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US630309A - Apparatus for cleaning paper-pulp. - Google Patents

Apparatus for cleaning paper-pulp. Download PDF

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Publication number
US630309A
US630309A US66334197A US1897663341A US630309A US 630309 A US630309 A US 630309A US 66334197 A US66334197 A US 66334197A US 1897663341 A US1897663341 A US 1897663341A US 630309 A US630309 A US 630309A
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vessel
fibers
pulp
baffles
spaces
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US66334197A
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Albert Aeberg
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B5/00Washing granular, powdered or lumpy materials; Wet separating
    • B03B5/62Washing granular, powdered or lumpy materials; Wet separating by hydraulic classifiers, e.g. of launder, tank, spiral or helical chute concentrator type

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  • the object of the present invention is a dresser for cleaning or purifying paper or wood pulp, and comprises a downwardly-tapering or conical vessel into which the paper or wood pulp to be purified is introduced and caused to rotate by any suitable means.
  • a downwardly-tapering or conical vessel into which the paper or wood pulp to be purified is introduced and caused to rotate by any suitable means.
  • the good fibers, with which are mixed the chips, twigs, knots, or other impurities become gradually released and, being of smaller specific gravity than water, rise and overflow at the overflow-outlet at the upper edge of the vessel.
  • the wood or paperpulp to be purified differs from other mixtures of substances in that the chief constituent parts of the impuritiesthe chips,twigs,or knots-have only a slightlygreater specific gravity than that of the fibers themselves.
  • the knots are of course so light that as long as they are surrounded with fibers they also have the same tendency to rise upward as the fibers. It is only by freeing or separating the fibers that the difference in the specific gravity of knots, twigs, and chips on one hand and fibers on the other hand be- This difference is, how ever, so small that the knots, &c., would rotate around the walls of the vessel and apart of them would even rise unless prevented from so doing.
  • bafiles For this purpose I secure battens, bafiles, or ribs to the inner surface" of the vessel at suitable distances apart. mass directly in front of. the baffles is stopped by the latter, the flow of the liquid being impeded and eddy-currents formed behind the bafiles, and so-called dead-spaces being formed in which the specifically-heavier substances are deposited. Particles of the wood or paper pulp that may have descended to the lower portion of the apparatus are caused to rise by means of a rotating worm.
  • FIG. 1 shows the apparatus in longitudi- The nal section, Fig. 2 being a plan, partly in sec tion, through Fig. 1.
  • the mass is introduced at the top, preferably at the center, into a stone or sand trap (it, (having preferably the shape of a box,) and from which it overflows into the main vessel, stones and heavy foreign substances be ing deposited in the trap.
  • the mass then passes into a lower chamber or deflector 1), ar-
  • a mixing device rotating in a horizontal plane, causing the fluid mass to rotate.
  • This mixing device may consist of a screw propeller or disk secured on a rotating central spindle r.
  • the funnel-shaped main vessel d is pro vided on its inner walls with slightlyprojecting longitudinal ribs or baffles e, converging toward the center, said baffies producing eddy currents and causing the heavier particles or impurities contained in the pulp to settle.
  • the fibers of the wood or paper pulp are thus separated from the twigs, chips, knots, and other specifically-heavier impurities which collect behind the-bafiies and descend to the.
  • a pipe 5, arrangedin the lower compartment, is quickly opened by means of any well-known device and impurities removed. Tlie impurities already collected in the lower portion escape at once, in consequence of which suction is produced only along the oblique wall at owing to the'rotat- 'ity only when there are such baffies.
  • the baffles 6, arranged on the inner wall of the vessel d, and these bafiles or ribs form an essential feature of the invention, as the lighter fibers having naturally a tendency to rise upward can be separated from the impurities of very slightly greater specific grav-
  • the (knots, chips, and twigs) being driven against the inner walls of the vessel d and against the projecting baffles e by the rotating mix ing device-c rotary motion is impeded and there are formed behind the baffles e eddycurrents and within those the so-called deadspaces, the heavier parts collecting in said spaces or settling against the walls of the vessel (1 and the battles e and sliding down them to the bottom, while only the specificallylighter fibers rise upward.
  • the worm mounted in the lower portion of the vessel on the spindle 1' assists the action of the apparatus, as it causes the substances which have reached the lower portion of the vessel and ceased to rotate to rise again, and the fibers that may have descendedare carried upward and the heavier particles mixed with them driven against the wall and bafiles of the vessel, where the already-described process of separation is repeated.
  • the spindle r is driven by any suitable means-such for instance, as bevel-gearing,
  • the material introduced into the pulp-- dresser according to the present inventioncould be also caused to rotate without the use of the central stirring device by introducing the fluid at the center and causing the whole apparatus to rotate about a vertical central axis.
  • I-c]aim 1 In an apparatus of the character described, the. combination with a conical vessel, of a series of baflies arranged longitudinally of the vessel upon the inner wall there-.
  • said spaces being adapted to intercept and collect heavier particles during the rotation of the contents of the vessel'and prevent such particles rising to the top, and a rotatable shaft arranged centrally of the vessel and a disk secured theretobelow but adjacent to the lower ends of the battles and above the lower open end of the vessel.
  • the combination with a conical was 1 sel, of baffles arranged longitudinally of the vessel upon the inner wall thereof, said baffles converging toward the lower end of the vessel and forming dead-spaces which converge toward said end of the vessel, said spaces being adapted to intercept and collect heavier particles during rotation of the contents of the vessel, and prevent such particles rising to the top, a vessel, ii, arranged below the lower open end of the conical vessel,

