CA2108598A1 - Rotary screening device - Google Patents
Rotary screening deviceInfo
- Publication number
- CA2108598A1 CA2108598A1 CA 2108598 CA2108598A CA2108598A1 CA 2108598 A1 CA2108598 A1 CA 2108598A1 CA 2108598 CA2108598 CA 2108598 CA 2108598 A CA2108598 A CA 2108598A CA 2108598 A1 CA2108598 A1 CA 2108598A1
- Authority
- CA
- Canada
- Prior art keywords
- screen
- rotor
- pulp
- baffle
- passage
- 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.)
- Abandoned
Links
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
- D21D5/00—Purification of the pulp suspension by mechanical means; Apparatus therefor
- D21D5/02—Straining or screening the pulp
- D21D5/023—Stationary screen-drums
- D21D5/026—Stationary screen-drums with rotating cleaning foils
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Paper (AREA)
Abstract
ABSTRACT
A rotary pulp screening device having a high efficiency. The screening device includes a rotor having an upper paraboloidal segment surrounded by a cylindrical baffle to split the incoming flow of pulp stock in two unequal parts. The predominant part flows through a first passage defined between the baffle and the paraboloidal segment of the rotor and is discharged against the screen at an intermediate axial location. The smallest part of the incoming flow passes between the baffle and the screen and merges with the main stream of the flow when reaching the outlet of the first passage.
A rotary pulp screening device having a high efficiency. The screening device includes a rotor having an upper paraboloidal segment surrounded by a cylindrical baffle to split the incoming flow of pulp stock in two unequal parts. The predominant part flows through a first passage defined between the baffle and the paraboloidal segment of the rotor and is discharged against the screen at an intermediate axial location. The smallest part of the incoming flow passes between the baffle and the screen and merges with the main stream of the flow when reaching the outlet of the first passage.
Description
2~08598 TITLE: ROTARY 8CREENING DEVICE
FIELD OF THE I~YEM~ION
The present invention relates to an apparatus for removing impurities in pulp stock, more particularly to a novel rotary screening device that uses power more efficiently.
BACRGROUND OF THE INVENTION
The screening of wood pulp slurry is necessary in the production of paper to remove large fibers, stones and other rejects. Over the years, eguipment and processes to screen pulp have improved. Initially, pulp stock was passed through a vibrating screen, an improvement of this méthod was a cylindrical pulsating method where foils were rotated inside a screen to produce a pulsating effect on a mat of fibers adjacent the screen. The present method, and the one that is used in most modern paper mills, is the rotating method where fibers are screened in a cylindrical screen, generally a vertical screen. A series of blades rotate inside the screen and pulp slurry is fed to the top of the screen. As the slurry passes through the screen, the fibers are formed into a mat between the screen basket and the impeller blades. The mat rotates due to the movement of the impeller blades and at the same ~ 2108~98 time has an axial movement downwards so that the reject particles in the pulp stock are held in the mat and conveyed to the bottom of the screen where they are removed in a reject chamber.
The United States patents 4,642,189 issued on February 10, 1987 discloses a rotary pressure screen of this type. The screen features an improved rotor construction allowing to increase the efficiency of the machine. More specifically, the upper section of the rotor has a parabolic shape and carries a frusto-conical baffle. The baffle and the upper section of the rotor define therebetween a first pulp stock passageway that has .: ..
a constant cross-sectional shape from top to bottom. A
second passageway is defined between the outer surface of the frusto-conical baffle and the screen basket. Pulp ,- :. :
stock to be screened discharged on top of the rotor is split in two parts that flow through respective passageways and are directed at different axial locations of the screen. As a result of this arrangement, the screen surface is utilized more efficiently. ~ ~;
The present invention is an improvement of this prior art rotary screening device. More particularly, the present inventor has made the surprising discovery that by re-configuring the pulp stock flow splitting baffle a significant gain in efficiency can be achieved.
