US2375826A - Vortex separator apparatus for treating paper pulp - Google Patents

Vortex separator apparatus for treating paper pulp Download PDF

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Publication number
US2375826A
US2375826A US346781A US34678140A US2375826A US 2375826 A US2375826 A US 2375826A US 346781 A US346781 A US 346781A US 34678140 A US34678140 A US 34678140A US 2375826 A US2375826 A US 2375826A
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Prior art keywords
vessel
pulp
vortex
pipe
inlet
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Expired - Lifetime
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US346781A
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English (en)
Inventor
Scott Harold Eric Baliol
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Vickerys Ltd
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Vickerys Ltd
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00—Apparatus in which the axial direction of the vortex is reversed
    • B04C5/12—Construction of the overflow ducting, e.g. diffusing or spiral exits
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00—Apparatus in which the axial direction of the vortex is reversed
    • B04C5/08—Vortex chamber constructions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00—Apparatus in which the axial direction of the vortex is reversed
    • B04C5/08—Vortex chamber constructions
    • B04C5/103—Bodies or members, e.g. bulkheads, guides, in the vortex chamber
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00—Apparatus in which the axial direction of the vortex is reversed
    • B04C5/12—Construction of the overflow ducting, e.g. diffusing or spiral exits
    • B04C5/13—Construction of the overflow ducting, e.g. diffusing or spiral exits formed as a vortex finder and extending into the vortex chamber; Discharge from vortex finder otherwise than at the top of the cyclone; Devices for controlling the overflow
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00—Apparatus in which the axial direction of the vortex is reversed
    • B04C5/14—Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00—Apparatus in which the axial direction of the vortex is reversed
    • B04C5/14—Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations
    • B04C5/15—Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations with swinging flaps or revolving sluices; Sluices; Check-valves
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00—Apparatus in which the axial direction of the vortex is reversed
    • B04C5/24—Multiple arrangement thereof
    • B04C5/26—Multiple arrangement thereof for series flow
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C9/00—Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks

