EP0117716B1 - Apparatus for pulping paper, and a rotor therefor - Google Patents
Apparatus for pulping paper, and a rotor therefor Download PDFInfo
- Publication number
- EP0117716B1 EP0117716B1 EP19840301139 EP84301139A EP0117716B1 EP 0117716 B1 EP0117716 B1 EP 0117716B1 EP 19840301139 EP19840301139 EP 19840301139 EP 84301139 A EP84301139 A EP 84301139A EP 0117716 B1 EP0117716 B1 EP 0117716B1
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- EP
- European Patent Office
- Prior art keywords
- rotor
- stock
- pulp
- vane
- screw
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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-
- 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
- D21B1/34—Kneading or mixing; Pulpers
- D21B1/345—Pulpers
- D21B1/347—Rotor assemblies
Definitions
- This invention relates to apparatus for pulping paper making stock at relatively high consistencies, and more particularly to paper pulping apparatus in which a vaned rotor is utilized to circulate the stock within a tub.
- Paper pulping apparatus typically includes a tub having a bottom wall and a cylindrical side wall extending upwardly therefrom, a vaned rotor centrally mounted on the bottom wall for rotation within the tub, and a screen or valve means located in or near the bottom wall to provide means for removal of the pulped paper stock.
- the rotor vanes include leading faces which are shaped and sized to contact stock near the bottom wall of the tub and propel it radially outwardly from the rotor against the side wall, which directs the stock upwardly.
- the rising stock flows to the center of the tub and then downwardly toward the rotating vanes.
- the stock is caused to flow in a generally circular pattern, and the reduction in size of the individual particles of paper stock is due largely if not exclusively to the high sheer forces between particles of stock created by this flow pattern.
- rotors In order to perform a pulping process upon stock having a consistency in excess of about 10%, special rotors have been developed.
- a high consistency pulping apparatus having a rotor with a vertically oriented and axially aligned feeding screw.
- the rotor includes vanes in the form of circumferentially-extending members with a half-crescent shape which are disposed about the periphery of a disk-shaped plate.
- the feeding screw is mounted in the center of the plate and includes a cylindrically-shaped body having a base which is spaced from the rotor vanes, and a helical screw flight which extends along the body and terminates at a squared end above the disk-sha.,,-v.3d plate supporting the vanes.
- the feeding screw When rotated in a tub containing stock at 12-13% consistency, the feeding screw guides the stock downwardly to the region of the rotor vanes which then propel it outwardly against the walls of the tub.
- the higher consistency stock climbs the walls of the tub, and baffles are employed to direct the pulp downwardly toward the tub center.
- a high consistency pulping apparatus having a rotor which minimizes the likelihood of cavitation.
- the rotor provides means for guiding the high density stock in a smooth and uninterrupted path from a location adjacent the center of the rotor to the working faces of the vanes without the stock becoming wedged between the screw flight and rotor vane.
- such a rotor is characterised by said conical body having a base with an outer periphery immediately adjacent to the said root portions such that pulp guided downwardly by said screw flight means is urged outwardly by said conical body to engage said root portions and be propelled by said vane means.
- the invention also includes apparatus for pulping paper making stock at high consistencies of the type having a tub having a bottom wall and a cylindrical side wall extending upwardly therefrom, a rotor body mounted for rotation on a vertical axis in the center of said bottom wall, vane means extending generally radially outwardly from said rotor body at root portions thereof and constructed to impel high consistency pulp stock toward said side wall, and a feed screw having a conical body mounted centrally of said rotor body and extending upwardly therefrom and screw flight means extending along said conical body for guiding pulp downwardly to said vanes, characterised by said conical body having a base with an outer periphery immediately adjacent to said root portions such that pulp guided downwardly by said screw flight means is guided outwardly to engage said root portions and be propelled by said vane means.
- the present invention provides an apparatus for pulping paper making stock which is capable of pulping relatively high consistency stock, that is, stock in a range of approximately 10-25% solids, in a manner that creates the necessary circular flow patterns to generate the high shear forces between paper particles in order to perform the pulping operation in a minimum amount of time.