-` 2108~98 As embodied and broadly described herein, the invention provides a rotary pulp screening device of the vertical pressure type, comprising:
- a housing defining an upper inlet chamber and a lower screening chamber in fluid communication;
- a generally cylindrical screen mounted in said lower screening chamber;
~ a rotor mounted for rotation about a generally vertical axis within said screen, said rotor having an upper section that tapers toward a top end of said rotor;
- a plurality of blades mounted to said rotor and radially extending therefrom to within a short distance from said screen, said blades constitute means for creating localized pressure pulsations in the pulp stock that act against said screen in order to dislodge impurities obturating apertures of said screen;
- a pulp flow splitting baffle having a generally circular configuration mounted to said rotor and encircling said upper section, said baffle and said rotor defining therebetween a first pulp f low passage having a gradually decreasing cross-sectional shape in a direction of pulp flow through said passage, said first pulp flow passage having an outlet opening through which pulp flow is discharged against said screen located at a point intermediate said top end and a bottom end of said rotor, said baffle and said screen defining therebetween a second pulp flow passage having a cross-sectional area 2108~98 substantially smaller than a cross-sectional area at an inlet end of said first passage, whereby pulp stock discharged in said inlet chamber enters said screening chamber and is split in two substantially unequal parts, a largest one of said parts flowing downward through said first passage toward said outlet opening, a sm~llest one of said parts flowing downward through said second passage along said screen and merging with pulp stock egressing from said outlet opening.
,:
The dramatic gain in efficiency observed with the screening device in accordance with the invention is a result of splitting the incoming flow of pulp stock to be screened in two substantially unequal parts, the large part flowing between the baffle and the upper section of the rotor and being discharged against the screen at an intermediate axial location thereof, while the smaller part flows between the outer surface of the baffle and the screen basket.
In a most preferred embodiment of the invention, the baffle is generally cylindrical maintaining from top to bottom a constant distance with the screen basket. The baffle is secured to the rotor by the intermediary of the blades provided to clear the screen openings. The blades are in the form of elongated vertical bars bolted to the lower cylindrical portion of the rotor. The upper part of --~ 2lns~ss the blades that extend at the level of the upper section of the rotor define a cage in which the baffle is received and supported. Since the blades extend over the outer surface of the baffle, there cleaning action is effective over the entire surface of the screen. This reduces the possibility of screen clogging and further proves the efficiency of the machine.
BRIEF DE8CRIPTION OF THE DRA~ING8 - Figure 1 is a schematical vertical cross-sectional view of a screening device of the pressure type in accordance with the invention;
15- Figure 2 is a top plan view of the screening device shown in Figure l; and - Figure 3 is a graphical representation of test data illustrating the efficiency of the screening device in 20accordance with the invention comparatively to a prior art machine.
.. .
, 25One embodiment of a pulp screening device 10 is shown in Figures 1 and 2 having a generally cylindrical housing 11 with a top cover 12 joined to the cylindrical housing --- 21085~8 11 at flange 13. In the cylindrical housing 11, spaced down from the top flange 13, is a disc ring 17 which divides the housing into an upper inlet chamber 18 above the disc ring 17, and a lower screening chamber 19 below the disc ring 17. A tubular inlet pipe 20 provides entry to the inlet chamber 18. Thus, pulp stock admitted in the inlet chamber 18 flows over the disc ring 17 and in the screening chamber 19.
A vertical cylindrical screen 25 is mounted axially in the lower chamber 19, and extends for the full height of the chamber 19. An annular accept chamber 26 which receives accepts completely surrounds the cylindrical screen 25. An outlet 27 at the bottom of the accept chamber 26 in the cylindrical housing 11, outside the screen 25, allows the screen accept fibers to leave the screening device 10.
A rotor 30 is positioned axially within the screen 25. In the embodiment shown, the rotor has an upper upwardly tapering portion 32 that is shaped approximately in the form of a paraboloid segment, and a lower cylindrical section 34. The paraboloid segment is formed from a series of truncated cones joined together and has a curved nose cone 36 on the top so the overall shape of the portion 20 is paraboloidal. The rotor 30 is mounted on a rotating axial shaft 38, which rotates in a bearing ' ~ ;
-' 2108~8 assembly . The drive shaft 34 has a V-belt pulley 41 mounted thereon for connection by means of V-belts to an electric drive motor (not shown in the drawings).