Definitions

  • the principal objects of this invention are to adapt separators of this type to operate under difierent conditions; to perfect the separation of impurities and achieve the maximum economy of useful pulp in circumstances which justify additional expense to those ends; and to simplify the construction of the separator.
  • the bafiie which divides the sheltered settling chamber from the vortex chamber is supported at the top of a pipe which opens laterally beneath it, and which can serve to carry a stream of impurity-laden liquid out of the sheltered chamber.
  • the bafiie has a skirt which adds to the length of the constricted annular passage by which separated impurities pass from the vortex chamber to the settling chamber; but for the purpose of this invention the skirt is divided from the bafile proper which lies across the separator so that it is possible for pulp to pass from within the skirt around the edge of the bailie.
  • the advantage of withdrawing a stream of pulp from the settling chamber and thereby facilitating and encouraging the flow of heavy impurities into that chamber is already known; the above described construction enables pulp to be so withdrawn and also enables the apparatus to operate when the pipe beneath its baflie-is closed. Improved separation is obtained when a stream of pulp is issuing from this pipe, and a further part of the invention provides for the recovery of good pulp from this issuing stream. To this end the stream is delivered into another substaniially similar separator, which may, however, be of smaller size and somewhat simpler construction, and a suflicient pressure is maintained in the principal separator to impart the requisite speed of rotation to the pulp entering the auxilticular paper product that is to be manufactured.
  • the present invention makes provision for varying the aperture, located in the interior of the vortex, through which light impurities are al-' lowed to escape.
  • Figure 1 is a central vertical sectional view of a paper pulp treating apparatus including main and auxiliary separators each of the vortex type.
  • Figure 2 is a sectional view on line 2--2 of Figure 1.
  • Figure 3 is a fragmentary vertical sectional view of the upper portion of a separator showing a modified construction suitable for the removal of light impurities.
  • Figure 4 is a fragmentary elevation projected at right angles to Figure 3.
  • Figure 5 is a sectional view on line 5-5 of Figure 4.
  • Figure 6 is a sectional view similar to a portion of Figure 1, but showing a. modification within the settling chamber.
  • Figure 7 is a view similar to, a portion of Figure 1, but to a larger scale.
  • the body of the separator consists, as usual, of an elongated vertical cylindrical vessel l in which a vortex of pulp is established. To its diameters 4, 5, the line of junction between them being helical.
  • An inlet passage running from the pipe connection 3 merges into the part 5 of larger diameter which by the fitting of 'a tube or sleeve 6 into the part of smaller diameter becomes a helical inlet channel.
  • the inlet passage varies in cross-section from a circular form at the pipe flange 3 to a substantially rectangular form of greater depth than width where it merges into the body of the inlet head-piece, the depth preferably expanding and the width contracting.
  • paper pulp under which term is here included all fibre suspensions that are treated by paper-making methods and apparatus for the production not only of paper, but also of such products as mill-board, roofing felt and the like, varies greatly in its nature and composition. Ingeneral it may contain impurities both of large and small size, any of which may be specifically'heavier or lighter than the fibre of which the pulp is, and must remain, a substantially uniform suspension. In some pulps there may be an appreciable proportion of light impurities which tend to separate upon the inner boundary wall of the vortex of pulp, and for cer tain purposes it will be desirable to remove these. In other cases the impurities soflppearing may be negligible.
  • the sleeve 6 fitting the inlet head-piece and completing the helicalinlet passage may form the outlet for purified pulp. It is continued by a tube 1 to such a depth below the inlet that its mouth lies in the middle of a vortex of purified pul from 'bore vertical.
  • a flanged collecting cone 9 To the flanged lower end 8 of the principal vortex vessel I is attached a flanged collecting cone 9, with a stout metal ring ll intervening between them.
  • This ring is the rim of a spider having a draw-off tube [2 for impure pulp projecting upward from its centre, the bore of which is continuous with a passage l3 through one arm of the spider and the ring II.
  • the tube 12' supports, and communicates with the interior of, a hollow upright cone [4, the base of which is only a little less in'diameter than the inner Wall of the vessel. At its top the cone is continued as lindrical (or slightly tapered) cock 2
  • makes communication between the collecting cone 9 of the settling chamber and the sump [9 when the cock is turned to set the
  • the bore is threaded to receive a sleeve 23, and the effective bore may be varied as desired by removing this sleeve altogether 01' substituting for it a thicker or thinner sleeve.
  • lateral openings 24 are made in the seating 22 of the isolating valve, so that when the cock is turned at right angles to its open position the sleeve 23 in its bore is accessible for removal or for cleaning.
  • a groove 25 may be made over part of the circumference of the cock, so that in an intermediate position of the cock there is an air vent passage around it from the sump IE to one of the lateral openings 24 of the seating.
  • the pipe I3 is shown as provided with a cock 20 by which it may be closed.
  • the separator thus far described then works as a self-contained unit. Pulp is supplied by a pump to the inlet 3 at such a pressure that the pulp enters at high speed. It is directed by the inlet in a tangential and downwardly inclined path so setting up a vortex of pulp within the vessel I. Since the outlet 1 is central and directed upward, thev pulp after a certain downward travel must move inward and reverse its' vertical component of movement, all the time rotating at .a high angular velocity determined by the inlet speed and the outlet path.