- Another advantage of the invention is that it includes a rotor that is designed to minimize the likelihood of cavitation and the likelihood of stock collecting on the rotor to obstruct the downward and outward flow of stock to the vanes.
- the conical body of the feed screw includes a base sized such that its periphery is adjacent the root portions of the rotor vanes.
- the trailing end of the screw flight blends into the working face of a vane to form a continuous surface therewith.
- the flight of the feed screw includes a trailing edge which tapers in width and terminates at the periphery of the base adjacent a vane root.
- the present invention preferably includes a tub having a bottom wall and a cylindrical side wall extending upwardly therefrom, and the rotor body is centrally mounted on the bottom wall for rotation in a vertical axis.
- the feed screw is sized such that, when mounted on the rotor body, its height above the bottom wall of the pulping tub approximates the intended depth of the stock within the tub.
- the rotor of the preferred embodiment causes the stock within the tub to flow in the previously described circular pattern such that the level of the stock at the center of the tub is below the level of the stock at the side wall, thereby exposing the tip of the feed screw.
- the feed screw and stock are in this configuration, the feed screw provides a means of escape for any air which is present in the vicinity of the vanes, thus further reducing the likelihood of cavitation.
- the invention can utilize prior art rotors which previously were capable of functioning only in low consistency pulping operations.
- the feed screw can be retrofitted to a prior art rotor, such as the rotor disclosed in the Couture U.S. Patent No. 3,889,885.
- a prior art rotor such as the rotor disclosed in the Couture U.S. Patent No. 3,889,885.
- an object of the present invention to provide an apparatus for pulping paper making stock at high consistencies which minimizes the likelihood of cavitation; an apparatus which provides a continuous path along which stock may travel from an upper portion of the pulping tub to the outer tip of the vane; and an apparatus for pulping high consistency stock which can be made by modifying low consistency systems.
- the pulper shown in Figure 1 includes a tub 10 having a cylindrical upper wall 12 and a bottom wall comprising a plane center section 14 surrounded by a frusto-conical portion 16.
- the center section 14 includes a perforated bed plate 18 for draining the pulped paper stock from the tub 10 after the completion of the pulping operation.
- the tub 10 is mounted on supports 20 above a gear drive 22 which is directly driven by a motor 24.
- the cylindrical side wall 12 includes baffles 26 which direct pulp stock flowing upwardly against the wall outwardly toward the center of the tub 10.
- a rotor, generally designated 28, is mounted in the center of the perforated bed plate 18 and is driven by the motor 24 and gear drive 22.
- the rotor 28 includes a rotor body 30 having a cover plate 32 and vane ring 34.
- the vane ring 34 supports a plurality of vanes 36, alternate ones of which are of increased thickness and function as pumping vanes 38.
- the rotor 28 as described thus far is of a type well-known in the art and is commonly used in pulping devices for defibering stock at between 5% and 8% consistency.
- the structure and cooperation of the rotor 28 with the perforated bed plate 18 are described more fully in the Couture U.S. Patent No. 3,889,885, commonly assigned, the disclosure of which is incorporated herein by reference.
- the rotor 28 of the present invention differs significantly from prior art rotors in that it includes a feed screw, generally designated 40.
- the feed screw 40 includes a conical body 42 which is concentric with the rotor body 30, and extends upwardly therefrom.
- the rotor 28 may be cast as a single unit, or the feed screw 40 and rotor body 30 may be fabricated separately and then joined together.
- the conical body 42 includes a rounded top 44 and a circular base 46 which extends to the root portions 48 of the pumping vanes 38.
- the feed screw 40 includes helical screw flights 50, 52 which intertwine along the length of the conical body 42.
- Each of the screw flights 50, 52 is ribbon-shaped and includes a trailing portion 54 which terminates at the base 46 of the conical body 42 adjacent the root 48 of a vane 38.
- the trailing portions 54 are twisted so that their undersides 56 are contiguous with the face 58 of the pumping vane 38 so as to form a continuous surface therewith.
- the tub 10 Prior to operation, the tub 10 is filled with paper making stock 60 which preferably is at a consistency of between 12% and 25% solids. The level of the stock within the tub 10 should approximate the height of the rounded top 44 of the feed screw 40 above the center section 14.
