US2757581A - Vortex separators - Google Patents

Vortex separators Download PDF

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US2757581A
US2757581A US331061A US33106153A US2757581A US 2757581 A US2757581 A US 2757581A US 331061 A US331061 A US 331061A US 33106153 A US33106153 A US 33106153A US 2757581 A US2757581 A US 2757581A
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chamber
gas
core
vortex
liquid
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US331061A
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Freeman Horace
John D Boadway
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Nichols Engineering and Research Corp
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Nichols Engineering and Research Corp
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Priority to US331061A priority Critical patent/US2757581A/en
Priority to FI144553A priority patent/FI40262B/fi
Priority claimed from US425942A external-priority patent/US2757582A/en
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Publication of US2757581A publication Critical patent/US2757581A/en
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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21DTREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
    • D21D5/00Purification of the pulp suspension by mechanical means; Apparatus therefor
    • D21D5/26De-aeration of paper stock
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D19/00Degasification of liquids
    • B01D19/0042Degasification of liquids modifying the liquid flow
    • B01D19/0052Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused
    • B01D19/0057Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused the centrifugal movement being caused by a vortex, e.g. using a cyclone, or by a tangential inlet
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24Feed or discharge mechanisms for settling tanks
    • B01D21/2405Feed mechanisms for settling tanks
    • B01D21/2411Feed mechanisms for settling tanks having a tangential inlet
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/26Separation of sediment aided by centrifugal force or centripetal force
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/26Separation of sediment aided by centrifugal force or centripetal force
    • B01D21/267Separation of sediment aided by centrifugal force or centripetal force by using a cyclone
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C3/00Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/08Vortex chamber constructions
    • B04C5/081Shapes or dimensions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/08Vortex chamber constructions
    • B04C5/107Cores; Devices for inducing an air-core in hydrocyclones
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/12Construction of the overflow ducting, e.g. diffusing or spiral exits
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/14Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/14Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations
    • B04C5/15Construction 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/14Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations
    • B04C5/18Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations with auxiliary fluid assisting discharge
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/14Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations
    • B04C5/185Dust collectors
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21DTREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
    • D21D5/00Purification of the pulp suspension by mechanical means; Apparatus therefor
    • D21D5/18Purification of the pulp suspension by mechanical means; Apparatus therefor with the aid of centrifugal force
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21DTREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
    • D21D5/00Purification of the pulp suspension by mechanical means; Apparatus therefor
    • D21D5/18Purification of the pulp suspension by mechanical means; Apparatus therefor with the aid of centrifugal force
    • D21D5/24Purification of the pulp suspension by mechanical means; Apparatus therefor with the aid of centrifugal force in cyclones

Definitions

  • This invention relates to methods and apparatus for separating gases, vapor and solid particles such as dirt, from liquids and liquid suspensions, the invention among various other possible uses being particularly adapted for the treatment of paper pulp suspensions.
  • the suspension is introduced tangentially at one end of a cylindrical separating chamber from which the vortex travels to the remote end of such chamber and then reverses and extends back as an inner vortex to a treated stock outlet located centrally of the rst end of the chamber and from which the stock is withdrawn by suction means such as a vacuum pump or barometric leg, While the gases are being exhausted through a gas outlet at the center of the remote end of the chamber by means of a vacuum pump, the dirt particles also being discharged from adjacent the periphery ot the vortex at such remote end.
  • the present invention relates to certain simplified ernbodiments ot' the methods and apparatus disclosed and claimed in ⁇ the aforesaid co-pending application, and in which embodiments the apparatus is so constructed and arranged as to cause a vortex of the stock being treated to pass directly through a separating chamber and thence ⁇ directly into a suction pump or barometric leg, without reversing the vortex.
  • a gas core in the vortex is maintained under low subatmospheric pressure by constantly evacuating gas from the mid portion of the intake end of the separating chamber and toward the other end of the separating chamber, the vortex passage is so shaped that the gas core is caused to diminish in diameter and disappear before the treated stream passes on to the suction pump or for any considerable distance into a barometric leg if such is used instead of a pump.
  • the separating chamber walls are so restricted and shaped at regions spaced from the intake end that the liquid immediately surrounding the core Will tend to travel back toward the gas exhausting connection and thus any bubbles or gas which have been forced to the innermost portions of the vortex will be kept from passing on with the treated stock, whereas the liquid in the outer portions of the vortex will be free to pass on to the barometric leg or equivalent suction pump, and meanwhile also a small amount of the liquid or suspension containing the undesired solid particles which have been iiung to the outermost part of the vortex, will be skimmed off and dis ⁇ charged.
