US20010037866A1 - Process for dispersing a fibrous paper stock and device for performing the process - Google Patents
Process for dispersing a fibrous paper stock and device for performing the process Download PDFInfo
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- US20010037866A1 US20010037866A1 US09/832,873 US83287301A US2001037866A1 US 20010037866 A1 US20010037866 A1 US 20010037866A1 US 83287301 A US83287301 A US 83287301A US 2001037866 A1 US2001037866 A1 US 2001037866A1
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- dispersing
- accordance
- stock
- fibrous
- highly consistent
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/27—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices
- B01F27/271—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/50—Mixing liquids with solids
- B01F23/56—Mixing liquids with solids by introducing solids in liquids, e.g. dispersing or dissolving
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/83—Mixing plants specially adapted for mixing in combination with disintegrating operations
- B01F33/831—Devices with consecutive working receptacles, e.g. with two intermeshing tools in one of the receptacles
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
- D21B1/00—Fibrous raw materials or their mechanical treatment
- D21B1/04—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
- D21B1/12—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
- D21B1/30—Defibrating by other means
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
- D21D1/00—Methods of beating or refining; Beaters of the Hollander type
- D21D1/004—Methods of beating or refining including disperging or deflaking
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
- D21D1/00—Methods of beating or refining; Beaters of the Hollander type
- D21D1/20—Methods of refining
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
- D21D1/00—Methods of beating or refining; Beaters of the Hollander type
- D21D1/20—Methods of refining
- D21D1/30—Disc mills
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/50—Mixing liquids with solids
- B01F23/57—Mixing high-viscosity liquids with solids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/112—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
- B01F27/1121—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades pin-shaped
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/27—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices
- B01F27/271—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator
- B01F27/2711—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator provided with intermeshing elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/60—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/836—Mixing plants; Combinations of mixers combining mixing with other treatments
- B01F33/8361—Mixing plants; Combinations of mixers combining mixing with other treatments with disintegrating
- B01F33/83612—Mixing plants; Combinations of mixers combining mixing with other treatments with disintegrating by crushing or breaking
Definitions
- the invention relates to a process and device for dispersing fibrous paper stock.
- the preocess includes providing an aqueous fibrous paper stock, pressing out some of the water to form a highly consistent coarse fibrous paper stock, transporting the highly consistent coarse fibrous paper stock into a dispersing machine, and dispersing with a dispersing machine.
- the dispersing machine includes at least two dispersing fittings (tools, elements), which have several interlocking lines of teeth and are movable relative to one another at a distance so as to disperse the highly consistent fibrous paper stock.
- Processes of the above-mentioned type are used, for instance, for improving the quality of fibrous stock made from recycled paper. It is known that fibrous paper stock can be homogenized by dispersion and, thus, be considerably improved. For this purpose, a highly consistent fibrous stock is produced having a dry content ranging from about 15 to 35%. In many cases, dispersion occurs at a temperature far exceeding the ambient temperature. Dispersion armaments used for such processes are compact and their dispersion effectiveness is excellent. However, they rely on an even stock flow. Since the duration in which the stock remains between them is very short, irregularities cannot be compensated. Thus, inhomogeneous dispersing would result.
- a dispersion device is known from DE 197 12 653 A1 into which the plug from the worm extruder is directly introduced. Here, it is ground by a grinding tools using scrapers or knives which are positioned in the feeder of the dispersing device.
- the present invention provides a device capable of feeding the highly consistent plug originating from the worm extruder into the dispersing process such that a particularly even dispersing is ensured at high operating security.
- the process of the present invention includes, prior to dispersing, introducing the highly consistent coarse fibrous stock into an effective area of a rotating mallet roll having circulating mallets which cooperate with fixed peripheral impact sections to loosen and distribute the highly consistent fibrous stock.
- the beetle roller used according to the invention accepts the plug pieces compressed by the water being pressing out and breaks them up, in particular, by cooperation of the circulating beetles with the impact sections fixed to the circumference. Bigger chunks remain in the processing area longer until they can pass so that the stock flow to the dispersing machine becomes very even. Then, it is further reduced and swirled in the radially interior area of the dispersing armaments, creating very fine fibrous crumbs. If desired, steam is introduced subsequently downstream into a heating zone of the armaments in order to heat the stock to the required temperature. Here, due to the previous breaking up, a comparatively short heating duration is sufficient.
- the dispersing itself i.e., the modification of the stock characteristics occurs in a dispersing zone of the device that follows downstream.
- the present invention is directed to a process for dispersing fibrous paper stock that includes delivering an aqueous fibrous paper stock, pressing some water out of the aqueous fibrous paper stock to form a highly consistent coarse fibrous paper stock, and introducing the highly consistent coarse fibrous stock into an effective area of a mallet roll having circulating mallets which cooperate with fixed peripheral impact sections. In this manner, the highly consistent coarse fibrous stock is loosened and distributed.