- the rotor 28 is rotated in a counterclockwise direction, indicated by arrows A shows in Figures 2 and 3.
- the helical screw flights 50, 52 of the feed screw 40 draw the stock 60 downwardly toward the rotor body 30.
- the stock is urged outwardly by the increasing diameter of the conical body 42.
- the stock travels in a downward helical path of increasing diameter, as indicated by arrows B in Figure 3.
- the pulp Once the pulp has contacted the vanes 38, it is propelled outwardly in a generally radial direction toward the frusto-conical portion 16, and then upwardly against the wall 12 to the top of the tub 10.
- the rising pulp encounters the baffles 26 which act to direct the pulp downwardly and inwardly toward the center of the tube where it again is directed toward the rotor body 30 by the feed screw 40.
- the baffles 26 Due to the high consistency of the stock 60, the depth of the upwardly rising stock at the periphery of the tub 10 is greater than that at the tub center. Therefore, during operation, the rounded top 44 becomes exposed and the feed screw provides a channel or conduit for the escape of air from the vicinity of the rotor body 30, thereby further reducing the likelihood of cavitation.
- the apparatus can be operated such that the depth of stock in the tub may exceed the height of the top 44, in which case the feed screw 40 will convey air to the upper level of the stock, where it will escape through the remaining stock to the atmosphere.
- the conical body 42, the flights 50, 52 and the vane faces 58 combine to provide a substantially continuous pathway which positively guides the stock from the top of the feed screw 40 to the outer tips of the rotor vane faces 58. Since the trailing portions 54 of the screw flights blend into the vane faces 58, there are no pockets or gaps which may collect pulp or form voids, so that the generated flow of pulp is much smoother than with prior art rotors having feed screws whose flights are not contiguous with the vane roots 48.
- the rotor 28A shown in Figure 4 includes a rotor body 30A in which a feed screw 40A has been attached to the cover plate 32A by a bolted flange 62 which extends outwardly from the ps'iphery base 46A of the conical body 42A.
- the design of the rotor 28A differs from the rotor 28 shown in Figures 1-3 in that the periphery of the base 46A is not immediately adjacent the vane roots 48A of the pumping vanes 38A.
- trailing portions 54A of the screw flights 50A, 52A are not contiguous with the vane roots 48A. Rather, the trailing portions 54A taper in width until they terminate at a point 64 located at the base 46A of the conical body 42A.
- the feed screw 40A cannot be fabricated easily such that its trailing portions 54A blend into the vane faces 58A of the pre-existing rotor 28A, it is desirable to taper the width of the trailing portions to a point 64 to reduce the likelihood that pulp stock will become wedged in the space between the underside of the trailing portions and the cover plate 32A or other portions of the rotor body 30A.
- the feed screw 40A will still impart a downward and outward motion to the pulp stock within a tub which directs it to the faces 58A of the vanes 38A. This motion minimizes the likelihood that pump stock will collect or stagnate in the central area of the rotor body 30A and not flow to the pumping vanes 38A.
- a rotor 28B includes a rotor body 30B having four vanes 368, each of which includes a pumping face 588.
- the vanes 36B are mounted on a generally frusto-conical shaped vane ring 348.
- Rotor bodies 30B of this type are generally used in pulping operations where the consistency of the pulp stock is between 5% and 8% solids.
- a feed screw 40B is mounted to the central portion of the rotor body 30B and includes screw flights 50B, 52B which intertwine about the conical body 42B and terminate immediately adjacent the vane roots 48B.
- Each of the trailing portions 548 of the screw flights 50B, 52B taper in width in a manner similar to that of the embodiment of Figure 4 and terminate at a point 64B on the base 468 of the conical body 428.
- the outer edges 66 of the trailing portions 548 combine with the upper edges 68 of the pumping faces 58B to form continuous edges therewith.
- the location of the trailing portions and the base 468 of the conical body 42B combine to provide a continuous path for the paper stock which guides the stock directly to the pumping faces 58B of the vanes 36B.
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Description
- This invention relates to apparatus for pulping paper making stock at relatively high consistencies, and more particularly to paper pulping apparatus in which a vaned rotor is utilized to circulate the stock within a tub.