  • the vortex core at a region spaced from the stock inlet is caused to disappear by reason of lthe combined effects of the restricted shape of the chamber Walls and of an axial obstruction located in the mid portion of the stream of treated stock.
  • Fig. l is a vertical sectional View of the presently preferred embodiment of the invention herein disclosed;
  • Fig. 2 is a vertical sectional view of another embodiment or' the invention; and t Fig. 3 is a horizontal sectional view taken substantially along line 3-3 of Fig. 2.
  • the liquid suspension or flowing mixture to be treated is forced under pressure from an intake pipe 10 through a headpiece member 11, the inlet portion 12 of which is so shaped as to greatly restrict the cross-section of the incoming stream (for example in the neighborhood of 50%) and from this trumpet-like portion 12 the stream is directed tangentially into a chamber 13 to form a vortex layer 14 of the mix ture around on the inside walls of ⁇ the headpiece chamber 13 and then around the inside wall of a chamber 15 preferably of cylindrical cross-section, the direction of ow of the liquid in the vortex being indicated by the helical line 16.
  • an axial gas discharge outlet 1.8 is provided for connection to a vacuum pump as indicated, which should be of sutilcient capacity to maintain the core 17 constantly at a low subatmospheric pressure, for example from about 5-8 cms. Hg absolute.
  • a vacuum pump as indicated, which should be of sutilcient capacity to maintain the core 17 constantly at a low subatmospheric pressure, for example from about 5-8 cms. Hg absolute.
  • the lower end of the chamber 15 is connected to another chamber portion 20, having walls to provide a funnel-like shape, the upper portions of which are more and more outwardly flared, whereby the outer diameter of the vortex layer as at Ma'becomes smaller and smaller and the diameter of the core as at 17o correspondingly diminishes, the core ceasing to exist as indicated at point 17h so that beyond this point the flow of liquid will be free of any gas core.
  • the restriction of the wall of chamber portion 2 ?
  • a particle at that point will be sub'iect to acceleration upwardly along the wall equal to z las@ and this acceleration of the particle will be opposed by one directed downwardly along the wall equal to g sin 6, where V equals the velocity of the steam tangentially 1ntroduced; r equals the radius of the point p about the axis of the apparatus; and g represents gravity.
  • the chamber portion is connected to a succeeding chamber portion 2l, the greater part of which may be cylindrical.
  • the solid particles in the vortex will have been thrown to the wall surfaces along which they travel downwardly and pass outwardly to the exterior of an annular lip 22, i. e. into a small annular cavity 23 from which a small amount of the stock, along with the particles, is discharged tangentially through a rejected stock outlet 24 having a suitable regulating valve as at 25, the construction here being similar to that shown in the horizontal sectional View of Fig. 3.
  • a relatively simple form of device having no moving parts, but which is adapted concurrently for removing from the liquid not only the solid particles such as dirt, but also gases and vapors, whether in the form of bubbles or as dissolved or occluded gas. And by reason of the manner in which the gas core is in effect extinguished and kept from penetrating into the liquid In case the outlet 26 o outlet stream, substantially no bubbles or froth can be carried out with the outlet stream of accepted stock, even when subjected to a strong suction force.
  • the embodiment of the invention here shown has the further advantage that in the upper portions of the device, the greater part of the gases are separated from the liquid and exhausted from the core, and hence such gases can no longer tend to float the suspended matter, such as fiber or the undesired particles. Thus in the lower portions of the apparatus, more effective separation of the solid particles is made possible.
  • Fig. 2 While the embodiment of the invention shown in Fig. 2, except for the features below mentioned, is similar to that of Fig. l and the corresponding parts are yidentiiied by the same reference numerals accompanied by prime marks.
  • Fig. 2 the walls of the chamber portion 20', instead of being formed with the particular curvature above-explained in connection with Fig. l, are here shown of a slightly conical shape, i. e. with a straight taper.
  • a central streamlined obstructing member 32 is mounted, preferably to extend into the lower end of chamber portion 21', and down for some distance into the upper end of outlet 26.
  • This member 32 may be supported as by small rods or spider-like means 33 axed in or about member 32 with outer portions extending through the walls of chamber portion 26.
