US3206917A - Deaerated stock flow control - Google Patents

Deaerated stock flow control Download PDF

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Publication number
US3206917A
US3206917A US142987A US14298761A US3206917A US 3206917 A US3206917 A US 3206917A US 142987 A US142987 A US 142987A US 14298761 A US14298761 A US 14298761A US 3206917 A US3206917 A US 3206917A
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United States
Prior art keywords
stock
receiver
pond
chamber
deaerated
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Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
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US142987A
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English (en)
Inventor
Robert G Kaiser
John C Stewart
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Clark and Vicario Corp
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Clark and Vicario Corp
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Publication date
Application filed by Clark and Vicario Corp filed Critical Clark and Vicario Corp
Priority to US142987A priority Critical patent/US3206917A/en
Priority to SE10525/62A priority patent/SE317254B/xx
Priority to FI1765/62A priority patent/FI43675B/fi
Priority to JP37042722A priority patent/JPS4827204B1/ja
Priority to DK427662AA priority patent/DK115897B/da
Priority to AT781562A priority patent/AT252709B/de
Priority to NO145949A priority patent/NO131467C/no
Priority to GB37573/62A priority patent/GB975207A/en
Application granted granted Critical
Publication of US3206917A publication Critical patent/US3206917A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D19/00—Degasification of liquids
    • B01D19/0042—Degasification of liquids modifying the liquid flow
    • B01D19/0047—Atomizing, spraying, trickling
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
    • D21D5/00—Purification of the pulp suspension by mechanical means; Apparatus therefor
    • D21D5/26—De-aeration of paper stock

Definitions

  • This invention relates to papermaking, and concerns apparatus and method for :assuring a substantially constant flow of deaerated papermaking stock, which may also be de-dirted, ⁇ from a deaerating station.
  • an aqueous suspension of cellulosic papermaking stock is fed to the headbox f a papermaking machine, whence the stock is supplied to the wire of the machine. It is important that the ilow of stock to the headbox be carefully regulated .and substantially uniform, else the weight and caliper of the paper made by the machine is subject to unacceptable variation. Particularly with the advent of increasingly rapid machine speeds, the necessity for more accurate control assuring constant flow of stock to the headbox has become of commensurately greater importance.
  • valvinlg in the discharge pipe connecting receiver and headbox may be connected with displacement iioats or the like Within the receiver in an .attempt to maintain a constant level of stock in the receiver, but it is found that such control valves tend to be in substantially constant motion, and .the system tends continually to .overcor'rect and to under-correct, causing significant variation in dow.
  • the present invention provides a solution to this problem and assures a substantially constant flow of papermaking stock from a deaerated station operating under substantially less than atmospheric pressure.
  • a feature xof the invention is maintenance of a substantially constant level of stock in the receiver for supply to the headbox.
  • Correlated improvements and advantages include means for rejecting foam, scum, and other undesirable fractions residing on the surface of the stock in ⁇ the receiver.
  • a particularly important advantage of the present invention is that it permits simple and rapid changeover by the paperm-aker from a given grade ⁇ or weight of paper to one of a different grade. Such changeovers may inice volve altering significantly the volume of stock fed to the headbox; presently known control systems must be manually and empirically adjusted to compensate for such substantial changes in iiow, but the method and apparatus of the present invention rapidly and .automatically accommodate changes in volume of the magnitude referred to.
  • the transient period of level instability is greatly reduced and a stable operating level in the receiver is achieved in the shortest possible time. The resultant saving in time alone is of appreciable economic importance.
  • an enclosed stock receiver in a deaerating station is equipped with evacua-ting means, suitably a vacuum pump, to maintain the receiver under substantially less than atmospheric pressure.
  • the receiver cooperates with means admitting feed stock thereto as .an atomized spray and is adapted to collect the resultant deaerated stock ina pond within said receiver.
  • Means are provided to withdraw product deaerated stock from the pond within the receiver.