- Paper pulping apparatus typically includes a tub having a bottom wall and a cylindrical side wall extending upwardly therefrom, a vaned rotor centrally mounted on the bottom wall for rotation within the tub, and a screen or valve means located in or near the bottom wall to provide means for removal of the pulped paper stock. The rotor vanes include leading faces which are shaped and sized to contact stock near the bottom wall of the tub and propel it radially outwardly from the rotor against the side wall, which directs the stock upwardly. The rising stock flows to the center of the tub and then downwardly toward the rotating vanes. Thus during a pulping operation, the stock is caused to flow in a generally circular pattern, and the reduction in size of the individual particles of paper stock is due largely if not exclusively to the high sheer forces between particles of stock created by this flow pattern.
- Many pulping devices of this construction presently in use are limited in application to paper making stock having a relatively low consistency, typically in the range of 4-7% solids content. If the consistency of the stock is raised appreciably above about 7%, the density of viscosity of the stock is such that it does not easily flow downwardly between the spinning vanes of the rotor. The vanes will displace an initial quantity of pulp outwardly, but cavitation will then occur since the displaced pulp is not replaced by downwardly flowing pulp.
- In order to perform a pulping process upon stock having a consistency in excess of about 10%, special rotors have been developed. For example, in our copending E.P. Application EP-A-122911 (
Article 54,3 EPC) a high consistency pulping apparatus is disclosed having a rotor with a vertically oriented and axially aligned feeding screw. The rotor includes vanes in the form of circumferentially-extending members with a half-crescent shape which are disposed about the periphery of a disk-shaped plate. The feeding screw is mounted in the center of the plate and includes a cylindrically-shaped body having a base which is spaced from the rotor vanes, and a helical screw flight which extends along the body and terminates at a squared end above the disk-sha.,,-v.3d plate supporting the vanes. - When rotated in a tub containing stock at 12-13% consistency, the feeding screw guides the stock downwardly to the region of the rotor vanes which then propel it outwardly against the walls of the tub. The higher consistency stock climbs the walls of the tub, and baffles are employed to direct the pulp downwardly toward the tub center.
- The potential advantages of high consistency pulping devices have been well recognized. For example, since the density of the stock is considerably higher for pulp stock having a consistency of about 14% than for stock having a consistency of about 7%, the shear stresses created during a high consistency pulping operation are significantly greater, so that the time required to perform a pulping operation with high consistency stock may be the same or even less than the time required for pulping the same volume of low consistency stock in the same pulping tub.
- However, there often exist inherent disadvantages with high consistency pulping devices of the type previously described. For example, since the helical screw flight of the feeding screw terminates above the base of the rotor and is spaced from the rotor vanes, there may exist a tendency for the high density stock to collect and form a wedge between the underside of the trailing portion of the screw flight and the portion of the rotor base immediately beneath it. Another disadvantage is that there does not exist means to guide the stock from the squared trailing portion of the screw flight to the working faces of the vanes, so that voids may be created surrounding the working faces of the vanes.
- Accordingly, there is a need for a high consistency pulping apparatus having a rotor which minimizes the likelihood of cavitation. There is also a need for a high consistency pulping apparatus in which the rotor provides means for guiding the high density stock in a smooth and uninterrupted path from a location adjacent the center of the rotor to the working faces of the vanes without the stock becoming wedged between the screw flight and rotor vane.
- It is known from GB-A-1 176 412 and DE-A-2 542 065 to provide a rotor for use in pulping paper making stock at high consistencies of the type having a rotor body adapted for mounting on a vertically extending drive shaft, vane means attached at root portions thereof to said rotor body and extending generally radially outwardly therefrom, and a feed screw having a conical body mounted centrally of said rotor body and extending upwardly therefrom, and screw flight means extending along said conical body for guiding pulp downwardly to said vanes.
- It is an object to provide an improved rotor having the aforesaid features.
- According to the invention such a rotor is characterised by said conical body having a base with an outer periphery immediately adjacent to the said root portions such that pulp guided downwardly by said screw flight means is urged outwardly by said conical body to engage said root portions and be propelled by said vane means.