  • Apparatus for separating gas and solid particles from liquid pulp suspensions comprising an elongated chamber having a body portion of circular internal crosssection, means for so discharging liquid into one end of said chamber as to maintain a helical high velocity ow of lthe liquid about the inside walls of the chamber, surrounding a core of gas and extending to the other end of the chamber, a gas outlet at the mid portion of said first-named end of said chamber, means connected to such outlet for -evacuating gas therethrough and for maintaining said core at a low sub-atmospheric pressure, a portion of said chamber which is spaced from the firstnamed end thereof being progressively restricted in cross section, the restriction being such as to cause said core gradually to diminish ,in diameter and then terminate, suction means in the form of and a barometrie leg connected to said other end of said chamber in a position whereby said helical flow after passing the end of said core may continue on directly into such leg, means providing an annular cavity for receiving the outermost portions of said helical
  • Apparatus for separating gas and solid particles from liquid comprising an elongated chamber having a body portion of circular internal cross-section, means for so introducing the mixture of liquid particles and gas into one end of said chamber as to cause a helical high velocity ow thereof about the inside walls of the chamber and surrounding a core of gas, with the helical ow extending to the other .end of the chamber, means for constantly evacuating gas from said core, suction means at said other end of the chamber for discharging said helical low, the passage provided for said helical flow at a region spaced from the said first-named end of the chamber being so restricted as to cause gradual restriction and then disappearance of said gas core before the helical flow is discharged to said suction means, and means providing an annular cavity for receiving the outermost portions of said helical ow at a region adjacent said other end of said chamber, whereby said particles as thrown by centrifugal action to the walls of the chamber will be re ceived in such cavity, and a connection

Description

H. FREEMAN Er AL 2,757,581
VORTEX SEPARATORS Filed Jan, 13, 1953 Mq cuz/M PUMP INVENTORS. HORACE fEE/MN BYJH/v D. .50A D WA y.
United States PatentN Oce 2,757,581 Patented Aug. 7, 1956 VORTEX SEPARATORS Horace Freeman, Cap-de-la-Madeleine, Quebec, and John l). Roadway, Three Rivers, Quebec, Canada, assignors, by mesne assignments, to Nichols Engineering and Research Corporation, New York, N. Y., a corporation of Delaware Application January 13, 1953, Serial No. 331,061
4 Claims. (Cl. 92-28) This invention relates to methods and apparatus for separating gases, vapor and solid particles such as dirt, from liquids and liquid suspensions, the invention among various other possible uses being particularly adapted for the treatment of paper pulp suspensions.
in our co-pending application Serial No. 314,248, tiled October ll, 1952, and now abandoned, entitled Method and Apparatus for Separating Undesired Particles and Gases from Paper Pulp Suspensions and Other Fluids, and a continuation-in-part thereof, Serial No. 324,561, tiled December 6, 1952, and entitled Method and Apparatus for Treating Pulp Suspensions and Other Fluids for Removal of Undesired Particles and Gases, reference to which is hereby made, there are disclosed methods and apparatus for separating dirtparticles, dissolved and occluded gas and bubbles from pulp suspensions and the like by maintaining a high velocity vortex of the suspension surrounding a gas core maintained under a low sub-atmospheric pressure by continuously exhausting gas therefrom, whereby dissolved gas and any occluded gas is liberated from the inner portions of the liquid of the vortex and the resulting bubbles and any bubbles originally present are forced by the action of the centrifugal force of the vortex into the core and evacuated, while the dirt particles are flung to the outer portions of the vortex, a stream of the treated suspension being continuously discharged from the mid portions of the vortex, while separately a small amount o1 the suspension containing the dirt particles is also continuously discharged from an outer portion of the vortex. i
With the embodiments of the invention disclosed in the above-mentioned applications, the suspension is introduced tangentially at one end of a cylindrical separating chamber from which the vortex travels to the remote end of such chamber and then reverses and extends back as an inner vortex to a treated stock outlet located centrally of the rst end of the chamber and from which the stock is withdrawn by suction means such as a vacuum pump or barometric leg, While the gases are being exhausted through a gas outlet at the center of the remote end of the chamber by means of a vacuum pump, the dirt particles also being discharged from adjacent the periphery ot the vortex at such remote end.