- the process also includes transporting the highly consistent fibrous paper stock into a dispersing machine, and dispersing the highly consistent fibrous paper stock in a dispersing machine.
- the dispersing machine may include at least two dispersing fittings with several lines of teeth.
- the at least two dispersing fittings can be arranged so that the several lines of teeth are intermeshed and spaced at a distance from each other, and the process can further include rotating the at least two dispersing fittings relative to each other.
- the process can also include introducing water steam into the highly consistent fibrous stock while it is located between the dispersing fittings, whereby the highly consistent fibrous stock is heated.
- the dispersing fittings can include a primary dispersing area and a ring shaped heating zone arranged radially inside of the primary dispersing area, and the process can include introducing the water steam into the ring shaped heating zone.
- the mallet roll can be essentially horizontally positioned, and the process may further include introducing the fibrous stock into the effective area of the mallet roll from above.
- a worm extruder can assist in the pressing of water out of the aqueous fibrous paper stock. Further, a transport direction in the worm extruder can be essentially horizontal and an axis of the mallet roll may be essentially horizontal and substantially perpendicular to the worm extruder transport direction.
- the process may further include rotating the mallets at a circumferential speed in a range between about 1 to 5 m/s, and can also include rotating the mallets at a circumferential speed of between about 2 and 4 m/s.
- the process can include calibrating the highly consistent fibrous stock between impact sections positioned at a distance from each other, as well as adjusting a maximum amount of calibrated fibrous stock pieces in the longitudinal direction to a size in a range between about 5 to 50 mm.
- the process includes transferring a specific work amount of less than about 1 kWh/t from the mallet roll to the fibrous stock.
- the process also includes dropping the fibrous stock, after passing the mallet roll, into a screw conveyor, and centrally introducing the dropped fibrous stock into the dispersing machine via the screw conveyor.
- the process includes heating the highly consistent fibrous stock while it is located between the dispersing fittings.
- the process may include introducing water steam between the dispersing fittings and into the highly consistent fibrous stock.
- the dispersing fittings may include a primary dispersing area and a ring shaped heating zone arranged radially inside of the primary dispersing area, and the process can also include introducing the water steam into the ring shaped heating zone to heat the highly consistent fibrous stock.
- the present invention is directed to an apparatus for performing a process for dispersing fibrous paper stock.
- the apparatus can include a worm extruder structured and arranged to create a highly consistent coarse fibrous paper stock, and a distribution device arranged downstream from the worm extruder, relative to a stock transport direction, and a dispersing machine.
- the distribution device includes at least one rotating mallet roll including a plurality of essentially radially extending mallets, a housing, and a plurality of impact sections arranged to extend essentially radially inwardly from an interior wall of the housing.
- the plurality of mallets and the plurality of impact sections can be axially spaced from each other.
- the mallet roll may be essentially horizontally arranged.
- an outermost diameter of the mallets may be in a range of between about 200-1000 mm.
- the impact sections may have staff shapes. Additionally, or alternatively, the impact sections may have plate shapes.
- An axial distance between neighboring impact sections may be in a range between about 10 and 100 mm. Further, an axial distance between the mallets and the impact sections can be in a range between about 5 to 50 mm.
- a length of the mallet roll within a tolerance of about ⁇ 20%, may be equivalent to an outer diameter of a press screw of the worm extruder.
- the dispersing machine may include at least two dispersing fittings with several lines of teeth mounted for rotation relative to each other, and the at least two dispersing fittings can be arranged so that the several lines of teeth are intermeshed and spaced at a distance from each other.
- a steam introducing element may be arranged to introduce water steam into the highly consistent fibrous stock while it is located between the dispersing fittings.
- the dispersing fittings can include a primary dispersing area and a ring shaped heating zone arranged radially inside of the primary dispersing area, and a steam introducing element can be arranged to introduce water steam into the ring shaped heating zone.
- FIG. 1 schematically illustrates a device for performing the process according to the present invention
- FIG. 2 illustrates an alternative device which is similar to that depicted in FIG. 1;
- FIG. 3 schematically illustrates a distribution device according to the instant invention.
- FIG. 1 shows details of a device that is particularly well suited for performing the process according to the invention.
- a worm extruder 8 is discernible in which a large portion of water W is expressed from aqueous fibrous paper stock S 1 .
- a compacted, highly consistent fibrous stock S 2 is produced, which breaks off in large chunks at the end of the press section and drops through a short shaft 10 into a distribution device 9 positioned below.
- Mallet roll 1 cooperates with impact sections 3 mounted in a fixed manner at the periphery, i.e., the housing of distribution device 9 , so that the above-described effect can occur.
- Such impact sections can be embodied in the form of radially oriented staffs, as depicted here or, e.g., cubic or plate-shaped as well.
- a highly consistent fibrous stock S 3 moves through a drop funnel 11 to a screw conveyer 7 installed immediately in front of dispersing machine 4 .