  • Weir means are provided Withinthe receiver and .are positioned with the upper terminus 4of the Weir at or slightly below the desired level of the pond of product deaerated stock within the receiver in such manner that excess product stock above the desired pond level overflows the Weir.
  • a closed chamber having a capacity substantially less than that of the receiver communicates with the receiver a-nd is adapted t-o receive and pool stock overflowing the weir for recycling.
  • Recycle stock return means are provided to convey the recycle stock from the pool in the closed chamber to the receiver. At least a slight excess of feed stock is supplied to the receiver over that which is withdrawn as product deaerated stock, resulting in continual overflow of excess stock to the chamber for recycling.
  • Means are provided to regulate the rate of flow of the recycle stock from the chamber to the receiver responsively to the level of the recycle stock pool in the chamber, suitably by employment of recycle stock pool level sensing means operatively connected lto valve means located in the recycle stock return means conveying the recycle stock to the receiver. ln this manner the level of the recycle stock pool is held substantially constant at a predetermined level or within predetermined lim-its.
  • the total volume of feed stock to the receiver fresh stock plus recycle stock
  • an increase in the volume of recycle stock be accompanied by a decrease in the amount of fresh stock supplied, and conversely. This may be accomplished in accordance with the invention by supplying recycle stock to the intake side of the feed pump at a point ahead of the fresh stock intake.
  • Variations in flow of product deaerated stock from the receiver are principally due to an inconstant level of product stock forming the pond in the receiver, either through inadequate regulation or through hunting or other iiuctuation as control devices measure the pond level and seek to restore or maintain the proper level by continually compensating for changes.
  • the present invention maintains the level of the pond of stock substantially constant at or slightly above the predetermined height of the upper terminus of the Weir, and avoids pond level sensing devices and associated control equipment and consequently avoids such seeking. Under equilibrium conditions the rate of excess stock overflowing the Weir is constant, as is the level of recycle stock in the chamber.
  • Imbalance in the system (e.g., when the discharge rate is altered) is rapidly and automatically corrected either by an increase or decrease in the recycle rate, and the variationin pond level within the receiver is merely the vvariation in head overflowing the weir, at most an inch or so.
  • the volume of overow stock while small in relation to the high capacity receiver, is large in relation to the small capacity chamber and causes a correspondingly significant in recycle stock pool level.
  • the effect of change of pond level within the receiver is thus magnified in the pooled recycle stock level within the chamber, and correction is rapidly and automatically made by responsive alteration of the recycle rate.
  • the magnitude of any permitted variation in flow rate from the receiver pond is extremely small, and the variation itself is promptly eliminated.
  • FIG. 1 is a schematic representation of a control system in accordance with the invention
  • FIGS. 2, 3 and 4 show equivalent arrangements of the weir means within receiver
  • FIGS. 5 and 6 illustrate a preferred nozzle for introducing stock into the receiver
  • FIGURE 7 is a schematic representation of an alternative arrangement of a control system similar to that shown in FIGURE l.
  • a stock deaerating station 16 is provided with an enclosed receiver 1 connected through port 2 to suitable vacuum-inducing means for maintaining the interior of the receiver under substantially less than atmospheric pressure.
  • Pump 4 draws dilution white water from wire pit or silo 3 and new thick stock from stock preparation chest or other source 42 in desired proportion by appropriate adjustment of values or other means of regulation (not shown) in accordance with known practice.
  • the resulting mixture is pumped through conduit 30 to header 43 for introduction to receiver 1.
  • Feed stock is atomized into receiver 1 from header 43 by appropriate nozzles, suitably of the type shown in FIGS. 5 and 6.
  • FIG. 1 are shown hydrocyclones 5, which de-dirt the feed stock and atomize it into receiver 1 through inlet pipes 31.
  • the nozzle of FIG. 5 may be substituted for ⁇ hydrocyclones 5, or the stock may be directly admitted to the receiver through inlet pipes 31, so long as the feed stock is atomizingly admitted. Deaerating conditions are enhanced by the use of nozzles or hydrocyclones.
  • a pond or reservoir 19 of deaerated stock is collected in receiver 1.
