Channel pulper

Information

  • Patent Grant
  • 6544385
  • Patent Number
    6,544,385
  • Date Filed
    Monday, September 16, 2002
    22 years ago
  • Date Issued
    Tuesday, April 8, 2003
    21 years ago
Abstract
A pulper in a stock preparation system includes a housing with a fiber inlet, at least one water inlet, at least one outlet and an inner chamber. A plurality of rotatable augers extend into the inner chamber.
Description




BACKGROUND OF THE INVENTION




1. Field of the Invention




The present invention relates to a stock preparation system for preparing a fiber suspension for use in a paper-making machine, and, more particularly, to a pulper in such a stock preparation system.




2. Description of the Related Art




A fiber stock preparation system is used to make a fiber suspension from a source of fiber such as wood. The fiber stock preparation system receives the raw source of fiber, breaks the raw source of fiber into individual fibers suspended within a liquid such as water, and separates contaminants from the fiber suspension.




It is known to provide a pulper in a fiber stock preparation system as described above to break down the raw source of fiber into individual fibers. A pulper typically includes a rotatable element therein which imparts mechanical forces to the source of fiber and breaks the source of fiber into individual fibers. The pulped fiber is transported downstream to other mechanical devices within the stock preparation system. For example, the pulped fiber may be further processed within a disperger. A disperger receives the pulped fiber, removes contaminants from the fiber suspension and thoroughly mixes chemicals within the fiber suspension. The disperger includes a shaft assembly with a plurality of foils which move in very close proximity relative to a plurality of foils carried by a housing. The tight tolerances within the disperger are intended to process the liquid under relatively high pressure so that the chemicals may be thoroughly mixed and the contaminants removed. To achieve thorough mixing of the chemicals, the dwell time of the fiber suspension within the disperger is relatively long. The disperger has an output which is in the form of an open end of the housing which discharges directly to the ambient environment. Because of the tight tolerances and pressures utilized within the disperger, the consistency of the input source of fiber must be relatively low in order for the disperger to operate properly without clogging. That is, the input source of fiber must have a high percentage of water by weight in order for the disperger to operate properly. For this and other reasons, such a disperger has a low throughput rate.




What is needed in the art is a pulper which can pulp an input source of fiber with a relatively high input consistency, and at a high throughput rate.




SUMMARY OF THE INVENTION




The present invention provides a pulper in a stock preparation system with a plurality of individually controllable augers which extend into an inner chamber of a housing.




The invention comprises, in one form thereof, a pulper in a stock preparation system. The pulper includes a housing with a fiber inlet, at least one water inlet, at least one outlet and an inner chamber. A plurality of rotatable augers extend into the inner chamber.




An advantage of the present invention is that a pulper with a simplified construction and high throughput rate is provided.




Another advantage is that the pulper is capable of pulping an input source of fiber that has a relatively high consistency.




Yet another advantage is that each of the augers is individually controllable and reversible, thereby avoiding clogs and maximizing both the throughput rate and the consistency of input fiber that can be pulped.




A further advantage is that the pulper is capable of pulping larger pieces of an input source of fiber. Thus, no shredder is required for shredding bales of wastepaper.











BRIEF DESCRIPTION OF THE DRAWINGS




The above-mentioned and other features and advantages of this invention, and the manner of attaining them, will become more apparent and the invention will be better understood by reference to the following description of embodiments of the invention taken in conjunction with the accompanying drawings, wherein:





FIG. 1

is a schematic, perspective view of a stock preparation system including an embodiment of a pulper of the present invention;





FIG. 2

is a schematic, side, sectional view of the stock preparation system of

FIG. 1

;





FIG. 3

is a schematic, sectional, bottom view of the stock preparation system of

FIG. 1

;





FIG. 4

is a fragmentary, sectional, perspective view of another embodiment of a tank of a pulper of the present invention; and





FIG. 5

is a fragmentary, schematic, bottom view of another embodiment of a detrashing device of a stock preparation system of the present invention;











Corresponding reference characters indicate corresponding parts throughout the several views. The exemplifications set out herein illustrate one preferred embodiment of the invention, in one form, and such exemplifications are not to be construed as limiting the scope of the invention in any manner.




DETAILED DESCRIPTION OF THE INVENTION




Referring now to the drawings, and more particularly to

FIG. 1

, there is shown a stock preparation system


10


including an embodiment of a pulper


12


of the present invention, feed device


14


, screen


16


and watering devices


18


. If stock preparation system


10


is disposed in an exterior location, it may include an enclosure


19


(

FIG. 2

) covering pulper


12


, feed device


14


and screen


16


.