- Screw conveyer 7 drives fibrous stock S 3 into a central area of dispersing machine 4 so that it arrives between dispersing fittings 5 and 6 and is dispersed.
- Dispersing fittings 5 and 6 include concentric lines of axially interlocking teeth which are spaced a small distance from each other and are arranged to move past one another. However, the rotor and the stator are not pressed against each other. Such dispersing fittings are particularly effective, but require as even a stock flow as possible for an even dispersion.
- a steam introduction 12 It may be preferred to raise the temperature of the stock to be dispersed to a higher temperature via a steam introduction 12 .
- hot water steam D is introduced into a space between dispersing fittings 5 and 6 , and preferably into a ring-shaped heating zone 13 positioned radially inside a primary dispersing area 14 of dispersing fittings 5 and 6 .
- primary dispersing area 14 the interlocking lines of teeth operate such that the highly consistent fibrous paper stock is dispersed in a manner that is known per se.
- dispersed fibrous paper stock S 4 exits dispersing machine 4 through an opening in the bottom.
- FIG. 2 depicts an arrangement of devices used for performing the process in a different view, i.e., seen in the direction toward dispersing machine 4 .
- distribution device 9 designed in accordance with the features of the instant invention, not only is an optimal distribution of stock produced by worm extruder 8 achieved, but also the advantage of a space-saving arrangement.
- a relatively large diameter must be selected for the shaft of worm extruder 8 due to the relatively large amounts of stock.
- the fibrous stock produced at the end of worm extruder 8 cannot flow and, therefore, an arrangement should be made so that it can essentially fall freely straight downward.
- the position of distribution device 9 in the manner shown allows to intercept the fibrous stock produced over the entire length of worm extruder 8 and to guide it off into drop shaft 10 positioned below after appropriate treatment. Therefore, it is advantageous to position mallet roll 1 perpendicular to a main transport direction of worm extruder 8 .
- This unit, i.e., worm extruder 8 and distribution device 9 can be advantageously positioned in relation to dispersing machine 4 depending on the availability of space.
- FIG. 3 The basic design of distribution device 9 with mallet roll 1 is shown in FIG. 3.
- Mallet roll 1 with a length L contains a number of mallets 2 whose outer ends rotate in a circle having a diameter D. They cooperate with impact sections 3 mounted to housing 15 of this device. This achieves the fact that the incoming coarse fibrous paper stock is first broken up. The breaking up occurs with a relatively small amount of force which can be explained in that the fibrous paper stock produced here is only compressed and merely this compression needs to be loosened. This is not to be compared, e.g., with recycled paper present in moist webs such as the one processed in, e.g., pulpers.
- the distances a between axially neighboring fixed impact sections 3 are chosen such that highly consistent fibrous stock S 2 is calibrated in between, i.e., the passing of stock chunks that are not been sufficiently broken up is prevented.
- the particles passing in the longitudinal direction have a defined maximum size of, e.g., about 30 mm. Accordingly, the distance a could be determined by a simple experiment. It could also be advantageous to design it in a variable fashion in order to adjust the machine to different requirements.
- An axial distance b between contacting mallets 2 and impact sections 3 has a strong influence on the breaking up effect of this device as well. It is advantageously between about 5 and 20 mm.
- mallets 2 or of impact sections 3 is to be determined in accordance with the purpose.
- rather simple shapes are depicted only to demonstrate the function. They can, e.g., be in an arched shape or, viewed in the circumferential direction, diagonally positioned as well. It is also conceivable to provide them with wear-resistant coatings in order to extend their life span.
Abstract
Process and apparatus for dispersing fibrous paper stock that includes delivering an aqueous fibrous paper stock, pressing some water out of the aqueous fibrous paper stock to form a highly consistent coarse fibrous paper stock, and introducing the highly consistent coarse fibrous stock into an effective area of a mallet roll having circulating mallets which cooperate with fixed peripheral impact sections. In this manner, the highly consistent coarse fibrous stock is loosened and distributed. The process also includes transporting the highly consistent fibrous paper stock into a dispersing machine, and dispersing the highly consistent fibrous paper stock in a dispersing machine.
Description
- The present application claims priority under 35 U.S.C. § 119 of German Patent Application No. 100 18 262.3, filed on Apr. 13, 2000, the disclosure of which is expressly incorporated by reference herein in its entirety.
- 1. Field of the Invention
- The invention relates to a process and device for dispersing fibrous paper stock. The preocess includes providing an aqueous fibrous paper stock, pressing out some of the water to form a highly consistent coarse fibrous paper stock, transporting the highly consistent coarse fibrous paper stock into a dispersing machine, and dispersing with a dispersing machine. The dispersing machine includes at least two dispersing fittings (tools, elements), which have several interlocking lines of teeth and are movable relative to one another at a distance so as to disperse the highly consistent fibrous paper stock.