Five blades 40 are equi-spaced about the rotor 30.
Each blade 40 is a vertically extending bar bolted to the cylindrical section 34 of the rotor in a parallel relationship with the axis of rotation of the rotor 30.
The blade 40 extends for the full height of the screen 25.
The blades 40 form at the level of the paraboloidal upper segment of the rotor 30 a cage in which is fitted a pulp stock flow splitting baffle 42. The baffle is cylindrical in shape and has upper and lower edges lying in parallel horizontal planes. It is bolted to the blades 40 that support it on the rotor 30. The baffle 42 is positioned near the inlet end of the screening chamber 19 and provides two distinct passageways for the incoming flow of pulp stock. The first passageway 44 is defined between the baffle 42 and the paraboloidal segment of the rotor 30. It will be noted that this passageway has a gradually decreasing cross-sectional shape in the direction of flow of pulp stock therein which has the effect of gradually increasing the velocity of the pulp stock as the latter travels downwardly in the screening chamber 19. The passageway 44 terminates with an annular outlet 46 defined between the lower edge of the baffle 42 and the upper edge of the lcwer cylindrical segment 34 of the rotor.
~ , :' 2~ 08598 ~ :
A portion of the pulp stock entering the screening chamber 19 also flows through a second passageway 46 defined between the outer surface of the baffle 42 and the screen 25. The passage 46 has a uniform cross-sectional shape along its length as a result of the constant gap between the baffle 42 and the screen 25. It will be noted that the passage 46 is significantly smaller than the passage 44, particularly than the inlet end of the passage 44.
In operation, pulp stock delivered to the inlet chamber 18 passes over the disc ring 17 and flows in the screening chamber 19. The pulp stock is divided in two parts by the baffle 42. The predominant part flows in the passage 44 and it is gradually accelerated as it advances downwards. The pulp stock in the passageway 44 exits through the annular outlet 46 located at an intermediate point between the axial extremities of the screen 25.
Only at this point the pulp stock is in contact with the screen and it is subjected to a screening action while traveling downwards along the lower cylindrical portion 34 of the rotor.
The smaller part of the pulp stock delivered through the inlet of the screening shamber 19 flows through the small annular passage 46. Immediately upon entering this passage, the pulp stock is subjected to screening action.
g As it moves downwards along the screen 25, the pulp stock gradually thickens because water is removed at a high rate through the screen apertures. When the thickened pulp stock reaches the annular outlet 46, it is then diluted with the incoming main pulp flow stream and the screening action is then continued along the bottom portion of the screen 25.
As it is well known to those skilled in the art, the purpose of the blades 40 is to unplug the screen apertures. The rotation of the blades 40 causes local pressure pulsations in the pulp stock that act against the screen and are capable of dislodging large fibers or other debris obturating the screen apertures. By providing blades that extend vertically over the lower cylindrical section 34 of the rotor and over the entire axial length of- the baffle 42, enables to provide a cleaning action over the full surface of the screeb 25. As a result, the screen basket 25 can be maintained cleaner for a more efficient operation.
In a most preferred embodiment, the screen has an inside diameter of 29.375 inches. The cylindrical baffles defines with the screen 25 a gap of 1.125 inches measured at some point between two adjacent blades. The height of the rotor is of 40.250 inches, the axial dimension of the ; ~ ;`'6~ '^~ 6'Q~qi v~ 6 ~ ~ ~, s ~ ~ ;
~ 2108~8 baffle 42 is of 14 inches, and the axial dimension of the annular outlet 46 is of 2.8125 inches.
Comparative studies conducted with prior art rotary pulp screening devices have demonstrated the superiority in terms of efficiency of the present rotor design. Test runs conducted with a rotary screen constructed in accordance with the teaching of the above-identified U.S.
patent 4,642,189 and a system in accordance with the invention, have shown significant gains in efficiency in favour of the invention. The test data is represented graphically in Figure 3. It will be noted that for a given horse power value the screening device in accordance with the invention has a significantly higher pulp stock screening capacity than the prior art design.
