[0001] The present application is a Continuation-in-Part of U.S. Serial No. 738,743 filed
on May 29, 1985 in the name of Harry Lampenius and Frey Frejborg. U.S. Serial No.
738,743 is the Continuation-in-Part of U.S. Serial No. 472,742, which was issued as
U.S.P. 4,529,520. The subject matter of U.S. Serial Nos. 472,742 and 738,743 is incorporated
herein by reference.
[0002] The present application relates generally to apparatuses for screening fiber suspensions
of consistency between 0.3% up to 6%, and in particular, to a screening apparatus
for screening papermaking pulp containing wood portions and other undesirable particles
of various sizes and types.
[0003] In U.S. Serial No. 738,743, a pulp screening apparatus is described which comprises
a vessel, a cylindrical screen within the vessel, a rotating element moving in the
vicinity of the screen at a predetermined speed, an inlet for the unscreened pulp,
an outlet for the accept screened pulp in the vessel, another outlet for the reject,
in operative communication with the screen. The rotating element has a contour surface
with grooves formed of a first bottom plane parallel to the envelope surface of the
screen, an inclined plane and a side plane. The side plane is essentially perpendicular
to the first bottom plane. The inclined plane forms an angle between 30° - 60° with
the first plane. The upper plane is parallel to the first plane. The screen is also
provided with grooves.
[0004] In the paper making process, pulp is produced by cooking wood which separates the
wood into fibers. Due to the different properties of the wood even from the same tree,
some of the fibers do not separate and are dispersed as fiber bundles usually called
debris, shives or slivers which form the reject. There are also other impurities,
such as bark, which must be removed. The screen must separate the undesirable impurities
and debris called the rejects from the accept portion. In order to avoid substantial
losses of fibers which could be carried over together with the debris in the reject
portion, it is necessary to remove the impurities efficiently and selectively.
[0005] It should be stressed that different applications have different requirements. In
some applications, it is necessary to achieve a high content of long fibers, especially
secondary fibers, in the accepts because the long fibers give strength to the final
product, for instance paper. In other applications, on the other hand, the contrary
is true. For instance, in virgin or pulp mill fibers, it is desirable to concentrate
the long fibers in the reject for reject refining.
[0006] In some applications, it is preferable to operate the screen under smoother flow
conditions while in other applications, it is advantageous to operate the screen under
more turbulent conditions.
[0007] In pulp screening apparatus having a screen member and a rotor which form an annular
screening zone, the stock enters at the inlet end of the screening zone and travels
in an angle along the screening surface with the acceptable portions of the stock
passing through the screening surface and with the rejectable portions of the pulp
traveling along the screening surface essentially in a spiral path and passing out
of the screening zone at the reject end. During the screening process, the liquid
that accompanies the fibrous stock passes through the screening surface more easily
than the fibers. Therefore, as the stock travels along the screening zone, it tends
to crease in consistency which means that the fiber-to-water ratio is increased. If
this ratio increases too much, the screening process will be slowed down or will be
even interrupted. In order to prevent this slow-down or interruption, it has been
common practice to add more water to the stock to replace some of the water which
has passed through the screening surface so as to maintain a satisfactory screening
consistency on the inlet side.
[0008] Another method used to maintain the screening consistency on the inlet side is to
intentionally feed the apparatus with over-diluted stock so that the excess water
at the inlet will be sufficient to allow for continuity of screening throughout the
screening zone. However, both methods of adding more water during the screening or
initially over-diluting the stock have undesirable effects such as diminishing the
capacity of the screen by the amount of water added.
[0009] Many proposals have been made to solve the problems discussed hereinabove. In Swedish
Patent 37 4148 to S.E.E. Ahlfors published in 1975 the apparatus comprises a pressure
screen having a coarse screening drum and a fine screening drum, the former surrounding
the latter and provided with pulse generating means and perforations on the back side
of or immediately behind the pulse generating means. This apparatus has the drawback
that it cannot be readily used in an existing housing as a retrofit and would be very
expensive since two motors are required to rotate the two drums, one independently
from the other.