- 2. Discussion of Background Information
- Processes of the above-mentioned type are used, for instance, for improving the quality of fibrous stock made from recycled paper. It is known that fibrous paper stock can be homogenized by dispersion and, thus, be considerably improved. For this purpose, a highly consistent fibrous stock is produced having a dry content ranging from about 15 to 35%. In many cases, dispersion occurs at a temperature far exceeding the ambient temperature. Dispersion armaments used for such processes are compact and their dispersion effectiveness is excellent. However, they rely on an even stock flow. Since the duration in which the stock remains between them is very short, irregularities cannot be compensated. Thus, inhomogeneous dispersing would result.
- In the thickening process performed, a considerable part of the previously present water content in the fibrous stock is pressed out, because of which, its viscosity in dispersion is considerably increased and, if necessary, less water needs to be heated. Worm extruders are particularly economical machines for thickening. In a worm extruder, the fibrous stock suspension is pressed out between a conveyer screw and a perforated jacket surrounding it, with the water exiting through the perforations of the jacket. The pressed article or plug developed here is pushed out of the screw and breaks into pieces. The pieces are comparatively large and thus lead to an uneven stock flow through the subsequent devices.
- A dispersion device is known from DE 197 12 653 A1 into which the plug from the worm extruder is directly introduced. Here, it is ground by a grinding tools using scrapers or knives which are positioned in the feeder of the dispersing device.
- The present invention provides a device capable of feeding the highly consistent plug originating from the worm extruder into the dispersing process such that a particularly even dispersing is ensured at high operating security.
- Accordingly, the process of the present invention includes, prior to dispersing, introducing the highly consistent coarse fibrous stock into an effective area of a rotating mallet roll having circulating mallets which cooperate with fixed peripheral impact sections to loosen and distribute the highly consistent fibrous stock.
- With the aid of this new process, it is possible to produce a highly consistent stock that can be perfectly processed in a dispersing machine. The beetle roller used according to the invention accepts the plug pieces compressed by the water being pressing out and breaks them up, in particular, by cooperation of the circulating beetles with the impact sections fixed to the circumference. Bigger chunks remain in the processing area longer until they can pass so that the stock flow to the dispersing machine becomes very even. Then, it is further reduced and swirled in the radially interior area of the dispersing armaments, creating very fine fibrous crumbs. If desired, steam is introduced subsequently downstream into a heating zone of the armaments in order to heat the stock to the required temperature. Here, due to the previous breaking up, a comparatively short heating duration is sufficient. The dispersing itself, i.e., the modification of the stock characteristics occurs in a dispersing zone of the device that follows downstream.
- The present invention is directed to a process for dispersing fibrous paper stock that includes delivering an aqueous fibrous paper stock, pressing some water out of the aqueous fibrous paper stock to form a highly consistent coarse fibrous paper stock, and introducing the highly consistent coarse fibrous stock into an effective area of a mallet roll having circulating mallets which cooperate with fixed peripheral impact sections. In this manner, the highly consistent coarse fibrous stock is loosened and distributed. The process also includes transporting the highly consistent fibrous paper stock into a dispersing machine, and dispersing the highly consistent fibrous paper stock in a dispersing machine.
- In accordance with a feature of the instant invention, the dispersing machine may include at least two dispersing fittings with several lines of teeth. The at least two dispersing fittings can be arranged so that the several lines of teeth are intermeshed and spaced at a distance from each other, and the process can further include rotating the at least two dispersing fittings relative to each other. The process can also include introducing water steam into the highly consistent fibrous stock while it is located between the dispersing fittings, whereby the highly consistent fibrous stock is heated. Moreover, the dispersing fittings can include a primary dispersing area and a ring shaped heating zone arranged radially inside of the primary dispersing area, and the process can include introducing the water steam into the ring shaped heating zone.
- According to another feature of the invention, the mallet roll can be essentially horizontally positioned, and the process may further include introducing the fibrous stock into the effective area of the mallet roll from above.
- A worm extruder can assist in the pressing of water out of the aqueous fibrous paper stock. Further, a transport direction in the worm extruder can be essentially horizontal and an axis of the mallet roll may be essentially horizontal and substantially perpendicular to the worm extruder transport direction.
- The process may further include rotating the mallets at a circumferential speed in a range between about 1 to 5 m/s, and can also include rotating the mallets at a circumferential speed of between about 2 and 4 m/s.
- Further, the process can include calibrating the highly consistent fibrous stock between impact sections positioned at a distance from each other, as well as adjusting a maximum amount of calibrated fibrous stock pieces in the longitudinal direction to a size in a range between about 5 to 50 mm.
- According to still another feature of the instant invention, the process includes transferring a specific work amount of less than about 1 kWh/t from the mallet roll to the fibrous stock.
- The process also includes dropping the fibrous stock, after passing the mallet roll, into a screw conveyor, and centrally introducing the dropped fibrous stock into the dispersing machine via the screw conveyor.