- The invention also includes apparatus for pulping paper making stock at high consistencies of the type having a tub having a bottom wall and a cylindrical side wall extending upwardly therefrom, a rotor body mounted for rotation on a vertical axis in the center of said bottom wall, vane means extending generally radially outwardly from said rotor body at root portions thereof and constructed to impel high consistency pulp stock toward said side wall, and a feed screw having a conical body mounted centrally of said rotor body and extending upwardly therefrom and screw flight means extending along said conical body for guiding pulp downwardly to said vanes, characterised by said conical body having a base with an outer periphery immediately adjacent to said root portions such that pulp guided downwardly by said screw flight means is guided outwardly to engage said root portions and be propelled by said vane means.
- The present invention provides an apparatus for pulping paper making stock which is capable of pulping relatively high consistency stock, that is, stock in a range of approximately 10-25% solids, in a manner that creates the necessary circular flow patterns to generate the high shear forces between paper particles in order to perform the pulping operation in a minimum amount of time. Another advantage of the invention is that it includes a rotor that is designed to minimize the likelihood of cavitation and the likelihood of stock collecting on the rotor to obstruct the downward and outward flow of stock to the vanes.
- The downward and outward movement of the pulp resulting from the rotation of the feed screw causes the pulp to flow directly to the faces of the vanes and reduces the likelihood of the stock collecting on the rotor between the feed screw and vanes. Furthermore, this flow path ensures that stock flows downwardly between vanes so that the entire face of each vane can provide the maximum pumping action for which it was designed.
- In a preferred embodiment, the conical body of the feed screw includes a base sized such that its periphery is adjacent the root portions of the rotor vanes. The trailing end of the screw flight blends into the working face of a vane to form a continuous surface therewith. In another embodiment, the flight of the feed screw includes a trailing edge which tapers in width and terminates at the periphery of the base adjacent a vane root. Thus, the combination of the feed screw with the rotor provides a guiding surface along which the stock may travel which extends from the upper tip of the feed screw to the outer tip of the rotor vane.
- The present invention preferably includes a tub having a bottom wall and a cylindrical side wall extending upwardly therefrom, and the rotor body is centrally mounted on the bottom wall for rotation in a vertical axis.
- The feed screw is sized such that, when mounted on the rotor body, its height above the bottom wall of the pulping tub approximates the intended depth of the stock within the tub. When rotated, the rotor of the preferred embodiment causes the stock within the tub to flow in the previously described circular pattern such that the level of the stock at the center of the tub is below the level of the stock at the side wall, thereby exposing the tip of the feed screw. When the feed screw and stock are in this configuration, the feed screw provides a means of escape for any air which is present in the vicinity of the vanes, thus further reducing the likelihood of cavitation.
- Another advantage of the construction of the present invention over prior art high consistency pulping devices is that the invention can utilize prior art rotors which previously were capable of functioning only in low consistency pulping operations. By sizing the feed screw such that the periphery of the base and trailing portion of the flight are substantially contiguous with the faces of the vanes, the feed screw can be retrofitted to a prior art rotor, such as the rotor disclosed in the Couture U.S. Patent No. 3,889,885. However, due to the nature of high consistency paper making stock, it is preferable although not necessary to utilise a rotor having between three and six vanes, since it is difficult to cause high consistency pulp to flow between the relatively narrow spaces existing between the vanes of rotors having more than six vanes. In rotors having more than three or four vanes, it is also preferable to utilise a feed screw having multiple flights so that the stock can be urged downwardly and outwardly in a relatively balanced pattern about the periphery of the rotor.
- Accordingly, it is an object of the present invention to provide an apparatus for pulping paper making stock at high consistencies which minimizes the likelihood of cavitation; an apparatus which provides a continuous path along which stock may travel from an upper portion of the pulping tub to the outer tip of the vane; and an apparatus for pulping high consistency stock which can be made by modifying low consistency systems.