The present invention relates to certain simplified ernbodiments ot' the methods and apparatus disclosed and claimed in `the aforesaid co-pending application, and in which embodiments the apparatus is so constructed and arranged as to cause a vortex of the stock being treated to pass directly through a separating chamber and thence `directly into a suction pump or barometric leg, without reversing the vortex. A gas core in the vortex is maintained under low subatmospheric pressure by constantly evacuating gas from the mid portion of the intake end of the separating chamber and toward the other end of the separating chamber, the vortex passage is so shaped that the gas core is caused to diminish in diameter and disappear before the treated stream passes on to the suction pump or for any considerable distance into a barometric leg if such is used instead of a pump.
Preferably also the separating chamber walls are so restricted and shaped at regions spaced from the intake end that the liquid immediately surrounding the core Will tend to travel back toward the gas exhausting connection and thus any bubbles or gas which have been forced to the innermost portions of the vortex will be kept from passing on with the treated stock, whereas the liquid in the outer portions of the vortex will be free to pass on to the barometric leg or equivalent suction pump, and meanwhile also a small amount of the liquid or suspension containing the undesired solid particles which have been iiung to the outermost part of the vortex, will be skimmed off and dis` charged. With another form of the invention, the vortex core at a region spaced from the stock inlet is caused to disappear by reason of lthe combined effects of the restricted shape of the chamber Walls and of an axial obstruction located in the mid portion of the stream of treated stock.
Various further and more specific objects, features and advantages of the invention will appear from the detailed description given below taken in connection with the accompanying drawings which form a part of this specification and illustrate merely by way of example, preferred forms of apparatus for the practice of the invention. The invention consists in such novel features, arrangements and combinations of parts and method steps as may be shown and described herein.
ln the drawings:
Fig. l is a vertical sectional View of the presently preferred embodiment of the invention herein disclosed;
Fig. 2 is a vertical sectional view of another embodiment or' the invention; and t Fig. 3 is a horizontal sectional view taken substantially along line 3-3 of Fig. 2.
Referring to Fig. l in further detail, the liquid suspension or flowing mixture to be treated is forced under pressure from an intake pipe 10 through a headpiece member 11, the inlet portion 12 of which is so shaped as to greatly restrict the cross-section of the incoming stream (for example in the neighborhood of 50%) and from this trumpet-like portion 12 the stream is directed tangentially into a chamber 13 to form a vortex layer 14 of the mix ture around on the inside walls of `the headpiece chamber 13 and then around the inside wall of a chamber 15 preferably of cylindrical cross-section, the direction of ow of the liquid in the vortex being indicated by the helical line 16. p
ln view of the form of the restricted inlet, a substantial part of the pressure energy of the incoming stream will be converted to velocity energy in the vortex layer 14, and the resulting high velocity will promptly cause solid particles in the mixture to be Hung toward the inner wall of the chamber 15, whereas any bubbles will be forced inwardly of the vortex and into a gas core thereof as indicated at 17.
Within the chamber portion 13 of the headpiece an axial gas discharge outlet 1.8 is provided for connection to a vacuum pump as indicated, which should be of sutilcient capacity to maintain the core 17 constantly at a low subatmospheric pressure, for example from about 5-8 cms. Hg absolute. Thus the liquid in the innermost portions of the vortex layer 14 will be maintained under low subatmospheric pressure with the result that any dissolved or occluded gases contained therein will be liberated into the core 17, into which also any bubbles in the liquid will be discharged, so that the gases and any vapors thus liberated, as Well as the gas of such bubbles, will be exhausted through the outlet 18.
As shown the lower end of the chamber 15 is connected to another chamber portion 20, having walls to provide a funnel-like shape, the upper portions of which are more and more outwardly flared, whereby the outer diameter of the vortex layer as at Ma'becomes smaller and smaller and the diameter of the core as at 17o correspondingly diminishes, the core ceasing to exist as indicated at point 17h so that beyond this point the flow of liquid will be free of any gas core. To accomplish this result effectively, the restriction of the wall of chamber portion 2? should preferably be such that the components of centrifugal force and of the force of gravity effective on the liquid at points in the innermost portions of the vortex layer Elda, will be such as to cause such inner portions to tend to rise, whereas the liquid in the outer portions of the vortex layer Mn are left free to pass downwardly. Thus, assuming that a vertical cross-section at a point p is at the angie t to the horizontal, then a particle at that point will be sub'iect to acceleration upwardly along the wall equal to z las@ and this acceleration of the particle will be opposed by one directed downwardly along the wall equal to g sin 6, where V equals the velocity of the steam tangentially 1ntroduced; r equals the radius of the point p about the axis of the apparatus; and g represents gravity.