[0010] In Finnish Patent 66218 to Sunds Defibrator Aktiebolag, published in 1979, a screen
apparatus is described in which a rotating coarse screening drum and a fine screening
drum, are provided. The former is provided with pumping means to remove by suction,
impurities which have plugged the openings of the fine screening drum. This proposal
which involves coarse screening and fine screening has met only with parial success
because of high manufacturing cost and low general performance. Further, due to the
size and operational conditions of the pumping pipes, this apparatus cannot be readily
used in a conventional housing as a retrofit.
[0011] The apparatus of Finnish Patent 66218 is also described in Tappi Journal, September,
1986, page 27, and in Tappi Proceedings, (1986) Engineering Conference, pp. 585-587.
[0012] Pulps of different consistencies require screens with different contours. Different
contours are also required with pulp suspensions having different physical properties
and for different applications.
[0013] An object of the present invention is to separate the long fibers from slives and
debris efficiently and selectively.
[0014] Another object is to provide a screening apparatus which may be operated under smooth
flow as well as under more turbulent flow conditions.
[0015] Still another object is to maintain the desired screening efficiency without adding
water during the screening operation and without using initially an overly diluted
stock.
[0016] A further object is to provide a screening apparatus which can operate at pulp feed
consistencies between 0.3% up to 6%.
[0017] Still another object is to provide a rotor which may be used with a variety of contoured
screens, for a variety of pulp suspensions, which may provide the pumping effect required
with the low consistency suspensions and which may provide the turbulence required
for higher consistency stocks.
[0018] To achieve the above objects, the screening apparatus according to the invention
comprises a housing having an inlet for allowing fibrous stock to be introduced into
the interior of the housing, an outlet for allowing the accepted screened stock to
be removed from the housing, an outlet for the reject, a contoured screen within the
housing, a rotor moving in the vicinity of the screen at a predetermined speed and
forming together with the screen an annular screening chamber, the rotor having at
least one partially contoured surface on the side facing screen and provided with
a plurality of perforations along at least a portion of the length of the screening
chamber to allow fibrous stock to be introduced into the screening chamber and to
prevent the undesired debris of the stock from entering the chamber.
[0019] Other objects and features of the present invention will be apparent from the following
description taken in conjunction with the appended drawings, of which:
Fig. 1 is a side elevation view, partly broken away, of a screening apparatus according
to the invention.
Fig. 2 illustrates the embodiment of the screening apparatus according to the present
invention and specifically with the rotor being located on the inlet side of the screen.
The rotor is always disposed on the inlet side of the screen but the apparatus may
be operated in an outflow or inflow manner. In the outflow manner of Fig. 2 the pulp
flows from the inside to the outside of the screen and the contoured surface of the
screen is on the inside of the screen.
Figs. 3,4,5,6,7 and 8 illustrate screenplates which may be used together with the
rotor according to the present invention.
Fig. 9 illustrates an apparatus intended for inflow configuration.
[0020] In the embodiment of Fig. 9, the pulp flows from the outside to the inside of the
screen and the contoured surface of the screen is on the outside of the screen.
[0021] As illustrated in Figs. 1 and 2 the screening apparatus includes a pressurized housing
1, a cylindrical screen 3 positioned within the housing, a rotor 4 mounted within
the screen on the upper part of a rotatable, veritcal shaft 5. The housing has an
inlet 6 for allowing unscreened pulp suspension to be introduced into a chamber 7
in the upper part of the housing, an outlet 8 for accepted (screened) stock, a reject
chamber 19 and an outlet 9 for rejected stock in the lower end. A screening chamber
12 is formed between the cylindrical screen and the rotor. Numeral 15 designates the
accept chamber.
[0022] Numeral 2 designates a removable cover for the housing and numeral 11 designates
a plate closing the upper end of the screening chamber. A flange 14 in the upper end
of the cylindrical screen by means of which the screen member is fixed to the structure
10 and the structure 10 form a partition between the first chamber 7 in the upper
part of the housing which is the infeed chamber and a second chamber 15 which is the
accept chamber. The latter is formed between the vertical walls 16 of the housing
and the cylindrical screen which second chamber surrounds the cylindrical screen.