- Other objects and advantages of the present invention will become apparent from the following description, the accompanying drawings and the appended claims. In order that the invention may be more readily understood, reference will now be made to the accompanying drawings, in which:
- Figure 1 is a perspective view of the pulping apparatus of the preferred embodiment of the invention in which the tub wall has been cut away to show the rotor;
- Figure 2 is a detail of the rotor of Figure 1;
- Figure 3 is a side elevation in section of the tub of Figure 1 showing the flow pattern of pulp stock during a pulping operation;
- Figure 4 is an alternate embodiment of the rotor of the invention; and
- Figure 5 is another embodiment of a rotor of the invention.
- The pulper shown in Figure 1 includes a
tub 10 having a cylindricalupper wall 12 and a bottom wall comprising aplane center section 14 surrounded by a frusto-conical portion 16. As shown in Figure 2, thecenter section 14 includes aperforated bed plate 18 for draining the pulped paper stock from thetub 10 after the completion of the pulping operation. Thetub 10 is mounted onsupports 20 above agear drive 22 which is directly driven by amotor 24. Thecylindrical side wall 12 includesbaffles 26 which direct pulp stock flowing upwardly against the wall outwardly toward the center of thetub 10. - A rotor, generally designated 28, is mounted in the center of the
perforated bed plate 18 and is driven by themotor 24 andgear drive 22. Therotor 28 includes arotor body 30 having acover plate 32 andvane ring 34. Thevane ring 34 supports a plurality ofvanes 36, alternate ones of which are of increased thickness and function aspumping vanes 38. Therotor 28 as described thus far is of a type well-known in the art and is commonly used in pulping devices for defibering stock at between 5% and 8% consistency. The structure and cooperation of therotor 28 with theperforated bed plate 18 are described more fully in the Couture U.S. Patent No. 3,889,885, commonly assigned, the disclosure of which is incorporated herein by reference. - However, the
rotor 28 of the present invention differs significantly from prior art rotors in that it includes a feed screw, generally designated 40. Thefeed screw 40 includes aconical body 42 which is concentric with therotor body 30, and extends upwardly therefrom. Therotor 28 may be cast as a single unit, or thefeed screw 40 androtor body 30 may be fabricated separately and then joined together. Theconical body 42 includes arounded top 44 and acircular base 46 which extends to theroot portions 48 of thepumping vanes 38. - The
feed screw 40 includeshelical screw flights conical body 42. Each of thescrew flights portion 54 which terminates at thebase 46 of theconical body 42 adjacent theroot 48 of avane 38. In the embodiment shown in Figures 1 and 2, the trailingportions 54 are twisted so that theirundersides 56 are contiguous with theface 58 of the pumpingvane 38 so as to form a continuous surface therewith. - The operation of the pumping apparatus is best shown in Figure 3. Prior to operation, the
tub 10 is filled withpaper making stock 60 which preferably is at a consistency of between 12% and 25% solids. The level of the stock within thetub 10 should approximate the height of therounded top 44 of thefeed screw 40 above thecenter section 14. Once thetub 10 is filled, therotor 28 is rotated in a counterclockwise direction, indicated by arrows A shows in Figures 2 and 3. When the rotational speed of therotor 28 has reached its intended operational speed, thehelical screw flights feed screw 40 draw thestock 60 downwardly toward therotor body 30. At the same time, the stock is urged outwardly by the increasing diameter of theconical body 42. Thus, the stock travels in a downward helical path of increasing diameter, as indicated by arrows B in Figure 3. - Since the
base 46 of thehelical body 42 and the trailingportions 54 of the screw flights are located adjacent theroots 48 of thevanes 38, thestock 60 is guided directly to thefaces 58 of the pumpingvanes 38. The downward and outward motion imparted to thestock 60 by the cooperation of theconical body 42 andflights vanes vane face 58. Thus, the efficiency of thevanes 38 is increased since almost the entire vane face 58 contacts thepulp 60. - Once the pulp has contacted the