As more fully explained in our above-mentioned application entitled Method and Apparatus for Treating Pulp Suspensions and Other Fluids for Removal of Undesired Particles and Gases, one may, by taking into censideration these opposed forces, so form the vertical crossscction of a funnel-shaped chamber as to accomplish theabove-mentioned result of causing the liquid of the inner portions of the vortex layer therein to rise while the liquid in the outer portions descends. constitutes a barometric leg, it should be of such height as to maintain the hydraulic liquid level in or above the tapered section 20, and if the discharge is a suction pump, such pump should be capable of accomplishing an equivalent etfect, Consequently substantially all of the gases, vapor and bubbles liberated from the vortex layer throughout the chamber portions and 20 will either be promptly exhausted from the core 17, or if some thereof remains, contained in the innermost parts of the vortex in the chamber portion 20, there will be no opportunity for such remaining gas to pass on in the treated flow, because of the upward movement of the innermost parts of the vortex.
As shown, the chamber portion is connected to a succeeding chamber portion 2l, the greater part of which may be cylindrical. In this portion the solid particles in the vortex will have been thrown to the wall surfaces along which they travel downwardly and pass outwardly to the exterior of an annular lip 22, i. e. into a small annular cavity 23 from which a small amount of the stock, along with the particles, is discharged tangentially through a rejected stock outlet 24 having a suitable regulating valve as at 25, the construction here being similar to that shown in the horizontal sectional View of Fig. 3. Either a barometric leg, anl upper portion of which is indicated at 26, or a suitable suction pump intake, then receives the swirling streamof treated stock as at 27, free of bul*- bles and gases, as Well as free of the undesired solid particles.
The various chamber parts of the apparatus may be interconnected by flanges vas indicated, detachably held together by bolts (which for clearness and simplicity are omitted from the drawings.) Y
Thus a relatively simple form of device is provided having no moving parts, but which is adapted concurrently for removing from the liquid not only the solid particles such as dirt, but also gases and vapors, whether in the form of bubbles or as dissolved or occluded gas. And by reason of the manner in which the gas core is in effect extinguished and kept from penetrating into the liquid In case the outlet 26 o outlet stream, substantially no bubbles or froth can be carried out with the outlet stream of accepted stock, even when subjected to a strong suction force. The embodiment of the invention here shown has the further advantage that in the upper portions of the device, the greater part of the gases are separated from the liquid and exhausted from the core, and hence such gases can no longer tend to float the suspended matter, such as fiber or the undesired particles. Thus in the lower portions of the apparatus, more effective separation of the solid particles is made possible.
While the embodiment of the invention shown in Fig. 2, except for the features below mentioned, is similar to that of Fig. l and the corresponding parts are yidentiiied by the same reference numerals accompanied by prime marks. in Fig. 2 the walls of the chamber portion 20', instead of being formed with the particular curvature above-explained in connection with Fig. l, are here shown of a slightly conical shape, i. e. with a straight taper. The chamber portion with this form of taper is incapable of diminishing a vortex gas core as at 30 to the point of extinction, but instead such core as indicated at 3l will tend to continue on within the vortexstream and consequently here, a central streamlined obstructing member 32 is mounted, preferably to extend into the lower end of chamber portion 21', and down for some distance into the upper end of outlet 26. This member 32 may be supported as by small rods or spider-like means 33 axed in or about member 32 with outer portions extending through the walls of chamber portion 26. By means of the member 32, the vortex core is caused to finally terminate as indicated at the upper end of this member.
Although certain particular embodiments of the invention are herein disclosed for purposes of explanation, vari ous further modifications thereof, after study of this application, will be apparent to those skilled in the art to which the invention pertains. Reference should accordingly be had to the appended claims in determining the scope of the invention.
What is claimed and desired to be secured by Letters Patent is:
l. Apparatus for separating gas and solid particles from liquid pulp suspensions comprising an elongated chamber having a body portion of circular internal crosssection, means for so discharging liquid into one end of said chamber as to maintain a helical high velocity ow of lthe liquid about the inside walls of the chamber, surrounding a core of gas and extending to the other end of the chamber, a gas outlet at the mid portion of said first-named end of said chamber, means connected to such outlet for -evacuating gas therethrough and for maintaining said core at a low sub-atmospheric pressure, a portion of said chamber which is spaced from the firstnamed end thereof being progressively restricted in cross section, the restriction being such as to cause said core gradually to diminish ,in diameter and then terminate, suction means in the form of and a barometrie leg connected to said other end of said chamber in a position whereby said helical flow after passing the end of said core may continue on directly into such leg, means providing an annular cavity for receiving the outermost portions of said helical flow at a region adjacent said other end of said chamber, whereby said particles as thrown by centrifugal action to the walls of the chamber will be received in such cavity, and a tangentially positioned connection for discharging a small amount of liquid with such particles from said annular cavity.