The housing includes an additional structure 17 which, together with a flange 18,
forms a partition between the second chamber and a third chamber 19 which is the reject
chamber in the bottom part of the housing. The stock inlet 6 communicates directly
with the first chamber, the accept outlet 8 communicates directly with the second
chamber and the reject outlet 9 communicates directly with the third chamber.
[0023] Essentially, axial bars or foils 20 which extend along at least a portion of the
length of the rotor are mounted on a support adjacent the inner surface of the rotor.
A plate 21 closes the lower end of the rotor. Openings 22 in the lower end of the
rotor drum 23 provide communication between the space inside the rotor and the reject
chamber.
[0024] The screen plate 3 has a contoured surface. According to one embodiment, shown in
Fig. 2, the cylindrical screen plate has grooves 24 in the inlet surface. Also the
outside and the inside surfaces of the rotor are contoured with grooves 25 and 26,
but the rotor could have only one contour surface facing the screen. The contour surface
is not necessarily continuous.
[0025] The grooves 25 on the screen side of the rotor are formed of a bottom plane 27 and
two side planes 28 and 29. The grooves 26 on the inlet side of the rotor are likewise
formed by a bottom plane 30 and two side planes 31 and 32.
[0026] The bottom planes 27 and 30 are generally perpendicular to the side planes 32 and
29. The side planes 28 and 31 are generally inclined with respect to the cylindrical
outer and inner surfaces. The angle α is formed between upper plane 33 and the inclined
plane 28 and is in this embodiment between 5° and 60°. The angle β is formed between
the envelope surface 34 and side plane 31 and is between 10° and 60°.
[0027] The symbol H₁ designates the distance between the bottom plane 27 and the upper plane
33 in the outer surface of the rotor and may be between 1/16 inch and 2 inches. The
symbol H₂ designates the distance between the bottom plane 30 and the envelope surface
34 in the inlet side of the rotor and may be between 1/16 inch and 2 inches. The symbols
B₁ and B₂ designate the width of the bottom planes 27 and 30 in the outer and inner
surface respectively of the rotor and may be as low as 1/8 inch and as long as 2 inches.
[0028] The rotor 23 has a plurality of perforations 35 extending along a portion (L in Fig.
1) of its axial length beginning from its upper end and a size allowing fibrous stock
to pass through the rotor but preventing foreign objects of larger size than the inlet
openings 36 of the perforations from entering the screening zone 12. The inlet openings
of the perforations are positioned in the bottom plane of the grooves 26 on the inlet
side of the rotor and the discharge openings 37 are positioned either on the upper
plane 33 of the outlet surface of the rotor or on the inclined plane 28 or on the
bottom plane 27.
[0029] The perforations in the rotor are either cylindrical or preferably slotted in section.
The discharge opening of the perforations is preferably larger than the inlet opening.
[0030] The grooves as well as the perforations of the rotor are larger than the grooves
and the perforations of the screen in the embodiment of Fig. 2 but this in not essential.
The rotor may also be constructed of profiled bars which, when assembled, form longitudinal
openings therebetween which then constitute the perforations of the rotor. The profiled
bars may be represented by the dotted lines drawn through the openings of the rotor
as shown in Fig. 2.
[0031] The inclined side plane on each surface of the rotor can be the leading side plane
or the trailing plane of the groove in relation to the direction of the rotation of
the rotor in the embodiment of Fig. 2.
[0032] The rotor may rotate in different directions, that is, clockwise as shown in Fig.
2, for high efficiency, or counterclockwise to achieve high capacity.
[0033] The grooves 25 and 26 may be located in relation to each other as shown in Fig. 2,
that is the inclined planes being the downflow sides of the grooves. However, either
or both of the grooves 25 and 26 may be formed so that the perpendicular planes 29,
32 are the downflow sides of the grooves. It is also possible that the grooves are
so formed that every second groove has as its downflow side the inclined plane and
the others have the perpendicular plane. Also it is possible to arrange the grooves
in groups so that a certain group of grooves has as its downflow side the inclined
planes and the next group of grooves the perpendicular planes.