  • the settling chamber re- .mains full of pulp and while shielded from the violent whirl above the baffle, whirling of the fluid column occurs therein above the major diameter portion of the cone l4 so that centrifugal stratification occurs, the stock of lowest consista tube l5 which, as shown, opens by a lateralv aperture beneath a horizontal baffle plate l6 attached to the top of the tube l5 of slightly less diameter than the base of the cone l4 and forming with the vessel wall a restricted annular passage !60.
  • annular wall or skirt l8 Beneath the bevelled edge of the baffle plate l6 and spaced slightly from it to form a second annular passage wardly inclined and leading into the passage IE0 is an annular wall or skirt l8 which tapers downward both in thickness and in external diameter and forms with the vessel wall a pro-. longation I62 of the passage I60.
  • the skirt may be integral with the baffle plate IE; it is preferable to support it independently from the draw-oil tube by a spider IT as shown, on order that there may be an uninterrupted gap between it and the baflle plate.
  • an isolating valve leading to a sump or collecting chamber l9 having in its lower end a discharge cook.
  • the isolating valve is of the nature of a cyl6l upwardly and outency, that is, of the maximum dilution of water, and the fine impurities being displaced toward the vertical axis of the whirl.
  • This portion of the settling chamber may be termed the active portion Below the major diameter portion of thecone l4, and particularly below the ring H, the centrifugal action is substantially spent.
  • the entry of the impurities into the settling chamber necessarily involves a corresponding displacement of fluid from that chamber, and this can take place by a creeping of pulp from within the skirt I 8 through the inclined channel l6! formed between the bevelled edges of the baffle l6 and the skirt 3.
  • should be no greater than is necessary for the passage of the largest agglomerations of impurities encountered; but as that varies with the class of pulp under treatment provision is made by openings 24 and the threading of the bore for readilyplacing and holding in the bore a sleeve 23 of such thickoutlet pipe, but by a depending cylindrical wall ness as circumstances admit, or of the removal of any such sleeve when the maximum bore is required.
  • the turning of the cock at right angles to the position shown in Figure 1 does not interrupt the operation of the separator, but only hinders for the few moments occupied in removing, replacing, or exchanging the sleeve, the passage of separated impurities into the collecting chamber.
  • the cock can also be so turned for the purpose of cleaning its bore should it become clogged.
  • the movement of heavy impurities into the settling chamber is greatly facilitated and encouraged by setting up a slight current of pulp through the annular gap between the baffle l5 and the vessel I beyond that afforded by the up- Ward flow between the baflle I6 and the skirt I8. This is done by constantly permitting a stream of material to be forced out'from the settling chamber through the pipe 15, the cone l4 and the pipe l3. Since the pipe 13 opens directly and unobstructedly at the most nearly axial point of the whirling column within the entire length of the active portion of the settling chamber, the stream of material passed through is drawn from stock of the lowest consistency, being much diluted, and contains the maximum amount of the small heavy impurities.
  • auxiliary separator may be of similar construction to that of the main separator. It can be of smaller size since the pulp it has to deal with is but a small fraction of the input into the principal separator; and it does not require a pipe I3 the aiding of the flow of heavy impurities into the set tling chamber being then done wholly by the spacing between the baflle l6 and the skirt I8 1 which facilitates upward displacement of material from the settling chamber around the periphery of the bafile. No alteration to the plant So far described is involved in making this addition, save the opening of the cock on pipe l3.
  • the pulp treated by the auxiliary separator being drawn from the inner portion of the-vortex in the main separator, conv tains a relatively large proportion of small size impurities, and the action of a pump on such im-" ,pure stock wouldhave the effect of So working the impurities into the fibers as to make later removal of the impurities almost if not quite impossible.
  • the condition of the pulp delivered to the auxiliary separator very little good fiber is lost in its collecting chamber.
  • inlet head As already indicated in some pulps there may be light impurities which tend to accumulate towards the interior boundary of the vortex of pulp. Removal of these may be provided for by the construction of inlet head shown in Figure 3 which may be substituted for that shown in Figure 1.
  • the inlet 3 leads is here completed, not by the The helical inlet passage to which that the pipe with 26, having a flange 21 a'nda lateral outlet 28.
  • the internal diameter of the wall 26 is reduced at its lower end, and the outlet pipe 29 for good pulp fits this reduced in the flange 27.
  • a portion of the annular space enclosed between the wall 26 and pipe 29 is partitioned oil by longitudinal ribs 30 seen in dotted lines in Fig. 4, which is an elevation of the lower part of the inlet head projected at right angles to Fig.
  • an opening or port 3! is made through the wall 26 at its lower end.
  • the wall 26 is surrounded by an apertured ring 32. which is rotatable upon the tube, and serves to close the opening 3
  • An opening is-made in the wall of the vessel l opposite the ring 32, and is normally closed by a plug 33 and cap 34. By removal of these access can 32 to turn it so as to close the entrance to the outlet channel 28 as much as desired.
  • FIG. 6 An alternative construction of parts within the settling chamber is shown in Figure 6 which may be substituted for that shown in Figure 1.
  • the pipe [5 connects directly with the pipe 12, and it is surrounded by a hollow cone 35 which is not in communication with it, and which is spaced a little from it at its upper end.
  • the cone is carried from the pipe I5 by a spider 36 and is integral with a cone 3'! covering the flange of pipe l2. permits of pulp displaced by the falling heavy impurities rising from the lower part of the settling chamber through the interior of the cone 35, and thence as before through the skirt l8 to the gap l6! between it and the baflle I6.