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Description

D P ABERG- atented Aug 8, I899 No. 630,309. A I
APPARATUS POR CLEANING PAPER PULP.
(Application filed Dec. 24, 1B97.|
No Modem Hill UNITED STATES PATENT OFFICE...
I ALBERT ABERG, OF PODGOBA, AUSTRIA-HUNGA RY.
APPARATUS FOR CLEANING P PER-Pu LP.
SPECIFICATION formingpart of Letters Patent No. 630,309, dated August 8, 1899/ Application filed December 24, 1897. Serial No. 663,341. (No model.)
To all whom it may concern/.
comes noticeable.
Be it known that I, ALBERT ABERG, manager of the Cellulose \Vorks at Podgora,country of Goerz, Austria, and a resident of Podgora, Empire of Austria-Hungary, have invented certain new and useful Improvements in Apparatus for Cleaning Paper-Pulp or Wood- Pulp, of which the following is a specification.
The object of the present invention is a dresser for cleaning or purifying paper or wood pulp, and comprises a downwardly-tapering or conical vessel into which the paper or wood pulp to be purified is introduced and caused to rotate by any suitable means. In consequence of this rotary motion the good fibers, with which are mixed the chips, twigs, knots, or other impurities, become gradually released and, being of smaller specific gravity than water, rise and overflow at the overflow-outlet at the upper edge of the vessel.
The wood or paperpulp to be purified differs from other mixtures of substances in that the chief constituent parts of the impuritiesthe chips,twigs,or knots-have only a slightlygreater specific gravity than that of the fibers themselves. The knots are of course so light that as long as they are surrounded with fibers they also have the same tendency to rise upward as the fibers. It is only by freeing or separating the fibers that the difference in the specific gravity of knots, twigs, and chips on one hand and fibers on the other hand be- This difference is, how ever, so small that the knots, &c., would rotate around the walls of the vessel and apart of them would even rise unless prevented from so doing. For this purpose I secure battens, bafiles, or ribs to the inner surface" of the vessel at suitable distances apart. mass directly in front of. the baffles is stopped by the latter, the flow of the liquid being impeded and eddy-currents formed behind the bafiles, and so-called dead-spaces being formed in which the specifically-heavier substances are deposited. Particles of the wood or paper pulp that may have descended to the lower portion of the apparatus are caused to rise by means of a rotating worm.
An apparatus according to the present invention is illustrated by way of example in the accompanying drawings, in which- Figure 1 shows the apparatus in longitudi- The nal section, Fig. 2 being a plan, partly in sec tion, through Fig. 1.
The mass is introduced at the top, preferably at the center, into a stone or sand trap (it, (having preferably the shape of a box,) and from which it overflows into the main vessel, stones and heavy foreign substances be ing deposited in the trap. The mass then passes into a lower chamber or deflector 1), ar-
ranged concentrically below the trap, a mixing device 0, rotating in a horizontal plane, causing the fluid mass to rotate. This mixing device may consist of a screw propeller or disk secured on a rotating central spindle r. The funnel-shaped main vessel d is pro vided on its inner walls with slightlyprojecting longitudinal ribs or baffles e, converging toward the center, said baffies producing eddy currents and causing the heavier particles or impurities contained in the pulp to settle. The fibers of the wood or paper pulp are thus separated from the twigs, chips, knots, and other specifically-heavier impurities which collect behind the-bafiies and descend to the.
bottom, the lighter fibers at the same time being caused to rise upward. These fibers rise and are discharged over the overflow edge m into a discharge-conduit n. The upward tendency of the fibers on the one hand and the sinking of the knots and im'purities on the other hand would, however, owing to the small difference of their specific weights, not take place without the addition of a rotating screwor worm g, which again directs the fine fibers upward that may have been carried downward and unless the baffies e intercepted the movement of knots, twigs, chips, and other impurities. These impurities slide down the bafiles into the lower portion 2' of the, vessel. If the latter is to be emptied, a pipe 5, arrangedin the lower compartment, is quickly opened by means of any well-known device and impurities removed. Tlie impurities already collected in the lower portion escape at once, in consequence of which suction is produced only along the oblique wall at owing to the'rotat- 'ity only when there are such baffies. Whole mass of fluid, fibers, and impurities- .the baffles 6, arranged on the inner wall of the vessel d, and these bafiles or ribs form an essential feature of the