vanes 38, it is propelled outwardly in a generally radial direction toward the frusto-conical portion 16, and then upwardly against thewall 12 to the top of thetub 10. The rising pulp encounters thebaffles 26 which act to direct the pulp downwardly and inwardly toward the center of the tube where it again is directed toward therotor body 30 by thefeed screw 40. Due to the high consistency of thestock 60, the depth of the upwardly rising stock at the periphery of thetub 10 is greater than that at the tub center. Therefore, during operation, the rounded top 44 becomes exposed and the feed screw provides a channel or conduit for the escape of air from the vicinity of therotor body 30, thereby further reducing the likelihood of cavitation. It is to be understood that the apparatus can be operated such that the depth of stock in the tub may exceed the height of the top 44, in which case thefeed screw 40 will convey air to the upper level of the stock, where it will escape through the remaining stock to the atmosphere. - With the embodiment shown in Figures 1,2 and 3, the
conical body 42, theflights feed screw 40 to the outer tips of the rotor vane faces 58. Since the trailingportions 54 of the screw flights blend into the vane faces 58, there are no pockets or gaps which may collect pulp or form voids, so that the generated flow of pulp is much smoother than with prior art rotors having feed screws whose flights are not contiguous with thevane roots 48. - One of the advantages of the present invention is that a previously existing low consistency pulping apparatus may be converted to perform the highly efficient high consistency pulping operation of the present invention with a minimum of expense. For example, the
rotor 28A shown in Figure 4 includes arotor body 30A in which afeed screw 40A has been attached to the cover plate 32A by a bolted flange 62 which extends outwardly from theps'iphery base 46A of theconical body 42A. The design of therotor 28A differs from therotor 28 shown in Figures 1-3 in that the periphery of thebase 46A is not immediately adjacent thevane roots 48A of thepumping vanes 38A. Furthermore, the trailingportions 54A of thescrew flights vane roots 48A. Rather, the trailingportions 54A taper in width until they terminate at apoint 64 located at thebase 46A of theconical body 42A. - Since the
feed screw 40A cannot be fabricated easily such that its trailingportions 54A blend into the vane faces 58A of thepre-existing rotor 28A, it is desirable to taper the width of the trailing portions to apoint 64 to reduce the likelihood that pulp stock will become wedged in the space between the underside of the trailing portions and the cover plate 32A or other portions of therotor body 30A. Despite the fact that theconical body 42A and screwflights vane roots 48A, thefeed screw 40A will still impart a downward and outward motion to the pulp stock within a tub which directs it to thefaces 58A of thevanes 38A. This motion minimizes the likelihood that pump stock will collect or stagnate in the central area of therotor body 30A and not flow to thepumping vanes 38A. - Another application of the invention is shown in Figure 5 in which a
rotor 28B includes arotor body 30B having four vanes 368, each of which includes a pumping face 588. Thevanes 36B are mounted on a generally frusto-conical shaped vane ring 348.Rotor bodies 30B of this type are generally used in pulping operations where the consistency of the pulp stock is between 5% and 8% solids. - A
feed screw 40B is mounted to the central portion of therotor body 30B and includesscrew flights 50B, 52B which intertwine about the conical body 42B and terminate immediately adjacent thevane roots 48B. Each of the trailingportions 548 of thescrew flights 50B, 52B taper in width in a manner similar to that of the embodiment of Figure 4 and terminate at a point 64B on the base 468 of theconical body 428. - Since the
base 46B and points 64B are located immediately adjacent the vane roots 488, theouter edges 66 of the trailingportions 548 combine with theupper edges 68 of the pumping faces 58B to form continuous edges therewith. Again, while the trailing portions 54B of thescrew flights 50B, 52B do not blend into the pumping faces 588, the location of the trailing portions and the base 468 of the conical body 42B combine to provide a continuous path for the paper stock which guides the stock directly to the pumping faces 58B of thevanes 36B. - While the forms of apparatus herein described constitute preferred embodiments of the invention, it is to be understood that the invention is not limited to these precise forms of apparatus, and that changes may be made therein without departing from the scope of the invention as defined in the appended claims.