[0034] In the outflow operation shown in Figs. 1 and 2, pulp suspension is supplied to the
first chamber 7 in the upper end of the apparatus through inlet 6 and flows into the
rotor 4. The fibrous stock flows through the perforations in the rotor to the screening
chamber and particles larger than the perforations will not pass through the perforations
of the rotor. The large cross-sectional area of the rotor allows heavy foreign material
to settle for rejection through the openings 22 at the lower end of the rotor and
allows the pulp suspension to flow in an almost radial direction towards the inner
surface of the rotor. Due to the interaction between the rotating grooved surface
of the rotor and the pulp suspension which is prevented from rotating by the essentially
axial flow interruptors 20, high-intensity pulses and turbulence are generated which
prevent a mat of fibers from forming at the openings in the grooves 26. By adjusting
the position and the inclination of the flow interruptors in relation to the grooved
surface, the intensity of the pulses and the turbulence can be varied. If required,
dilution water could be directed through the flow interruptors toward the grooved
surface in the lower part of the rotor.
[0035] The stock which enters the screening chamber is set into circumferential motion by
the rotor and subjected to high-intensity pulses and turbulence when flowing over
essentially in a direction perpendicular to the grooves on the screen surface. The
angle between the direction of the grooves and the axial direction of the cylinder
of the screen plate may be from 0° to 45°. The acceptable fibers pass through the
perforations in the screen to be collected in the chamber 15 surrounding the screen
and are removed through the outlet 8 as accepted stock. Any stock not passing through
the perforations of the rotor or the screen is collected in the chamber 19 in the
lower end of the housing and is discharged through the outlet 9 as rejects.
[0036] The screening chamber 12 between the rotor and the screen can be as narrow as 1 mm
and as large as 50 mm.
[0037] When the screening chamber is narrow, between 1 and 3 mm, an effective hydrodynamic
interaction between the grooved surfaces of the rotor and the screen facing each other
is achieved, and advantageous conditions for the screening are provided. This also
permits the screen to efficiently handle stock of high consistency, up to 6%.
[0038] In the embodiments of Figs. 3 and 4, the groove in the screen is formed of a bottom
plane 40 which is substantially parallel with the envelope surface 42 of the screen
surface, an upstream side plane 44 as seen standing from the bottom of the groove
and a downstream side plane 45. In Fig. 3, the angle α between the envelope surface
of the screen surface and the upstream side plane 44, or in other words between the
plane tangenting the envelope surface of the screen surface close to this side plane
and this side plane is approximately 90° and the angle β between the envelope surface
of the screen surface and the downstream side plane 45 is 5° - 60°. In Fig. 4 the
angle is α 5° - 60° and the angle β is 90°. The perforations of the screen plate are
disposed on the bottom planes 40 of the grooves.
[0039] In the embodiment illustrated in Fig. 5, the grooves 52 are U-shaped, and both side
planes 44 and 45 are substantially perpendicular to the envelope surface 42 of the
screen surface.
[0040] In the embodiment of Fig. 6, the screen surface is undulant and both sides 44 and
45 of the grooves 52 are inclined with regard to the envelope surface 42 of the screen
surface.
[0041] The surface of the rotor which does not face the screen is not necessarily grooved
and it is not necessary that the entire surface of the rotor be grooved.
[0042] The inlet side of the rotor also may have a contour surface, for instance, the contour
of the screen as shown in Figs. 3-8.
Example I:
[0043] This example describes a typical screening apparatus with a cylindrical rotor having
an outer diameter of 20 inches and a thickness of 3/8 inch.
Depth (H₁ and H₂) of grooves of the rotor: 1/8 inch
Width (B₁ and B₂) of bottom plane: 3/16 inch
Angle (α and β ) 50°
Width of axial slots (36): 1/16 inch
Circumferential spacing of grooves, that is the distance between consecutive grooves
26: 0.5 inch
Width (W) of the screening chamber: 3/16 inch
[0044] In the embodiment of Fig. 7, in the screen, the grooves have two side planes, a bottom
plane and an upper plane, one side plane is perpendicular to the envelope surface
of the screen and the other side plane is curved, convex or concave with respect to
the envelope surface.