It should be noted that the above description is not intended to be limiting as variations are possible without departing from the spirit of the invention. The scope of the invention is defined in the appended claims and their equivalents.
F~
FIELD OF THE I~YEM~ION
The present invention relates to an apparatus for removing impurities in pulp stock, more particularly to a novel rotary screening device that uses power more efficiently.
BACRGROUND OF THE INVENTION
The screening of wood pulp slurry is necessary in the production of paper to remove large fibers, stones and other rejects. Over the years, eguipment and processes to screen pulp have improved. Initially, pulp stock was passed through a vibrating screen, an improvement of this méthod was a cylindrical pulsating method where foils were rotated inside a screen to produce a pulsating effect on a mat of fibers adjacent the screen. The present method, and the one that is used in most modern paper mills, is the rotating method where fibers are screened in a cylindrical screen, generally a vertical screen. A series of blades rotate inside the screen and pulp slurry is fed to the top of the screen. As the slurry passes through the screen, the fibers are formed into a mat between the screen basket and the impeller blades. The mat rotates due to the movement of the impeller blades and at the same ~ 2108~98 time has an axial movement downwards so that the reject particles in the pulp stock are held in the mat and conveyed to the bottom of the screen where they are removed in a reject chamber.
The United States patents 4,642,189 issued on February 10, 1987 discloses a rotary pressure screen of this type. The screen features an improved rotor construction allowing to increase the efficiency of the machine. More specifically, the upper section of the rotor has a parabolic shape and carries a frusto-conical baffle. The baffle and the upper section of the rotor define therebetween a first pulp stock passageway that has .: ..
a constant cross-sectional shape from top to bottom. A
second passageway is defined between the outer surface of the frusto-conical baffle and the screen basket. Pulp ,- :. :
stock to be screened discharged on top of the rotor is split in two parts that flow through respective passageways and are directed at different axial locations of the screen. As a result of this arrangement, the screen surface is utilized more efficiently. ~ ~;
The present invention is an improvement of this prior art rotary screening device. More particularly, the present inventor has made the surprising discovery that by re-configuring the pulp stock flow splitting baffle a significant gain in efficiency can be achieved.
-` 2108~98 As embodied and broadly described herein, the invention provides a rotary pulp screening device of the vertical pressure type, comprising:
- a housing defining an upper inlet chamber and a lower screening chamber in fluid communication;
- a generally cylindrical screen mounted in said lower screening chamber;
~ a rotor mounted for rotation about a generally vertical axis within said screen, said rotor having an upper section that tapers toward a top end of said rotor;
- a plurality of blades mounted to said rotor and radially extending therefrom to within a short distance from said screen, said blades constitute means for creating localized pressure pulsations in the pulp stock that act against said screen in order to dislodge impurities obturating apertures of said screen;
- a pulp flow splitting baffle having a generally circular configuration mounted to said rotor and encircling said upper section, said baffle and said rotor defining therebetween a first pulp f low passage having a gradually decreasing cross-sectional shape in a direction of pulp flow through said passage, said first pulp flow passage having an outlet opening through which pulp flow is discharged against said screen located at a point intermediate said top end and a bottom end of said rotor, said baffle and said screen defining therebetween a second pulp flow passage having a cross-sectional area 2108~98 substantially smaller than a cross-sectional area at an inlet end of said first passage, whereby pulp stock discharged in said inlet chamber enters said screening chamber and is split in two substantially unequal parts, a largest one of said parts flowing downward through said first passage toward said outlet opening, a sm~llest one of said parts flowing downward through said second passage along said screen and merging with pulp stock egressing from said outlet opening.
,:
The dramatic gain in efficiency observed with the screening device in accordance with the invention is a result of splitting the incoming flow of pulp stock to be screened in two substantially unequal parts, the large part flowing between the baffle and the upper section of the rotor and being discharged against the screen at an intermediate axial location thereof, while the smaller part flows between the outer surface of the baffle and the screen basket.