invention, as the lighter fibers having naturally a tendency to rise upward can be separated from the impurities of very slightly greater specific grav- The (knots, chips, and twigs) being driven against the inner walls of the vessel d and against the projecting baffles e by the rotating mix ing device-c rotary motion is impeded and there are formed behind the baffles e eddycurrents and within those the so-called deadspaces, the heavier parts collecting in said spaces or settling against the walls of the vessel (1 and the battles e and sliding down them to the bottom, while only the specificallylighter fibers rise upward. The worm mounted in the lower portion of the vessel on the spindle 1', assists the action of the apparatus, as it causes the substances which have reached the lower portion of the vessel and ceased to rotate to rise again, and the fibers that may have descendedare carried upward and the heavier particles mixed with them driven against the wall and bafiles of the vessel, where the already-described process of separation is repeated.
The spindle r is driven by any suitable means-such for instance, as bevel-gearing,
as illustrated in Fig. 1.
The material introduced into the pulp-- dresser according to the present inventioncould be also caused to rotate without the use of the central stirring device by introducing the fluid at the center and causing the whole apparatus to rotate about a vertical central axis. A,
I-c]aim 1. In an apparatus of the character described, the. combination with a conical vessel, of a series of baflies arranged longitudinally of the vessel upon the inner wall there-.
of, said bafiiesconverging toward the lower end of the vessel and forming dead-spaces which converge toward said end of the vessel and said spaces being adapted to intercept and collect heavier particles during the rotation of the contents of the vessel and prevent such particles rising to the top.
2. ..In an apparatus of the character described, the combination with a conical vessel, of a series of bafi'les arranged longitudinally of the vessel upon the inner wall thereof, said battles converging toward the lower end of the vessel and forming dead-spaces which converge toward said end of the vessel,
said spaces being adapted to intercept and collect heavier particles during the rotation of the contents of the vessel'and prevent such particles rising to the top, and a rotatable shaft arranged centrally of the vessel and a disk secured theretobelow but adjacent to the lower ends of the battles and above the lower open end of the vessel.
'3. In an apparatus of the character described, the combination with a conical vessel, of a series of baffles arranged longitudinally of the vessel upon the inner wall thereof, said baffles converging toward the lower end or the vessel and forming dead-spaces which converge toward said end of the vessel, said spaces being adapted to intercept and collect heavier particles during the rotation scribed, the combination with a conical was 1 sel, of baffles arranged longitudinally of the vessel upon the inner wall thereof, said baffles converging toward the lower end of the vessel and forming dead-spaces which converge toward said end of the vessel, said spaces being adapted to intercept and collect heavier particles during rotation of the contents of the vessel, and prevent such particles rising to the top, a vessel, ii, arranged below the lower open end of the conical vessel,
a discharge therefor, a shaft arranged centrally of the conical vesseha worm carried by said shaft, and a disk also carried by the shaft below but adjacent to the lower ends of the baffles and over the lower open end of the conical vessel.
IOC
5. In an apparatus or the character described, the combination with a conical vessel, of battles arranged longitudinally of the vessel upon the inner wall thereof, said baffles converging toward the lower end of the vessel and forming dead-spaces which converge toward said end of the vessel, said spacesbeing adapted to intercept and collect heavier particles during rotation of the contents of the vessel and prevent such particles rising to the top, a vessel, 2', arranged below the lower open end of the conical vessel, a discharge therefor, ashaft arranged centrally of the conical vessel, a worm carried by said shaft, a disk carried by the shaft below but adjacent to the lowerends of the baffles, and over the lower open end of the conical vessel, a trap a, the chamber 19, arranged below the trap having an open lower end, and a mixing device carried by the shaft within the open end of said chamber b, all arranged for cooperation as and forthe purposes set forth.
In testimony that I claim the foregoing as my invention I have signed my name in presence of two subscribing witnesses.
- ALBERT ABERG. \Vitnesses:
HENRY SoHMoLKY, ADOLPH, FISCHER.
IIC
IZC
US66334197A 1897-12-24 1897-12-24 Apparatus for cleaning paper-pulp. Expired - Lifetime US630309A (en)