2. Apparatus for separating gas and solid particles from liquid, comprising an elongated chamber having a body portion of circular internal cross-section, means for so introducing the mixture of liquid particles and gas into one end of said chamber as to cause a helical high velocity ow thereof about the inside walls of the chamber and surrounding a core of gas, with the helical ow extending to the other .end of the chamber, means for constantly evacuating gas from said core, suction means at said other end of the chamber for discharging said helical low, the passage provided for said helical flow at a region spaced from the said first-named end of the chamber being so restricted as to cause gradual restriction and then disappearance of said gas core before the helical flow is discharged to said suction means, and means providing an annular cavity for receiving the outermost portions of said helical ow at a region adjacent said other end of said chamber, whereby said particles as thrown by centrifugal action to the walls of the chamber will be re ceived in such cavity, and a connection for discharging a small amount of liquid with such particles from said annular cavity.
3. Apparatus in accordance with claim 2 and in which the diameter of the chamber is diminished to cause said gradual restriction and an axial obstruction is provided for causing termination and disappearance of the gas core.
4. Apparatus in accordance with claim 2 and in which the means for introducing the mixture comprises a restricted tangential inlet and the means for evacuating gas comprises an outlet conduit positioned centrally of the chamber and at the same end thereof as the inlet and a vacuum pump connected to such conduit.
References Cited in the le of this patent UNITED STATES PATENTS

Claims (1)

1. APPARATUS FOR SEPARATING GAS AND SOLID PARTICLES FROM LIQUID PULP SUSPENSIONS COMPRISING AN ELONGATED CHAMBER HAVING A BODY PORTION OF CIRCULAR INTERNAL CROSSSECTION, MEANS FOR SO DISCHARGING LIQUID INTO ONE END OF SAID CHAMBER AS TO MAINTAIN A HELICAL HIGH VELOCITY FLOW OF THE LIQUID ABOUT THE INSIDE WALLS OF THE CHAMBER, SURROUNDING A CORE OF GAS AND EXTENDING TO THE OTHER END OF THE CHAMBER, A GAS OUTLET AT THE MID PORTION OF SAID FIRST-NAMED END OF SAID CHAMBER, MEANS CONNECTED TO SUCH OUTLET FOR EVACUATING GAS THERETHROUGH AND FOR MAINTAINING SAID CORE AT A LOW SUB-ATMOSPHERIC PRESSURE, A PORTION OF SAID CHAMBER WHICH IS SPACED FROM THE FIRSTNAMED END THEREOF BEING PROGRESSIVELY RESTRICTED IN CROSSSECTION, THE RESTRICTION BEING SUCH AS TO CAUSE SAID CORE GRADUALLY TO DIMINISH IN DIAMETER AND THEN TERMINATE,
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US425942A US2757582A (en) 1952-09-24 1954-04-27 Separation of gas and undesired particles from liquids

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Cited By (31)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2859668A (en) * 1956-07-02 1958-11-11 Dominion Eng Works Ltd Method and apparatus for forming pulp stock into a sheet
US2977355A (en) * 1954-01-13 1961-03-28 Celanese Corp Alkali cellulose aging
US3007542A (en) * 1957-06-18 1961-11-07 Salvatore W Giampapa Degasifier
US3105044A (en) * 1960-03-14 1963-09-24 Bird Machine Co Separator
US3173683A (en) * 1961-09-27 1965-03-16 Headley Townsend Backhouse Sheet feeding machines
US3176912A (en) * 1962-06-11 1965-04-06 Leybold Holding A G Device to reduce oil losses
US4308038A (en) * 1979-05-10 1981-12-29 Santek, Inc. Inertial-electrostatic wet precipitator
US4378289A (en) * 1981-01-07 1983-03-29 Hunter A Bruce Method and apparatus for centrifugal separation
US4392950A (en) * 1977-08-23 1983-07-12 The Bauer Bros. Co. Centrifugal type cleaner
US4411673A (en) * 1980-07-17 1983-10-25 Sweco, Incorporated Method and apparatus for degassing liquids