[0045] In Fig. 8 the sides of the grooves have an inverted V-shape configuration.
[0046] Although Figs. 1 and 2 show an apparatus intended for outflow operation, the apparatus
according to Fig. 9 may be readily adapted for inflow configuration according to which
the pulp is fed into the outer surface of the rotor, goes through the perforations
inwardly, flows into the screening chamber. Thereafter the accept portion passes through
the finer perforations of the screen into the accept chamber and the remaining reject
portion in the screening chamber moves towards the reject chamber. This operation
is particularly advantageous when large dirt type particles are to be removed.
[0047] Another advantage of the apparatus according to the present invention is that it
may be retrofitted and used with conventional screen housings, resulting in major
capital savings.
1. A pulp screening apparatus comprising a housing (1) having an inlet (6) for allowing
fibrous stock to be introduced into the interior thereof, a first outlet (8) for allowing
the accept screened stock to be removed therefrom, a second outlet (9) for the reject,
a screen (3) having a contour surface within said housing (1), a rotor (4) moving
in the vicinity of said screen (3) at a predetermined speed and forming together with
said screen (3) an annular screening chamber (12), said rotor (4) having at least
the surface facing the screen (3) partially contoured and being provided with a plurality
of perforations (35) along at least a portion of the length of said screening chamber
(12) to allow fibrous stock to be introduced into said screening chamber (12) and
prevent the undesired debris of the stock from entering said chamber (12).
2. The apparatus according to claim 1, wherein said contoured surface of the rotor
(4) consists of grooves (25; 26), the rotor (4) has an inlet side surface and an outlet
side surface and both surfaces of said rotor (4) are grooved (25; 26).
3. The apparatus according to claim 1, wherein the said contoured surface of the rotor
(4) consists of grooves (25; 26) said grooves (25; 26) having a bottom plane (27;
30) and two side planes (28, 29; 31, 32) of which one is inclined and the other is
perpendicular to the bottom plane (27; 30), said inclined plane forming an angle with
the bottom plane (27; 30) between 5° and 60°.
4. The apparatus according to claim 3, wherein said contoured surface of the rotor
(4) consists of grooves (25; 26), said grooves (25; 26) have an upper plane (33; 34),
a bottom plane (27; 30) and two side planes (28, 29; 31, 32), one side plane is inclined
and the other side plane is perpendicular to the bottom plane (27; 30), said inclined
plane forming an angle with the bottom plane (27; 30) between 5° and 60°.
5. The apparatus according to claim 3, wherein the grooves (25; 26) of the rotor (4)
have an upstream side and a downstream side, the downstream side of the grooves (25;
26) of the rotor (4) is inclined against the surface of the rotor (4) and the upstream
side is essentially perpendicular to the surface of the rotor (4).
6. The apparatus according to claim 3 wherein the grooves (25; 26) of the rotor (4)
have an upstream side and a downstream side, the downstream side plane of the grooves
(25; 26) of the rotor (4) is essentially perpendicular to the bottom plane (27; 30)
and the upstream side is inclined against the surface of the rotor (4).
7. The apparatus according to claim 2, wherein the rotor (4) has grooves (25; 26)
on both surfaces, the perforations (35) have an inlet (36) and the inlet (36) of the
perforations (35) is disposed in the bottom part (30) of the grooves (26) of the rotor
(4) inlet side.
8. The apparatus according the claim 3, wherein the perforations (35) have an outlet
(37) and the outlet (37) is disposed in the inclined plane of the grooves (25) of
the rotor (4) outlet side.
9. The apparatus according to claim 3, wherein the perforations (35) have an outlet
(37) disposed in the upper plane (33) of the grooves (25) of the rotor (4) outlet
side.
10. The apparatus according to claim 3, wherein the perforations (35) have an outlet
(37) disposed in the bottom plane (27) of the grooves (25) of the rotor (4) outlet
side.