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2425372A (en) * 1943-01-07 1947-08-12 Infilco Inc Apparatus and process for improving separation of clarified liquid from a slurry by maintaining a slurry circulation including a flow of slurry adjacent the separation interface
US2702184A (en) * 1951-10-26 1955-02-15 Du Pont Screw mixer and blender
US2711644A (en) * 1951-05-28 1955-06-28 Edwin D Myers Apparatus for determining and measuring the gas content of soils
US3399770A (en) * 1966-01-19 1968-09-03 Beloit Corp Method for centrifugal separation of particles from a mixture
US3620370A (en) * 1969-06-02 1971-11-16 Rue E Swayze Ore concentrator
US3887456A (en) * 1973-10-01 1975-06-03 James W Loughner Classifier with rifflers and variable throat
US4124497A (en) * 1976-07-02 1978-11-07 Hulegard Trueman L Apparatus for separating mineral and the like from earth and the like
EP1516672A1 (en) * 2003-09-22 2005-03-23 Hans Huber AG Maschinen- und Anlagenbau Apparatus for separating of organic from inorganic material
US20220305448A1 (en) * 2020-07-21 2022-09-29 Hefei General Machinery Research Institute Co., Ltd Integrated production system for ternary material

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2425372A (en) * 1943-01-07 1947-08-12 Infilco Inc Apparatus and process for improving separation of clarified liquid from a slurry by maintaining a slurry circulation including a flow of slurry adjacent the separation interface
US2711644A (en) * 1951-05-28 1955-06-28 Edwin D Myers Apparatus for determining and measuring the gas content of soils
US2702184A (en) * 1951-10-26 1955-02-15 Du Pont Screw mixer and blender
US3399770A (en) * 1966-01-19 1968-09-03 Beloit Corp Method for centrifugal separation of particles from a mixture
US3620370A (en) * 1969-06-02 1971-11-16 Rue E Swayze Ore concentrator
US3887456A (en) * 1973-10-01 1975-06-03 James W Loughner Classifier with rifflers and variable throat
US4124497A (en) * 1976-07-02 1978-11-07 Hulegard Trueman L Apparatus for separating mineral and the like from earth and the like
EP1516672A1 (en) * 2003-09-22 2005-03-23 Hans Huber AG Maschinen- und Anlagenbau Apparatus for separating of organic from inorganic material
US20050061715A1 (en) * 2003-09-22 2005-03-24 Branner Wolfgang Apparatus for separating organic material from inorganic material
US7318527B2 (en) 2003-09-22 2008-01-15 Hans Huber Ag Maschinen-Und Anlagenbau Apparatus for separating organic material from inorganic material
US20220305448A1 (en) * 2020-07-21 2022-09-29 Hefei General Machinery Research Institute Co., Ltd Integrated production system for ternary material
US12053750B2 (en) * 2020-07-21 2024-08-06 Hefei General Machinery Research Institute Co., Ltd Processing system with agitated nutsche filter and conical double helix dryer

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