US4605495A (en) * 1984-03-19 1986-08-12 Bird Machine Company, Inc. Hydrocyclone separator apparatus
EP0200096A2 (en) * 1985-05-03 1986-11-05 Hein, Lehmann Aktiengesellschaft Screening device
EP0234101A1 (en) * 1986-02-22 1987-09-02 Elp Products Ltd. A reverse hydrocyclone cleaner for removing light contaminants from pulp slurry
US4744890A (en) * 1979-11-15 1988-05-17 University Of Utah Flotation apparatus and method
US4838434A (en) * 1979-11-15 1989-06-13 University Of Utah Air sparged hydrocyclone flotation apparatus and methods for separating particles from a particulate suspension
US4900339A (en) * 1989-03-20 1990-02-13 Ward David P Ammonia flow divider
US4997549A (en) * 1989-09-19 1991-03-05 Advanced Processing Technologies, Inc. Air-sparged hydrocyclone separator
US5045218A (en) * 1986-11-26 1991-09-03 Delawood Pty. Ltd. Method of separating a lighter dispersed fluid from a denser liquid in a hydrocyclone having flow-modifying means
US5071542A (en) * 1989-06-01 1991-12-10 Tuszko Wlodzimierz J Anti-suction cyclone separation method and apparatus
US5250093A (en) * 1992-03-09 1993-10-05 O. I. Corporation Water management device for gas chromatography sample concentration
US5938926A (en) * 1995-08-11 1999-08-17 Thermo Black Clawson Extended dwell reverse hydrocyclone cleaner
US6485534B2 (en) * 2000-12-20 2002-11-26 Axcellis Technologies, Inc. Contaminant collector trap for ion implanter
US20040144256A1 (en) * 2003-01-28 2004-07-29 Mazzei Angelo L. Enhanced separation and extraction of gas from a liquid utilizing centrifugal forces
WO2004097107A1 (en) * 2003-04-25 2004-11-11 Pom Technology Oy Ab Method and arrangement at gas removal, and the use thereof
US20060226055A1 (en) * 2003-08-29 2006-10-12 Oscar Castro Soto Inlet head for a cyclone separator
US20090071880A1 (en) * 2003-08-29 2009-03-19 Vulco, S.A. Cyclone Separator Having An Inlet Head
DE102009031103A1 (en) * 2009-06-29 2010-12-30 Khs Gmbh Method and device for degassing a liquid
US20120211230A1 (en) * 2009-10-27 2012-08-23 Karl Gregory Anderson Subsea separation systems
US20150110933A1 (en) * 2012-05-23 2015-04-23 Fruit Tech Natural S.A. Apparatus and method for ohmic-heating a particulate liquid
US20190257330A1 (en) * 2018-02-19 2019-08-22 Vtx Technology Llc Vortex flow catalytic conversion apparatus and method of vortex flow catalytic conversion
US11059049B2 (en) * 2016-07-21 2021-07-13 Superior Industries, Inc. Classifying apparatus, systems and methods

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US2187646A (en) * 1935-08-16 1940-01-16 Bbc Brown Boveri & Cie Separator
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US2346005A (en) * 1940-08-15 1944-04-04 Tandy A Bryson Vortex separator
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Cited By (43)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2977355A (en) * 1954-01-13 1961-03-28 Celanese Corp Alkali cellulose aging
US2859668A (en) * 1956-07-02 1958-11-11 Dominion Eng Works Ltd Method and apparatus for forming pulp stock into a sheet
US3007542A (en) * 1957-06-18 1961-11-07 Salvatore W Giampapa Degasifier
US3105044A (en) * 1960-03-14 1963-09-24 Bird Machine Co Separator
US3173683A (en) * 1961-09-27 1965-03-16 Headley Townsend Backhouse Sheet feeding machines
US3176912A (en) * 1962-06-11 1965-04-06 Leybold Holding A G Device to reduce oil losses
US4392950A (en) * 1977-08-23 1983-07-12 The Bauer Bros. Co. Centrifugal type cleaner
US4308038A (en) * 1979-05-10 1981-12-29 Santek, Inc. Inertial-electrostatic wet precipitator
US4744890A (en) * 1979-11-15 1988-05-17 University Of Utah Flotation apparatus and method
US4838434A (en) * 1979-11-15 1989-06-13 University Of Utah Air sparged hydrocyclone flotation apparatus and methods for separating particles from a particulate suspension