11. The apparatus according to claim 1, wherein the rotor (4) is disposed within the
screen (3).
12. The apparatus according to claim 1, wherein the rotor (4) inner surface faces
the outer surface of the screen (3).
13. The apparatus according to claim 1, wherein said rotor (4) is cylindrical.
14. The apparatus according to claim 1, wherein said rotor (4) is non-cylindrical.
15. The apparatus according to claim 1, wherein the perforations (35) in the rotor
(4) are cylindrical.
16. The apparatus according to claim 1, wherein the perforations (35) in the rotor
(4) are non-cylindrical.
17. The apparatus according to claim 2, wherein the contoured surface of the screen
(3) consists of grooves (24) with perforations, the grooves (25; 26) and the perforations
(35) of the rotor (4) are larger than the grooves and perforations of the screen (3).
18. The apparatus according to claim 1, wherein the screen (3) is a cylindrical screenplate
having grooves (24, 52) with perforations, the perforations are at the bottom of the
grooves (24, 52), the bottom plane (40) of the grooves is parallel to the envelope
surface (42), the grooves (24, 52) have two side planes (44; 45), one side plane of
the grooves (24, 52) is substantially perpendicular to the envelope surface (42) of
the screen surface and the other side plane is inclined with regard to said envelope
surface (42).
19. The apparatus according to claim 18, wherein said screen plate (3) has grooves
(24, 52) in the side of the inlet recessed in the screen surface, the screen plate
(3) having an envelope surface (42), the grooves (24, 52) being formed of an upstream
side plane (44), as seen standing from the bottom of the grooves (24, 52), a downstream
side plane (45) and a bottom plane (40), said bottom plane (40) being substantially
parallel to the envelope surface (42) of the screen plate (3), the grooves (24, 52)
having perforations in the bottom plane (40), the upstream side plane (44) of the
grooves (24, 52) being substantially perpendicular to said envelope surface (42) and
the downstream side plane (45) of the grooves (24, 52) forming a 60° - 5° angle against
said envelope surface (42).
20. The apparatus according to claim 19, wherein in said screen plate (3) the downstream
side plane (45) and the upstream side plane (44) of the grooves (24, 52) are connected
to each other by means of a plane substantially parallel to said envelope surface
(42).
21. The apparatus according to claim 11, wherein said screen (3) has an inlet side
and an outlet side, said rotor (4) is located on the inlet side of said screen (3);
the contoured surface of the screen (3) is on the inside of the screen (3).
22. The apparatus according to claim 12, wherein said screen (3) has an inlet side
and an outlet side, the rotor (4) is located on the inlet side of the screen (3) and
the contoured surface of the screen (3) is on the outside of the screen (3).
23. The apparatus according to claim 18, wherein the downstream side plane (45) of
the grooves (24, 52) is substantially perpendicular to the envelope surface (42) of
the screen surface and the upstream side plane (44) is inclined.
24. The apparatus according to claim 1, wherein the contoured surface of the screen
(3) consists of grooves (24, 52) and both side planes (44; 45) of the grooves (24,
52) are substantially perpendicular to the envelope surface (42) of the screen (3).
25. The apparatus according to claim 1, wherein the screen (3) is a cylindrical screenplate
having grooves (24, 52), the perforations are at the bottom of the grooves (24, 52),
the bottom plane (40) of the grooves (24, 52) is parallel to the envelope surface
(42), the grooves (24, 52) have two side planes (44; 45) and an upper plane, one side
plane of the grooves (24, 52) is substantially perpendicular to the envelope surface
(42) of the screen (3) and the other side plane is curved with regard to said envelope
surface (42).
26. The apparatus according to claim 25, wherein said side plane is convex or concave
with respect to said envelope surface (42).
27. The apparatus according to claim 1, wherein the screen surface is undulant, the
screen (3) has grooves (24, 52) and both sides of the grooves (24, 52) are inclined
with respect to the envelope surface (42).
28. The apparatus according to claim 1, wherein said contoured surface of the rotor
(4) is formed by spaced contoured bars (20).