In a most preferred embodiment of the invention, the baffle is generally cylindrical maintaining from top to bottom a constant distance with the screen basket. The baffle is secured to the rotor by the intermediary of the blades provided to clear the screen openings. The blades are in the form of elongated vertical bars bolted to the lower cylindrical portion of the rotor. The upper part of --~ 2lns~ss the blades that extend at the level of the upper section of the rotor define a cage in which the baffle is received and supported. Since the blades extend over the outer surface of the baffle, there cleaning action is effective over the entire surface of the screen. This reduces the possibility of screen clogging and further proves the efficiency of the machine.
BRIEF DE8CRIPTION OF THE DRA~ING8 - Figure 1 is a schematical vertical cross-sectional view of a screening device of the pressure type in accordance with the invention;
15- Figure 2 is a top plan view of the screening device shown in Figure l; and - Figure 3 is a graphical representation of test data illustrating the efficiency of the screening device in 20accordance with the invention comparatively to a prior art machine.
.. .
, 25One embodiment of a pulp screening device 10 is shown in Figures 1 and 2 having a generally cylindrical housing 11 with a top cover 12 joined to the cylindrical housing --- 21085~8 11 at flange 13. In the cylindrical housing 11, spaced down from the top flange 13, is a disc ring 17 which divides the housing into an upper inlet chamber 18 above the disc ring 17, and a lower screening chamber 19 below the disc ring 17. A tubular inlet pipe 20 provides entry to the inlet chamber 18. Thus, pulp stock admitted in the inlet chamber 18 flows over the disc ring 17 and in the screening chamber 19.
A vertical cylindrical screen 25 is mounted axially in the lower chamber 19, and extends for the full height of the chamber 19. An annular accept chamber 26 which receives accepts completely surrounds the cylindrical screen 25. An outlet 27 at the bottom of the accept chamber 26 in the cylindrical housing 11, outside the screen 25, allows the screen accept fibers to leave the screening device 10.
A rotor 30 is positioned axially within the screen 25. In the embodiment shown, the rotor has an upper upwardly tapering portion 32 that is shaped approximately in the form of a paraboloid segment, and a lower cylindrical section 34. The paraboloid segment is formed from a series of truncated cones joined together and has a curved nose cone 36 on the top so the overall shape of the portion 20 is paraboloidal. The rotor 30 is mounted on a rotating axial shaft 38, which rotates in a bearing ' ~ ;
-' 2108~8 assembly . The drive shaft 34 has a V-belt pulley 41 mounted thereon for connection by means of V-belts to an electric drive motor (not shown in the drawings).
Five blades 40 are equi-spaced about the rotor 30.
Each blade 40 is a vertically extending bar bolted to the cylindrical section 34 of the rotor in a parallel relationship with the axis of rotation of the rotor 30.
The blade 40 extends for the full height of the screen 25.
The blades 40 form at the level of the paraboloidal upper segment of the rotor 30 a cage in which is fitted a pulp stock flow splitting baffle 42. The baffle is cylindrical in shape and has upper and lower edges lying in parallel horizontal planes. It is bolted to the blades 40 that support it on the rotor 30. The baffle 42 is positioned near the inlet end of the screening chamber 19 and provides two distinct passageways for the incoming flow of pulp stock. The first passageway 44 is defined between the baffle 42 and the paraboloidal segment of the rotor 30. It will be noted that this passageway has a gradually decreasing cross-sectional shape in the direction of flow of pulp stock therein which has the effect of gradually increasing the velocity of the pulp stock as the latter travels downwardly in the screening chamber 19. The passageway 44 terminates with an annular outlet 46 defined between the lower edge of the baffle 42 and the upper edge of the lcwer cylindrical segment 34 of the rotor.
~ , :' 2~ 08598 ~ :
A portion of the pulp stock entering the screening chamber 19 also flows through a second passageway 46 defined between the outer surface of the baffle 42 and the screen 25. The passage 46 has a uniform cross-sectional shape along its length as a result of the constant gap between the baffle 42 and the screen 25. It will be noted that the passage 46 is significantly smaller than the passage 44, particularly than the inlet end of the passage 44.