  • a paper pul separator In a paper pul separator. the combination with a vortex vessel having a pulp inlet tangential to said vessel at the upper end'thereof, and a central pulp outlet pipe extending through the upper end of said vessel to a distance below said inlet. of a baifie dividing the vortex vessel below said outlet pipe into a vortex chamber above said bafiie and a settling chamber below said baflie communicating only through a restricted annular passage between the periphery of said bafile and the wall of the vessel, and a skirt supported within said vessel beneath and spaced from said bafile prolonging said annular passage, the periphery of said bafilebeing downwardly and inwardly beveled and the upper edge of said skirt part and also an opening-' be had to the ring v be found in the This construction.
  • Apparatus for treating paper pulp comprising a cylindrical vortex vessel having a tangential inlet at its top and a central pulp outlet pipe extending through the upper end of said vessel to a distance below said inlet, a battle extending transversely across said vessel below said pipe, said baender having a periphery spaced from the vessel wall to provide a narrow annular passage therebetween, said baffle dividing said vessel into an upper vortex chamber and a lower settling chamber communicating with each other only by said annular passage, and a second pipe extending into said settling chamber and opening directly into said settling chamber beneath the center of said baflle in position to receive therein material reaching the most nearly axial position within said settling chamber and for discharge of such material from said vessel.
  • Apparatus for treating pulp comprising a pair of elongated cylindrical vortex vessels each having a tangential inlet at .the top thereof and a central outlet pipe extending through the top thereof and downwardly below said inlet, a baffie within and extending transversely across each vessel beneath said outlet pipe and dividing the vessel into a vortex chamber above and a settling chamber below said baflie communicating with each other through a restricted passage between the periphery of said baffle and the vessel wall, a skirt within each vessel spaced below said baiiie and forming with said vessel wall a continuation of said restricted passage, said space forming a second annular passage providing for upward fiow from within said skirt around the periphery of said baille, and a pipe extending into the settling chamber of the first and principal separator and opening unobstructedly beneath said battle in position to receive therein all material reaching the most nearly axial position within said settling chamber, said pipe leading directly to the inlet of the other vortex vessel, said other vortex vessel being
  • Apparatus for treating pulp comprising a pair of elongated cylindrical vortex vessels each having a tangential inlet at the top thereof and a central outlet pipe extending through the top thereof and downwardly below said inlet, a baffle within and extending transversely across each vessel beneath its outlet pipe and dividing the vessel into a vortex chamber above and a settling chamber below said baffle communicating with each other through a restricted passage between the periphery of said baille and the vessel wall, a skirt within each vessel spaced below said baffle and forming with said vessel wall a continuation of said restricted passage, the periphery of said baflle being downwardly and inwardly beveled and the upper edge of said skirt similarly beveled to define between them an upwardly and outwardly inclined passage providing for an upward and outward flow from within said skirt into said annular passage, and a pipe extending upwardly through the settling chamber of the first and principal vessel and opening directly into said settling chamber centrally beneath the baflie of said first vessel and in position to receive there
  • a pipe mounted centrally in the lower part of said vessel and communicating with a channel extending to and through the wall of said vessel, a baflle supported above said pipe, said pipe opening beneath the baffle in position to receive fluid therein from the most nearly axial position between said baflie and channel, said baflie dividing the vortex vessel into a vortex chamber and settling chamber communicating only by a restricted annular passage between the periphery of said baffle and the wall of the vessel, a skirt supported beneath and spaced from the periphery of said baille prolonging said annular passage, said space forming a second annular passage providing for upward flow from within said skirt around said baffle through said first-mentioned annular passage, and means for collecting material which settles in said settling chamber.
  • a paper pulp separator the combination with a vortex vessel having a pulp inlet tangential to said vessel at the upper end thereof and a central pulp outlet pipe extending through the upper end of said vessel to a distance below said inlet, of a battle dividing the vortex vessel into a vortex chamber and a settling chamber communicating with each other only by a restricted annular passage between the periphery of said battle and the wall of the vessel, a skirt supported beneath and spaced from the periphery of said batile prolonging said annular passage, the space between said skirt and baflle forming a channel providing for upward flow of pulp from within said skirt around said bave, means for collecting material which settles into said settling chamber, and a pipe extending centrally within said skirt and open at its upper end beneath said baffle to receive material from the nearest to the axial center within the length of said skirt and leading outside of said vessel below said skirt.
  • a paper pulp separator the combination with a vortex vessel having a pulp inlet tangential to said vessel at the upper end thereof and a central pulp outlet pipe extending through the upper end of said vessel to a distance below said inlet, of a bafile dividing the vortex vessel into a, vortex chamber and a settling chamber communicating with each other only by a restricted annular passage between the periphery of said baflle and the wall of the vessel, the outer edge of said baflie being inwardly and downwardly beveled, a skirt positioned beneath said outer edge and defining therewith a narrow downwardly and inwardly inclined annular passage through which pulp may pass upward from within said skirt around said baflle, said skirt forming between its outer face and the vessel wall a continuation of said restricted annular passage between said baffle and vessel wall, and a pipe havinga lateral aperture centrally of and beneath said baffle in position to receive material from within said settling chamber nearest to the central axis thereof, said pipe leading outwardly from said settling chamber