- In accordance with a further feature of the present invention, the process includes heating the highly consistent fibrous stock while it is located between the dispersing fittings. Moreover, the process may include introducing water steam between the dispersing fittings and into the highly consistent fibrous stock. The dispersing fittings may include a primary dispersing area and a ring shaped heating zone arranged radially inside of the primary dispersing area, and the process can also include introducing the water steam into the ring shaped heating zone to heat the highly consistent fibrous stock.
- The present invention is directed to an apparatus for performing a process for dispersing fibrous paper stock. The apparatus can include a worm extruder structured and arranged to create a highly consistent coarse fibrous paper stock, and a distribution device arranged downstream from the worm extruder, relative to a stock transport direction, and a dispersing machine. The distribution device includes at least one rotating mallet roll including a plurality of essentially radially extending mallets, a housing, and a plurality of impact sections arranged to extend essentially radially inwardly from an interior wall of the housing.
- According to a feature of the invention, the plurality of mallets and the plurality of impact sections can be axially spaced from each other.
- Further, the mallet roll may be essentially horizontally arranged.
- In accordance with another feature of the instant invention, an outermost diameter of the mallets may be in a range of between about 200-1000 mm.
- According to still another feature of the invention, the impact sections may have staff shapes. Additionally, or alternatively, the impact sections may have plate shapes.
- An axial distance between neighboring impact sections may be in a range between about 10 and 100 mm. Further, an axial distance between the mallets and the impact sections can be in a range between about 5 to 50 mm.
- Moreover, a length of the mallet roll, within a tolerance of about ±20%, may be equivalent to an outer diameter of a press screw of the worm extruder.
- In accordance with yet another feature of the instant invention, the dispersing machine may include at least two dispersing fittings with several lines of teeth mounted for rotation relative to each other, and the at least two dispersing fittings can be arranged so that the several lines of teeth are intermeshed and spaced at a distance from each other. Further, a steam introducing element may be arranged to introduce water steam into the highly consistent fibrous stock while it is located between the dispersing fittings. Moreover, the dispersing fittings can include a primary dispersing area and a ring shaped heating zone arranged radially inside of the primary dispersing area, and a steam introducing element can be arranged to introduce water steam into the ring shaped heating zone.
- Other exemplary embodiments and advantages of the present invention may be ascertained by reviewing the present disclosure and the accompanying drawing.
- The present invention is further described in the detailed description which follows, in reference to the noted plurality of drawings by way of non-limiting examples of exemplary embodiments of the present invention, in which like reference numerals represent similar parts throughout the several views of the drawings, and wherein:
- FIG. 1 schematically illustrates a device for performing the process according to the present invention;
- FIG. 2 illustrates an alternative device which is similar to that depicted in FIG. 1; and
- FIG. 3 schematically illustrates a distribution device according to the instant invention.
- The particulars shown herein are by way of example and for purposes of illustrative discussion of the embodiments of the present invention only and are presented in the cause of providing what is believed to be the most useful and readily understood description of the principles and conceptual aspects of the present invention. In this regard, no attempt is made to show structural details of the present invention in more detail than is necessary for the fundamental understanding of the present invention, the description taken with the drawings making apparent to those skilled in the art how the several forms of the present invention may be embodied in practice.
- FIG. 1 shows details of a device that is particularly well suited for performing the process according to the invention. In the upper part of the drawing, a
worm extruder 8 is discernible in which a large portion of water W is expressed from aqueous fibrous paper stock S1. In this manner, a compacted, highly consistent fibrous stock S2 is produced, which breaks off in large chunks at the end of the press section and drops through ashort shaft 10 into adistribution device 9 positioned below. This contains as an essential component a mallet (hammer)roll 1 with moving mallets (hammers) 2 mounted in a circulating manner.Mallet roll 1 cooperates withimpact sections 3 mounted in a fixed manner at the periphery, i.e., the housing ofdistribution device 9, so that the above-described effect can occur. Such impact sections can be embodied in the form of radially oriented staffs, as depicted here or, e.g., cubic or plate-shaped as well. After treatment, a highly consistent fibrous stock S3 moves through adrop funnel 11 to ascrew conveyer 7 installed immediately in front of dispersingmachine 4.Screw conveyer 7 drives fibrous stock S3 into a central area of dispersingmachine 4 so that it arrives between dispersingfittings fittings - It may be preferred to raise the temperature of the stock to be dispersed to a higher temperature via a
steam introduction 12. With the aid ofsteam introduction 12, hot water steam D is introduced into a space between dispersingfittings heating zone 13 positioned radially inside aprimary dispersing area 14 of dispersingfittings primary dispersing area 14, the interlocking lines of teeth operate such that the highly consistent fibrous paper stock is dispersed in a manner that is known per se. Subsequently, dispersed fibrous paper stock S4exits dispersing machine 4 through an opening in the bottom. - FIG. 2 depicts an arrangement of devices used for performing the process in a different view, i.e., seen in the direction toward dispersing