In operation, pulp stock delivered to the inlet chamber 18 passes over the disc ring 17 and flows in the screening chamber 19. The pulp stock is divided in two parts by the baffle 42. The predominant part flows in the passage 44 and it is gradually accelerated as it advances downwards. The pulp stock in the passageway 44 exits through the annular outlet 46 located at an intermediate point between the axial extremities of the screen 25.
Only at this point the pulp stock is in contact with the screen and it is subjected to a screening action while traveling downwards along the lower cylindrical portion 34 of the rotor.
The smaller part of the pulp stock delivered through the inlet of the screening shamber 19 flows through the small annular passage 46. Immediately upon entering this passage, the pulp stock is subjected to screening action.
g As it moves downwards along the screen 25, the pulp stock gradually thickens because water is removed at a high rate through the screen apertures. When the thickened pulp stock reaches the annular outlet 46, it is then diluted with the incoming main pulp flow stream and the screening action is then continued along the bottom portion of the screen 25.
As it is well known to those skilled in the art, the purpose of the blades 40 is to unplug the screen apertures. The rotation of the blades 40 causes local pressure pulsations in the pulp stock that act against the screen and are capable of dislodging large fibers or other debris obturating the screen apertures. By providing blades that extend vertically over the lower cylindrical section 34 of the rotor and over the entire axial length of- the baffle 42, enables to provide a cleaning action over the full surface of the screeb 25. As a result, the screen basket 25 can be maintained cleaner for a more efficient operation.
In a most preferred embodiment, the screen has an inside diameter of 29.375 inches. The cylindrical baffles defines with the screen 25 a gap of 1.125 inches measured at some point between two adjacent blades. The height of the rotor is of 40.250 inches, the axial dimension of the ; ~ ;`'6~ '^~ 6'Q~qi v~ 6 ~ ~ ~, s ~ ~ ;
~ 2108~8 baffle 42 is of 14 inches, and the axial dimension of the annular outlet 46 is of 2.8125 inches.
Comparative studies conducted with prior art rotary pulp screening devices have demonstrated the superiority in terms of efficiency of the present rotor design. Test runs conducted with a rotary screen constructed in accordance with the teaching of the above-identified U.S.
patent 4,642,189 and a system in accordance with the invention, have shown significant gains in efficiency in favour of the invention. The test data is represented graphically in Figure 3. It will be noted that for a given horse power value the screening device in accordance with the invention has a significantly higher pulp stock screening capacity than the prior art design.
It should be noted that the above description is not intended to be limiting as variations are possible without departing from the spirit of the invention. The scope of the invention is defined in the appended claims and their equivalents.
F~
Claims (5)
1. A rotary pulp screening device of the vertical pressure type, comprising:
- a housing defining an upper inlet chamber and a lower screening chamber in fluid communication;
- a generally cylindrical screen mounted in said lower screening chamber;
- a rotor mounted for rotation about a generally vertical axis within said screen, said rotor having an upper section that tapers toward a top end of said rotor;
- a plurality of blades mounted to said rotor and radially extending therefrom to within a short distance from said screen, said blades constitute means for creating localized pressure pulsations in the pulp stock that act against said screen in order to dislodge impurities obturating apertures of said screen;
- a pulp flow splitting baffle having a generally circular configuration mounted to said rotor and encircling said upper section, said baffle and said rotor defining therebetween a first pulp flow passage having a gradually decreasing cross-sectional shape in a direction of pulp flow through said passage, said first pulp flow passage having an outlet opening through which pulp flow is discharged against said screen located at a point intermediate said top end an a bottom end of said rotor, said baffle and said screen defining therebetween a second pulp flow passage having a cross-sectional area substantially smaller than a cross-sectional area at an inlet end of said first passage, whereby pulp stock discharged in said inlet chamber enters said screening chamber and is split in two substantially unequal parts, a largest one of said parts flowing downward through said first passage toward said outlet opening, a smallest one of said parts flowing downward through said second passage along said screen and merging with pulp stock egressing from said outlet opening.