US4411673A (en) * 1980-07-17 1983-10-25 Sweco, Incorporated Method and apparatus for degassing liquids
US4378289A (en) * 1981-01-07 1983-03-29 Hunter A Bruce Method and apparatus for centrifugal separation
US4605495A (en) * 1984-03-19 1986-08-12 Bird Machine Company, Inc. Hydrocyclone separator apparatus
EP0200096A2 (en) * 1985-05-03 1986-11-05 Hein, Lehmann Aktiengesellschaft Screening device
EP0200096A3 (en) * 1985-05-03 1987-04-29 Hein, Lehmann Aktiengesellschaft Screening device
EP0234101A1 (en) * 1986-02-22 1987-09-02 Elp Products Ltd. A reverse hydrocyclone cleaner for removing light contaminants from pulp slurry
US4797203A (en) * 1986-02-22 1989-01-10 Elp Products Limited Reverse hydrocyclone cleaner for removing light contaminants from pulp slurry
US5045218A (en) * 1986-11-26 1991-09-03 Delawood Pty. Ltd. Method of separating a lighter dispersed fluid from a denser liquid in a hydrocyclone having flow-modifying means
US4900339A (en) * 1989-03-20 1990-02-13 Ward David P Ammonia flow divider
US5071542A (en) * 1989-06-01 1991-12-10 Tuszko Wlodzimierz J Anti-suction cyclone separation method and apparatus
US4997549A (en) * 1989-09-19 1991-03-05 Advanced Processing Technologies, Inc. Air-sparged hydrocyclone separator
US5250093A (en) * 1992-03-09 1993-10-05 O. I. Corporation Water management device for gas chromatography sample concentration
US5358557A (en) * 1992-03-09 1994-10-25 O.I. Corporation Water management device for gas chromatography sample concentration
US5470380A (en) * 1992-03-09 1995-11-28 O. I. Corporation Management device for gas chromatography sample concentration
US5582633A (en) * 1992-03-09 1996-12-10 O.I. Corporation Water management device for gas chromatography sample concentration
US5814128A (en) * 1992-03-09 1998-09-29 Oi Corporation Water management device for gas chromatography sample concentration
US5938926A (en) * 1995-08-11 1999-08-17 Thermo Black Clawson Extended dwell reverse hydrocyclone cleaner
US6485534B2 (en) * 2000-12-20 2002-11-26 Axcellis Technologies, Inc. Contaminant collector trap for ion implanter
US6866703B2 (en) * 2003-01-28 2005-03-15 Angelo L. Mazzei Enhanced separation and extraction of gas from a liquid utilizing centrifugal forces
US20040144256A1 (en) * 2003-01-28 2004-07-29 Mazzei Angelo L. Enhanced separation and extraction of gas from a liquid utilizing centrifugal forces
US7691184B2 (en) 2003-04-25 2010-04-06 Pom Technology Oy Ab Method and arrangement at gas removal, and the use thereof
US20070028778A1 (en) * 2003-04-25 2007-02-08 Pom Technology Oy Ab Method and arrangement at gas removal, and the use thereof
WO2004097107A1 (en) * 2003-04-25 2004-11-11 Pom Technology Oy Ab Method and arrangement at gas removal, and the use thereof
US20060226055A1 (en) * 2003-08-29 2006-10-12 Oscar Castro Soto Inlet head for a cyclone separator
US7434696B2 (en) * 2003-08-29 2008-10-14 Vulco, S.A. Inlet head for a cyclone separator
US20090071880A1 (en) * 2003-08-29 2009-03-19 Vulco, S.A. Cyclone Separator Having An Inlet Head
US8104622B2 (en) 2003-08-29 2012-01-31 Vulco, S.A. Cyclone separator having an inlet head
DE102009031103A1 (en) * 2009-06-29 2010-12-30 Khs Gmbh Method and device for degassing a liquid
US20120211230A1 (en) * 2009-10-27 2012-08-23 Karl Gregory Anderson Subsea separation systems
US20150110933A1 (en) * 2012-05-23 2015-04-23 Fruit Tech Natural S.A. Apparatus and method for ohmic-heating a particulate liquid
US11059049B2 (en) * 2016-07-21 2021-07-13 Superior Industries, Inc. Classifying apparatus, systems and methods
US11845088B2 (en) 2016-07-21 2023-12-19 Superior Industries, Inc. Classifying apparatus, systems and methods
US20190257330A1 (en) * 2018-02-19 2019-08-22 Vtx Technology Llc Vortex flow catalytic conversion apparatus and method of vortex flow catalytic conversion

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