machine 4. By usingdistribution device 9 designed in accordance with the features of the instant invention, not only is an optimal distribution of stock produced byworm extruder 8 achieved, but also the advantage of a space-saving arrangement. In the industrial use of the process, a relatively large diameter must be selected for the shaft ofworm extruder 8 due to the relatively large amounts of stock. The fibrous stock produced at the end ofworm extruder 8 cannot flow and, therefore, an arrangement should be made so that it can essentially fall freely straight downward. The position ofdistribution device 9 in the manner shown allows to intercept the fibrous stock produced over the entire length ofworm extruder 8 and to guide it off intodrop shaft 10 positioned below after appropriate treatment. Therefore, it is advantageous to positionmallet roll 1 perpendicular to a main transport direction ofworm extruder 8. This unit, i.e.,worm extruder 8 anddistribution device 9, can be advantageously positioned in relation to dispersingmachine 4 depending on the availability of space. - The basic design of
distribution device 9 withmallet roll 1 is shown in FIG. 3.Mallet roll 1 with a length L contains a number ofmallets 2 whose outer ends rotate in a circle having a diameter D. They cooperate withimpact sections 3 mounted tohousing 15 of this device. This achieves the fact that the incoming coarse fibrous paper stock is first broken up. The breaking up occurs with a relatively small amount of force which can be explained in that the fibrous paper stock produced here is only compressed and merely this compression needs to be loosened. This is not to be compared, e.g., with recycled paper present in moist webs such as the one processed in, e.g., pulpers. Advantageously, the distances a between axially neighboring fixedimpact sections 3 are chosen such that highly consistent fibrous stock S2 is calibrated in between, i.e., the passing of stock chunks that are not been sufficiently broken up is prevented. The particles passing in the longitudinal direction have a defined maximum size of, e.g., about 30 mm. Accordingly, the distance a could be determined by a simple experiment. It could also be advantageous to design it in a variable fashion in order to adjust the machine to different requirements. An axial distance b between contactingmallets 2 andimpact sections 3 has a strong influence on the breaking up effect of this device as well. It is advantageously between about 5 and 20 mm. - The shape of
mallets 2 or ofimpact sections 3 is to be determined in accordance with the purpose. Here, rather simple shapes are depicted only to demonstrate the function. They can, e.g., be in an arched shape or, viewed in the circumferential direction, diagonally positioned as well. It is also conceivable to provide them with wear-resistant coatings in order to extend their life span. - It is noted that the foregoing examples have been provided merely for the purpose of explanation and are in no way to be construed as limiting of the present invention. While the present invention has been described with reference to an exemplary embodiment, it is understood that the words which have been used herein are words of description and illustration, rather than words of limitation. Changes may be made, within the purview of the appended claims, as presently stated and as amended, without departing from the scope and spirit of the present invention in its aspects. Although the present invention has been described herein with reference to particular means, materials and embodiments, the present invention is not intended to be limited to the particulars disclosed herein; rather, the present invention extends to all functionally equivalent structures, methods and uses, such as are within the scope of the appended claims.
Claims (28)
1. A process for dispersing fibrous paper stock comprising:
delivering an aqueous fibrous paper stock;
pressing some water out of the aqueous fibrous paper stock to form a highly consistent coarse fibrous paper stock;
introducing the highly consistent coarse fibrous stock into an effective area of a mallet roll having circulating mallets which cooperate with fixed peripheral impact sections, whereby the highly consistent coarse fibrous stock is loosened and distributed;
transporting the highly consistent fibrous paper stock into a dispersing machine;
dispersing the highly consistent fibrous paper stock in a dispersing machine.
2. The process in accordance with , wherein the dispersing machine comprises at least two dispersing fittings with several lines of teeth, the at least two dispersing fittings being arranged so that the several lines of teeth are intermeshed and spaced at a distance from each other, and said process further comprises:
claim 1
rotating the at least two dispersing fittings relative to each other.
3. The process in accordance with , further comprising:
claim 2
introducing water steam into the highly consistent fibrous stock while it is located between the dispersing fittings, whereby the highly consistent fibrous stock is heated.
4. The process in accordance with , wherein the dispersing fittings include a primary dispersing area and a ring shaped heating zone arranged radially inside of the primary dispersing area, and said process comprises:
claim 3
introducing the water steam into the ring shaped heating zone.
5. The process in accordance with , wherein the mallet roll is essentially horizontally positioned, and said process further comprises:
claim 1
introducing the fibrous stock into the effective area of the mallet roll from above.
6. The process in accordance with , wherein a worm extruder assists in the pressing of water out of the aqueous fibrous paper stock.
claim 1
7. The process in accordance with , wherein a transport direction in the worm extruder is essentially horizontal and an axis of the mallet roll is essentially horizontal and substantially perpendicular to the worm extruder transport direction.
claim 6
8. The process in accordance with , further comprising:
claim 1
rotating the mallets at a circumferential speed in a range between about 1 to 5 m/s.
9. The process in accordance with , further comprising:
claim 8
rotating the mallets at a circumferential speed of between about 2 and 4 m/s.