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US346781A 1939-07-26 1940-07-22 Vortex separator apparatus for treating paper pulp Expired - Lifetime US2375826A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB21725/39A GB532808A (en) 1939-07-26 1939-07-26 Improvements in separators of the vortex type for paper-pulp and the like

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US2375826A true US2375826A (en) 1945-05-15

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US346781A Expired - Lifetime US2375826A (en) 1939-07-26 1940-07-22 Vortex separator apparatus for treating paper pulp

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US (1) US2375826A (de)
DE (1) DE807354C (de)
FR (1) FR911603A (de)
GB (1) GB532808A (de)
NL (1) NL71650C (de)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2521103A (en) * 1948-09-15 1950-09-05 Minute Arthur Vortex separator for paper pulp
US2631728A (en) * 1946-10-22 1953-03-17 Lee W Popp Separation of solids from fluids
US2737857A (en) * 1950-07-01 1956-03-13 Kimberly Clark Co Hydraulic apparatus
US2796808A (en) * 1955-12-06 1957-06-25 Vickerys Ltd Vortex separators
US2856072A (en) * 1955-05-04 1958-10-14 Kronstad Haavard Centrifugal separators
US3405803A (en) * 1963-08-26 1968-10-15 Voith Gmbh J M Vortex separator
US3716137A (en) * 1969-03-21 1973-02-13 Celleco Ab Cyclone separator
US4282016A (en) * 1979-02-01 1981-08-04 Technical Development Co. Gas and failure particle separator system
US4392950A (en) * 1977-08-23 1983-07-12 The Bauer Bros. Co. Centrifugal type cleaner
US5071542A (en) * 1989-06-01 1991-12-10 Tuszko Wlodzimierz J Anti-suction cyclone separation method and apparatus
US20140326684A1 (en) * 2013-05-06 2014-11-06 Gregory S. Antoun Separation devices, systems and methods for separation of particulates from liquid

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2631728A (en) * 1946-10-22 1953-03-17 Lee W Popp Separation of solids from fluids
US2521103A (en) * 1948-09-15 1950-09-05 Minute Arthur Vortex separator for paper pulp
US2737857A (en) * 1950-07-01 1956-03-13 Kimberly Clark Co Hydraulic apparatus
US2856072A (en) * 1955-05-04 1958-10-14 Kronstad Haavard Centrifugal separators
US2796808A (en) * 1955-12-06 1957-06-25 Vickerys Ltd Vortex separators
US3405803A (en) * 1963-08-26 1968-10-15 Voith Gmbh J M Vortex separator
US3716137A (en) * 1969-03-21 1973-02-13 Celleco Ab Cyclone separator
US4392950A (en) * 1977-08-23 1983-07-12 The Bauer Bros. Co. Centrifugal type cleaner
US4282016A (en) * 1979-02-01 1981-08-04 Technical Development Co. Gas and failure particle separator system
US5071542A (en) * 1989-06-01 1991-12-10 Tuszko Wlodzimierz J Anti-suction cyclone separation method and apparatus
US20140326684A1 (en) * 2013-05-06 2014-11-06 Gregory S. Antoun Separation devices, systems and methods for separation of particulates from liquid
US9687760B2 (en) * 2013-05-06 2017-06-27 Gregory S. Antoun Separation devices, systems and methods for separation of particulates from liquid

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Publication number Publication date
DE807354C (de) 1951-06-28
GB532808A (en) 1941-01-31
NL71650C (de)
FR911603A (fr) 1946-07-16

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