- a housing defining an upper inlet chamber and a lower screening chamber in fluid communication;
- a generally cylindrical screen mounted in said lower screening chamber;
- a rotor mounted for rotation about a generally vertical axis within said screen, said rotor having an upper section that tapers toward a top end of said rotor;
- a plurality of blades mounted to said rotor and radially extending therefrom to within a short distance from said screen, said blades constitute means for creating localized pressure pulsations in the pulp stock that act against said screen in order to dislodge impurities obturating apertures of said screen;
- a pulp flow splitting baffle having a generally circular configuration mounted to said rotor and encircling said upper section, said baffle and said rotor defining therebetween a first pulp flow passage having a gradually decreasing cross-sectional shape in a direction of pulp flow through said passage, said first pulp flow passage having an outlet opening through which pulp flow is discharged against said screen located at a point intermediate said top end an a bottom end of said rotor, said baffle and said screen defining therebetween a second pulp flow passage having a cross-sectional area substantially smaller than a cross-sectional area at an inlet end of said first passage, whereby pulp stock discharged in said inlet chamber enters said screening chamber and is split in two substantially unequal parts, a largest one of said parts flowing downward through said first passage toward said outlet opening, a smallest one of said parts flowing downward through said second passage along said screen and merging with pulp stock egressing from said outlet opening.
2. A rotary pulp screening device as defined in claim 1, wherein said baffle is generally cylindrical.
3. A rotary pulp screening device as defined in claim wherein said impeller blades extend generally vertically over an outer surface of said baffle.
4. A rotary pulp screening device as defined in claim 1, wherein said impeller blades extend generally vertically and are secured to a lower section of said rotor, upper portions of said blades extending at a level of said upper section define a cage receiving and supporting said baffle.
5. A rotary pulp screening device as defined in claim 1, wherein said upper section is generally parabolic.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA 2108598 CA2108598A1 (en) | 1993-10-18 | 1993-10-18 | Rotary screening device |
| AU78513/94A AU7851394A (en) | 1993-10-18 | 1994-10-18 | Rotary screening device |
| PCT/CA1994/000579 WO1995011336A1 (en) | 1993-10-18 | 1994-10-18 | Rotary screening device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA 2108598 CA2108598A1 (en) | 1993-10-18 | 1993-10-18 | Rotary screening device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2108598A1 true CA2108598A1 (en) | 1995-04-19 |
Family
ID=4152458
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA 2108598 Abandoned CA2108598A1 (en) | 1993-10-18 | 1993-10-18 | Rotary screening device |
Country Status (3)
| Country | Link |
|---|---|
| AU (1) | AU7851394A (en) |
| CA (1) | CA2108598A1 (en) |
| WO (1) | WO1995011336A1 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SE511786C2 (en) * | 1998-03-06 | 1999-11-22 | Sunds Defibrator Ind Ab | Screening device with two screening chambers for separating fiber suspensions |
| JP3435346B2 (en) * | 1998-04-16 | 2003-08-11 | 相川鉄工株式会社 | Screen device |
| SE9901148L (en) | 1999-03-29 | 2000-06-12 | Valmet Fibertech Ab | Screening device with a rotatable and stationary screen means |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4642189A (en) * | 1983-12-12 | 1987-02-10 | Uniweld Inc. | Rotary screen of the vertical pressure type having pulp stock feed at different axial positions on the screen |
| US4744894A (en) * | 1986-06-30 | 1988-05-17 | Gauld W Thomas | Fibrous stock screening apparatus |
-
1993
- 1993-10-18 CA CA 2108598 patent/CA2108598A1/en not_active Abandoned
-
1994
- 1994-10-18 AU AU78513/94A patent/AU7851394A/en not_active Abandoned
- 1994-10-18 WO PCT/CA1994/000579 patent/WO1995011336A1/en active Application Filing
Also Published As
| Publication number | Publication date |
|---|---|
| AU7851394A (en) | 1995-05-08 |
| WO1995011336A1 (en) | 1995-04-27 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FZDE | Dead |