10. The process in accordance with , further comprising:
claim 1
calibrating the highly consistent fibrous stock between impact sections positioned at a distance from each other.
11. The process in accordance with , further comprising:
claim 10
adjusting a maximum amount of calibrated fibrous stock pieces in the longitudinal direction to a size in a range between about 5 to 50 mm.
12. The process in accordance with , further comprising:
claim 1
transferring a specific work amount of less than about 1 kWh/t from the mallet roll to the fibrous stock.
13. The process in accordance with , further comprising:
claim 1
dropping the fibrous stock, after passing the mallet roll, into a screw conveyor; and
centrally introducing the dropped fibrous stock into the dispersing machine via the screw conveyor.
14. The process in accordance with , further comprising heating the highly consistent fibrous stock while it is located between the dispersing fittings.
claim 1
15. The process in accordance with , further comprising introducing water steam between the dispersing fittings and into the highly consistent fibrous stock.
claim 14
16. The process in accordance with , wherein the dispersing fittings include a primary dispersing area and a ring shaped heating zone arranged radially inside of the primary dispersing area, and said process comprises:
claim 14
introducing the water steam into the ring shaped heating zone to heat the highly consistent fibrous stock.
17. An apparatus for performing a process for dispersing fibrous paper stock, said apparatus comprising:
a worm extruder structured and arranged to create a highly consistent coarse fibrous paper stock;
a distribution device arranged downstream from said worm extruder, relative to a stock transport direction; and
a dispersing machine,
wherein said distribution device comprises:
at least one rotating mallet roll including a plurality of essentially radially extending mallets;
a housing; and
a plurality of impact sections arranged to extend essentially radially inwardly from an interior wall of said housing.
18. The apparatus in accordance with , wherein said plurality of mallets and said plurality of impact sections are axially spaced from each other.
claim 17
19. The apparatus in accordance with , wherein said mallet roll is essentially horizontally arranged.
claim 17
20. The apparatus in accordance with , wherein an outermost diameter of said mallets is in a range of between about 200-1000 mm.
claim 17
21. The apparatus in accordance with , wherein said impact sections have staff shapes.
claim 17
22. The apparatus in accordance with , wherein said impact sections have plate shapes.
claim 17
23. The apparatus in accordance with , wherein an axial distance between neighboring impact sections is in a range between about 10 and 100 mm.
claim 17
24. The apparatus in accordance with , wherein an axial distance between said mallets and said impact sections is in a range between about 5 to 50 mm.
claim 17
25. The apparatus in accordance with , wherein a length of said mallet roll with a tolerance of about ±20% is equivalent to an outer diameter of a press screw of said worm extruder.
claim 17
26. The apparatus in accordance with , said dispersing machine comprises at least two dispersing fittings with several lines of teeth mounted for rotation relative to each other; and
claim 17
said at least two dispersing fittings being arranged so that the several lines of teeth are intermeshed and spaced at a distance from each other.
27. The apparatus in accordance with , further comprising a steam introducing element arranged to introduce water steam into the highly consistent fibrous stock while it is located between said dispersing fittings.
claim 26
28. The apparatus in accordance with , wherein said dispersing fittings include a primary dispersing area and a ring shaped heating zone arranged radially inside of said primary dispersing area; and
claim 26
wherein a steam introducing element is arranged to introduce water steam into said ring shaped heating zone.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10018262A DE10018262A1 (en) | 2000-04-13 | 2000-04-13 | Process for dispersing a paper pulp and plant for carrying out the process |
DE10018262.3 | 2000-04-13 |
Publications (1)
Publication Number | Publication Date |
---|---|
US20010037866A1 true US20010037866A1 (en) | 2001-11-08 |
Family
ID=7638558
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US09/832,873 Abandoned US20010037866A1 (en) | 2000-04-13 | 2001-04-12 | Process for dispersing a fibrous paper stock and device for performing the process |
Country Status (7)
Country | Link |
---|---|
US (1) | US20010037866A1 (en) |
EP (1) | EP1147805B1 (en) |
JP (1) | JP2001348791A (en) |
AT (1) | ATE274370T1 (en) |