Feed device


14


provides an input source of fiber


20


such as wood fiber, pulp bales or recycled paper to pulper


12


. In the embodiment shown, feed device


14


includes a conveyor


22


flanked by walls


24


. Conveyor


22


receives the input source of fiber such as a bale


20


of recycled paper or cardboard and drops the input source of fiber into pulper


12


for disintegration therein.




Although feed device


14


is shown in the form of a conveyor


22


and walls


24


in the embodiment of

FIG. 1

, it is also possible for feed device


14


to be configured differently as part of stock preparation system


10


for providing an input source of fiber to pulper


12


. For example, feed device


14


may be in the form of a sedimentation tank (not shown) with an outlet from which an input source of fiber is discharged to pulper


12


.




Screen


16


receives the pulped input source of fiber from pulper


12


and further processes the pulped input source of fiber into a fiber suspension which is utilized by a paper-making machine. In the embodiment shown, screen


16


is in the form of a vibration screen used to separate foreign particles from the pulped input source of fiber. Screen


16


sorts out contaminants having an area of approximately one square inch or larger. The reject is dumped into a dumpster box


26


for further processing or disposal. The usable fibers are fed through line


27


for further processing. Vibration screen


16


is powered by a drive unit


31


(FIG.


3


).




Watering devices


18


spray water into pulper


12


and onto screen


16


. That is, at least one water spray device


18


is associated with screen


16


, and at least one water spray device


18


is associated with pulper


12


. The water mixes with bales


20


in pulper


12


in order to facilitate pulping. The mixture has a consistency approximately between 15% and 40% when output from housing


28


. That is, bales


20


provide approximately between 15% and 40% of the weight of the mixture of bales


20


and water. The mixture can possibly have an output consistency approximately between 20% and 30%. Water from a watering device


18


also rinses usable pulp fibers from contaminants on screen


16


.




Pulper


12


generally includes a housing


28


, a discharge roll


29


, and a plurality of augers


30


,


32


. Housing


28


is in the form of a concrete or steel tank having an open top


34


providing access to an inner chamber


36


which forms a channel along the length of housing


28


. Open top


34


also provides housing


28


with a fiber inlet


38


, a water inlet


40


, and an outlet


42


. Water inlet


40


is in fluid communication with at least one water sprayer


18


.




Rotatable augers


30


,


32


extend into inner chamber


36


in a cantilevered fashion, and are spaced apart at predetermined intervals along a length of housing


28


. First augers


30


extend in a first horizontal direction


44


from a first side


46


of housing


28


. Second augers


32


extend in a second horizontal direction


48


, opposite from first horizontal direction


44


, from a second side


50


of housing


28


. Each first auger


30


is closely adjacent to at least one second auger


32


to thereby enable effective pulping therebetween. Augers


30


,


32


have respective rotational axes


52


,


54


that are parallel to and coplanar with each other in a horizontal plane. A gap


56


between augers


30


,


32


and a bottom side


58


of housing


28


is approximately between three and six inches. Augers


30


,


32


may either be separate from and attached to housing


24


, or may be integrally formed with housing


24


.




Each of augers


30


,


32


can be individually driven and controlled by a common, centralized hydraulic power unit


60


via respective drives


62


. Each of augers


30


,


32


is rotatable in either of the rotational directions indicated by double arrow


63


. Power unit


60


, which includes an electrical processor, can individually control the rotational speed, rotational direction and/or torque exerted on each of augers


30


,


32


in order to achieve good mixing and forward movement of the pulp. Drives


62


can each include either a hydraulic motor or an electric motor.




In use, the rotation of augers


30


,


32


mixes the water and input source of fiber into a pulp slurry. As the high consistency pulp slurry proceeds along the length of housing


28


, the pulp slurry is discharged from housing


28


by the rotation of discharge roll


29


. The pulp slurry is retained in housing


28


for approximately between five minutes and twenty minutes, and possibly approximately between ten minutes and fifteen minutes. If the torque exerted on one of augers


30


,


32


exceeds a predetermined level, perhaps because of a clog, power unit


60


causes a reversal of the rotational direction of that auger, thereby alleviating the clog.




In contrast with a conventional disperger used in a stock preparation system, pulper


12


of the present invention provides a very high throughput rate with a high level of input consistency. A disperger includes a shaft assembly with an auger and movable pulping foils which move relative to stationary pulping foils within a housing. However, the purpose of a disperger is entirely different than that of a pulper and accordingly the configuration of the various components within a disperger is entirely different than pulper


12


of the present invention. For example, a disperger is typically utilized to remove small contaminants (such as dirt specs, stickies and coating particles) from the fiber suspension or to thoroughly mix chemicals added to the fiber suspension. Because of this functionality, the various tolerances between the moving parts within a disperger are kept at a very small distance, the throughput rate is very low and the input consistency must be relatively low. More particularly, a disperger of conventional design receives an inlet fiber stock at a consistency of between 25 to 35%.