Claims (8)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US47084783A | 1983-02-28 | 1983-02-28 | |
US470847 | 1983-02-28 |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0117716A2 EP0117716A2 (en) | 1984-09-05 |
EP0117716A3 EP0117716A3 (en) | 1985-05-29 |
EP0117716B1 true EP0117716B1 (en) | 1988-09-07 |
Family
ID=23869305
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19840301139 Expired EP0117716B1 (en) | 1983-02-28 | 1984-02-22 | Apparatus for pulping paper, and a rotor therefor |
Country Status (6)
Country | Link |
---|---|
EP (1) | EP0117716B1 (en) |
JP (1) | JPS59199895A (en) |
BR (1) | BR8400776A (en) |
CA (1) | CA1242346A (en) |
DE (1) | DE3473894D1 (en) |
ES (1) | ES530083A0 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10821408B2 (en) | 2015-10-30 | 2020-11-03 | Lenzing Aktiengesellschaft | High-concentration mixer for producing a cellulose suspension having a high cellulose concentration |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA1228762A (en) * | 1983-05-18 | 1987-11-03 | Joseph W. Couture | Pulping apparatus and method |
DE3743247A1 (en) * | 1987-12-19 | 1989-06-29 | Escher Wyss Gmbh | PULPER WITH HIGH RESOLUTION EFFICIENCY |
SE509293C2 (en) | 1997-04-29 | 1999-01-11 | Cellwood Machinery Ab | Device at mass solver |
ITVI20020048A1 (en) * | 2002-03-19 | 2003-09-19 | Comer Spa | PROPULSOR FOR THE STIRRING OF SUSPENSIONS OF SOLIDS INSIDE A TREATMENT TANK |
GB0703053D0 (en) | 2007-02-16 | 2007-03-28 | Ici Plc | Apparatus for and Methods of Mixing and Dispensing Samples |
CN101708819B (en) * | 2008-12-03 | 2012-07-04 | 鞍钢集团矿业公司 | Ore pulp distributer |
DE102010005596B4 (en) | 2010-01-25 | 2015-11-05 | Epcos Ag | Electroacoustic transducer with reduced losses due to transversal emission and improved performance by suppression of transverse modes |
DE102011082976A1 (en) | 2011-09-19 | 2013-03-21 | Günter Betz | Device for breaking up (shredding, shredding, dissolving, processing) of waste paper and pulp in a pulper (pulper) |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3171606A (en) * | 1962-06-06 | 1965-03-02 | Ed Jones Corp | Circulating and disintegrating rotor for pulping apparatus |
GB1176412A (en) * | 1967-01-26 | 1970-01-01 | Bolton Emerson | Improvements in and relating to an apparatus and method for Pulping and Defibering |
JPS5225104A (en) * | 1975-08-14 | 1977-02-24 | Bolton Emerson | Pulp making method |
DE2542065A1 (en) * | 1975-09-20 | 1977-03-24 | Bolton Emerson | Vortical circulation fibre refining pulper - treats unconventional materials by advancing rotor to zero clearance from stator |
DE2917814C2 (en) * | 1979-05-03 | 1983-12-08 | J.M. Voith Gmbh, 7920 Heidenheim | Pulpers for the production of paper stock suspensions |
DE3027044C2 (en) * | 1980-07-17 | 1982-12-16 | J.M. Voith Gmbh, 7920 Heidenheim | Rotor for a pulper |
-
1984
- 1984-02-21 BR BR8400776A patent/BR8400776A/en unknown
- 1984-02-22 EP EP19840301139 patent/EP0117716B1/en not_active Expired
- 1984-02-22 DE DE8484301139T patent/DE3473894D1/en not_active Expired
- 1984-02-27 CA CA000448340A patent/CA1242346A/en not_active Expired
- 1984-02-27 ES ES530083A patent/ES530083A0/en active Granted
- 1984-02-28 JP JP3721584A patent/JPS59199895A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10821408B2 (en) | 2015-10-30 | 2020-11-03 | Lenzing Aktiengesellschaft | High-concentration mixer for producing a cellulose suspension having a high cellulose concentration |
Also Published As
Publication number | Publication date |
---|---|
EP0117716A2 (en) | 1984-09-05 |
ES8503050A1 (en) | 1985-02-01 |
CA1242346A (en) | 1988-09-27 |
JPH055958B2 (en) | 1993-01-25 |
DE3473894D1 (en) | 1988-10-13 |
JPS59199895A (en) | 1984-11-13 |
EP0117716A3 (en) | 1985-05-29 |
BR8400776A (en) | 1984-10-02 |
ES530083A0 (en) | 1985-02-01 |
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