CA (1) | CA2344103A1 (en) |
DE (2) | DE10018262A1 (en) |
ES (1) | ES2225318T3 (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2003056097A1 (en) * | 2001-12-18 | 2003-07-10 | Metso Paper, Inc. | Broke system for a paper machine or equivalent |
WO2003056098A1 (en) * | 2001-12-18 | 2003-07-10 | Metso Paper, Inc. | Broke system for a paper machine or equivalent |
WO2003057981A1 (en) * | 2001-12-19 | 2003-07-17 | Metso Paper, Inc. | Broke system for a paper machine or an equivalent fibrous web machine |
EP1348802A1 (en) * | 2002-03-27 | 2003-10-01 | Andritz AG | Process and apparatus for dispersing a paper fibre slurry |
CN100347374C (en) * | 2005-08-30 | 2007-11-07 | 天津科技大学 | Fibre detaching apparatus with high shearing |
US8215824B2 (en) | 2006-06-03 | 2012-07-10 | Frymakoruma Ag | Homogenizer device having horizontally mounted gear rims |
CN110075746A (en) * | 2019-04-23 | 2019-08-02 | 安徽华文塑胶科技有限公司 | A kind of heavy metal-polluted soil stabilizer treatment system and processing method |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT507837B1 (en) * | 2008-12-29 | 2010-10-15 | Andritz Ag Maschf | METHOD AND DEVICE FOR DRAINING AND DISPERSING A FIBROUS MATERIAL |
AT14115U1 (en) * | 2013-04-12 | 2015-04-15 | Valmet Technologies Inc | dispersant |
DE102013226597A1 (en) * | 2013-12-19 | 2015-06-25 | Voith Patent Gmbh | Disperser-heating |
CN111608000A (en) * | 2020-05-26 | 2020-09-01 | 陈爱丽 | Paper recycling device capable of introducing shredded paper once based on paper volume change |
FI20225817A1 (en) * | 2022-09-21 | 2024-03-22 | Valmet Technologies Oy | Disperger |
CN115556265A (en) * | 2022-10-10 | 2023-01-03 | 亨弗劳恩(江苏)复合材料研发有限公司 | Chopped fiber dispersing device and dispersing method |
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JPS5430907A (en) * | 1977-08-10 | 1979-03-07 | Kobayashi Seisakusho | Beater for waste paper |
JP2964751B2 (en) * | 1991-12-18 | 1999-10-18 | 王子製紙株式会社 | Pulping method of pressure-sensitive adhesive waste paper |
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JPH08127988A (en) * | 1994-10-28 | 1996-05-21 | Chuetsu Pulp Kogyo Kk | Substratum for label and method for recycling the same |
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DE19712653C2 (en) * | 1997-03-26 | 2002-10-24 | Voith Paper Fiber Systems Gmbh | Method and device for dispersing a waste paper pulp |
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- 2000-04-13 DE DE10018262A patent/DE10018262A1/en not_active Withdrawn
-
2001
- 2001-02-09 ES ES01103044T patent/ES2225318T3/en not_active Expired - Lifetime
- 2001-02-09 AT AT01103044T patent/ATE274370T1/en not_active IP Right Cessation
- 2001-02-09 EP EP01103044A patent/EP1147805B1/en not_active Expired - Lifetime
- 2001-02-09 DE DE50103371T patent/DE50103371D1/en not_active Expired - Fee Related
- 2001-04-11 JP JP2001113172A patent/JP2001348791A/en not_active Ceased
- 2001-04-12 CA CA002344103A patent/CA2344103A1/en not_active Abandoned
- 2001-04-12 US US09/832,873 patent/US20010037866A1/en not_active Abandoned
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US5200038A (en) * | 1985-08-28 | 1993-04-06 | International Paper Company | Pulp refiner with fluidizing inlet |
US4820381A (en) * | 1987-02-25 | 1989-04-11 | Internationa Paper Company | Pulp refiner with fluidizing inlet |
US5176793A (en) * | 1988-08-30 | 1993-01-05 | Cellwood Machinery Ab | Method of treating and a disperger for disintegrating wood pulp, especially containing waste paper |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2003056097A1 (en) * | 2001-12-18 | 2003-07-10 | Metso Paper, Inc. | Broke system for a paper machine or equivalent |
WO2003056098A1 (en) * | 2001-12-18 | 2003-07-10 | Metso Paper, Inc. | Broke system for a paper machine or equivalent |
WO2003057981A1 (en) * | 2001-12-19 | 2003-07-17 | Metso Paper, Inc. | Broke system for a paper machine or an equivalent fibrous web machine |
EP1348802A1 (en) * | 2002-03-27 | 2003-10-01 | Andritz AG | Process and apparatus for dispersing a paper fibre slurry |
CN100347374C (en) * | 2005-08-30 | 2007-11-07 | 天津科技大学 | Fibre detaching apparatus with high shearing |
US8215824B2 (en) | 2006-06-03 | 2012-07-10 | Frymakoruma Ag | Homogenizer device having horizontally mounted gear rims |
CN110075746A (en) * | 2019-04-23 | 2019-08-02 | 安徽华文塑胶科技有限公司 | A kind of heavy metal-polluted soil stabilizer treatment system and processing method |
Also Published As
Publication number | Publication date |
---|---|
DE10018262A1 (en) | 2001-10-18 |
JP2001348791A (en) | 2001-12-21 |
EP1147805A1 (en) | 2001-10-24 |
ES2225318T3 (en) | 2005-03-16 |
EP1147805B1 (en) | 2004-08-25 |
CA2344103A1 (en) | 2001-10-13 |
ATE274370T1 (en) | 2004-09-15 |
DE50103371D1 (en) | 2004-09-30 |
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