediate supporting members 3|. The diaphragms produce alternating pressure and suction beneath the screen plates and serve to draw stock through these plates. The stock to be screened is supplied by the launder 01' trough 21, formed by the boards 35 which are joined to the head board 34. The stock passes from the launder over the head-board falling on a board 29, these boards serving to distribute the stock uniformly over the screen. The screenings leave by way of the launder 30 while the screened stock which collects beneath the screen plates is withdrawn from the side of the screening vat.

Our tests show that excellent results are obtained in our invention when the slotted sections of our screen plate against which the flowing stock is forced to impinge rise, with respect to the base line of the screen plate, at an angle of at least 5 degrees. A 10 degree rise produces better results. The maximum angle of rise for good results is about 45 to 55 degrees. We have also found that it is advantageous to shape the screens in such manner that no deep pockets are formed in which dirt and other impurities may collect and which may tend to block the forward motion of the stream of pulp. In general, the pockets formed between undulations should not have a depth greater than would form a dam equal in height to the average thickness of the freely flowing stock above the plates. Satisfactory results can be obtained, for example, with pockets having a depth ranging from about A; inch to V4 inches. Constructions tending to produce the formation of eddys in which dirt might become trapped should be avoided. The plates should, of course, be streamlined, without sharp ridges or depressions which might tend to block the flow of stock.

While we have described what we consider to be the more important embodiments of our screen plate and process, it is obvious that various modifications can be made in the specific structures and procedures which have been set forth without departing from the purview of this invention. Our invention is particularly adapted for use in connection with screening vats in which the screens are rigidly secured above the liquid level in the discharge chamber, the stock flowing in a continuous stream across these screens. The structure of our screen plate may be varied widely both as to the contour of its screening surface as well as in its physical structure. It is possible, for example, to produce a complete screen from a single, l0ngitudinallyslotted, rolled sheet having a length correspond: ing to the width of two of the usual screen plates, or even to the length of the usual screening vat, this screen being provided with transverse undulations and supporting bars. The lengths and disposition of the slots in our plates may be varied in accordance with the usual practice. It is possible, for example, to incline the slots to as much as 45 degrees to the direction of the stream of stock, the undulations remaining substantially transverse to the course of the stream. With this construction the slots will have a component of their length equal to at least about 70 per cent of that length parallel to the course of the stream, and perpendicular to the undulations. The thickness of the screen plate may be varied. And, as indicated previously, a wide range of different methods of manufacturing these plates is available.

with respect to the process of our invention it is only necessary that a continuous stream of stock be passed across an undulated, slotted screening surface in such manner that its line of motion. if extended in the direction of the motion, passes through said slots at a plurality of points. This causes impingement of the stream of stock against the undulations of said screening surface and rippling or cascading where the stream crosses the undulations. The surface must be slotted at these points of impingement, the slots running in a direction substantially parallel with, or having a substantial component of their length parallel with said relative motion, whereby said impingement causes the stock to pass through said slots.

If desired, water may be sprayed on the stock as it passes over the screening surface in order to dilute and agitate the stock, and add to its momentum.

Further modifications of this invention, which fall within the scope of the following claim will be immediately evident to those skilled in this art.

In the ensuring claim, by a screen plate oi the nonsubmerged type we mean the type of plate adapted to be mounted above a discharge chamber, the chamber containing air and screened stock, the plate being mounted either at or above the average level of the screened stock in the discharge chamber.

What is claimed is:

A screen for screening thin aqueous suspensions of paper pulp in combination with a screening vat, said screen being mounted stationary in said vat above the average level of the liquid in said vat in such manner that its base line slopes downwardly towards one end of said vat, means for introducing a continuous stream of stock to be screened on the top surface of the high end of said screen, said screen being provided with slotted undulations running perpendicular to said stream of stock, said slots running parallel with the flow of stock and being sufficiently fine to screen out. knots and dirt while permitting paper fibers to pass therethrough, the undulations being of sufficient height to form depressions therebetween having depths ranging from about to 1% inches, the upstream portion of said undulations being slotted and rising at an angle of from about 5" to 45 with respect to said base line, whereby the said stream of stock is caused to repeatedly impinge against said slots in passing across said plate thereby developing a force tending to make said stock pass through said plate, and means for intermittently producing suction and pressure beneath said screen to clean the same and to draw stock through said screen.

ERICH A. BECK.

RALPH E. CLEVELAND.

Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US2446551 *Oct 19, 1945Aug 10, 1948Weyerhaeuser Timber CoSeparation of pure bark fiber from finely comminuted bark
US2626710 *Mar 29, 1948Jan 27, 1953Rudolph V SeaholmSelf-cleaning strainer for water and other liquids
US2905973 *Apr 16, 1956Sep 29, 1959William J NolanProcess for separating pith from fibers
US3409132 *Jan 3, 1966Nov 5, 1968Buckeye Cellulose CorpScreen plate for centrifugal pulp screens
US3533841 *Aug 14, 1968Oct 13, 1970Heinkel & Co Kg AFilter structure for dishwashers
US3939065 *Aug 23, 1973Feb 17, 1976Ahlfors S E EScreening device
US4758333 *Mar 23, 1987Jul 19, 1988General Electric CompanySieve
US4802591 *Mar 14, 1988Feb 7, 1989Rotex, Inc.Louvered chip screener
US4954249 *Jun 10, 1988Sep 4, 1990Beloit CorporationWave screen plate
US5023986 *Apr 17, 1990Jun 18, 1991Beloit CorporationMethod of manufacturing a wave screen plate
US5041212 *Jan 2, 1990Aug 20, 1991Beloit CorporationEfficiency screen plate for screening pulp
US5041214 *Apr 16, 1990Aug 20, 1991Beloit CorporationWave screen plate
US5285560 *Jan 24, 1992Feb 15, 1994Beloit Technologies, Inc.Method for repairing a screen plate assembly
US5575559 *Nov 1, 1995Nov 19, 1996Goulds Pumps, Inc.Mixer for mixing multi-phase fluids
US5791495 *Mar 11, 1996Aug 11, 1998Beloit Technologies, Inc.Paper pulp screen cylinder
US5944197 *Apr 24, 1997Aug 31, 1999Southwestern Wire Cloth, Inc.Rectangular opening woven screen mesh for filtering solid particles
US6530483 *Apr 12, 2001Mar 11, 2003Varco I/P, Inc.Unibody structure for screen assembly
US6892888Jul 24, 2002May 17, 2005Varco I/P, Inc.Screen with unibody structure
WO1989012137A1 *Jun 2, 1989Dec 14, 1989Beloit CorporationWave screen plate and manufacturing methods
WO1991010008A1 *Dec 5, 1990Jul 11, 1991Beloit CorporationImproved efficiency screen plate for screening pulp
Classifications
U.S. Classification209/397, 209/506
International ClassificationD21D5/00, D21D5/04
Cooperative ClassificationD21D5/04
European ClassificationD21D5/04