In contrast, pulper


12


of the present invention receives an input source of fiber at a consistency of between 80 and 100% and provides a pulped output source of fiber at a consistency of between 15 and 40%. That is, pulper


12


receives an input source of fiber with little or no water added thereto at fiber inlet


38


. Augers


30


,


32


are structured and arranged relative to each other to receive the dry input source of fiber and still adequately pulp the fiber for use by a paper-making machine. A disperger of conventional design cannot be utilized to pulp an essentially dry input source of fiber.




Bottom side


58


of housing


28


is shown in the embodiment of

FIGS. 1-3

as having a substantially flat or planar top surface. In another embodiment (FIG.


4


), a bottom side


64


of housing


66


has an undulating top surface


68


. More particularly, top surface


68


has a conical wave shape with a plurality of curved sections


70


,


72


. Each curved section


70


,


72


conforms to a portion of an outer surface of a respective one of augers


30


,


32


. For example, the surface of a curved section


70


follows along and is equidistant from the rotational path of the periphery of an associated auger


30


. That is, every point on curved section


70


may be distanced approximately between three and six inches from the rotational path of the periphery of the associated auger


30


. Likewise, every point on a curved section


72


may be distanced approximately between three and six inches from the rotational path of the periphery of an associated auger


32


. Peaks


74


formed between sections


70


,


72


prevent pulp from accumulating in areas between augers


30


,


32


where neither auger can reach the pulp.




In another embodiment (not shown), the top surface of the bottom side of the housing is provided with a series of ribs. Such ribs may extend parallel to the rotational axes of augers


30


,


32


.




Pulper


12


is shown in

FIGS. 1-3

as using a discharge roll


29


to discharge the pulped input source of fiber to a screen


16


. In another embodiment (FIG.


5


), a side wall


76


of housing


78


includes a discharge port


80


through which the pulped slurry is discharged to a screen drum


82


for further processing the pulped input source of fiber. It is possible to direct water through discharge port


80


in order to facilitate the discharge of pulp slurry therethrough. Discharge port


80


may be plugged in order to prevent the contents of housing


78


from being discharged before they are properly pulped. It is also possible to discharge the pulped input source of fiber to another type of device within stock preparation system


10


for further processing of the pulped input source of fiber into a fiber suspension useable by a paper-making machine. Augers


30


,


32


are shown in the embodiments of

FIGS. 1-5

as being conical screw type augers having a continuous series of between one and six spiraling flights.




While this invention has been described as having a preferred design, the present invention can be further modified within the spirit and scope of this disclosure. This application is therefore intended to cover any variations, uses, or adaptations of the invention using its general principles. Further, this application is intended to cover such departures from the present disclosure as come within known or customary practice in the art to which this invention pertains and which fall within the limits of the appended claims.



Claims
  • 1. A method of pulping an input source of fiber, comprising the steps of:transporting the source of fiber to a fiber inlet of a housing, said housing having an inner chamber and a plurality of rotatable augers extending into said inner chamber; injecting water into said housing; rotating said augers within said housing to thereby pulp the source of fiber and the water into a pulped output source of fiber; and discharging the pulped output source of fiber from said housing.
  • 2. The method of claim 1, wherein said rotating step includes individually controlling a respective speed of each of said augers.
  • 3. The method of claim 1, wherein said rotating step includes individually controlling a respective torque applied to each of said augers.
  • 4. The method of claim 1, wherein said rotating step includes reversing a direction of rotation of at least one of said augers if a torque applied to said at least one auger exceeds a predetermined level.
  • 5. The method of claim 1, wherein said discharging step includes rotating a discharge roll.
  • 6. The method of claim 1, wherein said discharging step includes discharging the fiber suspension through a discharge port in said housing.
  • 7. The method of claim 1, wherein the fiber suspension is retained within said housing
Parent Case Info

This is a continuation of application Ser. No. 09/710,752 filed Nov. 9, 2000. now U.S. Pat. No. 6,451,165 B1.

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Number Name Date Kind
3814336 Brewer Jun 1974 A
4111113 Lambert Sep 1978 A
4121967 Reinhall Oct 1978 A
4274786 Svensson et al. Jun 1981 A
4326913 Mattsson Apr 1982 A
4457804 Reinhall Jul 1984 A
4563243 Koch et al. Jan 1986 A
4582261 Perry Apr 1986 A
4663045 Yeagley May 1987 A
5220382 Hediger Jun 1993 A
5233932 Robertson Aug 1993 A
5871619 Finley et al. Feb 1999 A
6162496 Blue Dec 2000 A
6267847 Doelle et al. Jul 2001 B1
Continuations (1)
Number Date Country
Parent 09/710752 Nov 2000 US
Child 10/244771 US