  • Inlet pipes 31 extend upwardly through pond 19 and admit atomized feed stock above the level 8 of pond 19.
  • Product stock is withdrawn from receiver 1 through port 10, located at or near the bottom of receiver 1, by conduit 11 and pump 12 is fed through conduit 25 to headbox 13 and thence to the wire 14 of a papermaking machine.
  • Papermakers valve 26 is located in conduit and permits regulation of the rate of ow of stock by the papermaker according to the demand for the particular weight of paper being made.
  • At least a slightly greater amount of stock is fed to Y the receiver through header 43 and inlet pipes 31 than is withdrawn through port 10. Conveniently, the feed may be slightly greater than the maximum demand of the papermaking machine. Valve 29 in conduit 30 may be employed to regulate the flow of feed stock to the appropriate or desired volume. f
  • receiver 1 There is provided within receiver 1 a weir 6, the Weir being so positioned as to permit excess stock to overflow its upper terminus 9 for recycling. Recycle stock overflowing the Weir passes to chamber 7, which is adapted to receive and pool overflow stock. Recycle stock from chamber 7 is returned at a controlled rate to receiver 1, as hereinafter more fully appears.
  • chamber 7 is shown communicating by means of a conduit 60 to the intake side of pump 15. Alternatively, if desired, chamber 7 may communicate by a barometric drop leg to the intake side of pump 4 for regulated return of overiiow stock to the receiver, as shown in FIG. 7.
  • sensing means 17 may be any of a variety of devices, illustratively a iioat, differential pressure cell, or the like.
  • the sensing means 17 may conveniently operate through control instrument 18 by pneumatic or electrical means 44 and 45 to regulate valve 21 responsively to changes in the level of the pool recycle stock within chamber 7 to maintain that level substantially constant or within predetermined limits.
  • recycle stock is conveyed from chamber 7 through conduit 20 to the intake side of feed-pump 4, which supplies stock to receiver 1.
  • feed-pump 4 which supplies stock to receiver 1.
  • FIG. 4 shows an alternative embodiment of an overiiow Weir of the type shown in FIG. 1.
  • a weir 6 having an upper terminus 9 is provided as before, with the addition of a baiiie plate 22 extending downwardly from a point above weir 6, said baffle plate 22 terminating below the level 8 of the stock in the receiver 1.
  • the stock in receiver 1 which overflows the top 9 of Weir 6 is'thus drawn from a point below the surface 8 of the stock. In this manner scum and other undesirable surface matter not drawn off to chamber 7, and possible interference with the operation of pump 15 and other pumps which may be employed in the system is thereby avoided.
  • a venting aperture (not shown) is provided in baflie 22 and located at a point well above level 8 of the stock in receiver 1 to equalize pressure on either side of the bafiie.
  • Baffle 22 serves also to prevent stock spray 24 emitted from inlet pipe 31 from being diverted into chamber 7 and is particularly useful where a plurality of inlets are provided to admit stock to receiver 1.
  • FIGS. 5 and 6 A preferred nozzle for use in conjunction with inlet pipes 31 for introducing the feed stock to receiver'l as a spray is shown in FIGS. 5 and 6 and comprises a hollow truncated cone 50 having a solid base 51 and an open top 52 adapted to fit inlet pipe 31.
  • Supply pipe 53 adapted to convey feed stock to the nozzle from header 43, is fitted to cone 50 so that entering stock will be admitted under pressure tangentially.
  • the feed stock cyclonically rises through the nozzle and feed pipe 31 and atomizingly enters the receiver.
  • valve 26 Assuming that the papermaker desires to increase the consistency of the furnish to the headbox, he will manually or otherwise partially close papermakers valve 26. As a result less stock is drawn from receiver 1 through port 10 and an imbalance in liow rates results. An in creased amount of stock overilows the upper terminus 9 of weir 6 into chamber 7, and the consequent rise in the level of the recycle stock pool in chamber 7 is detected by sensor 17. Valve 21 in conduit 20 in the efuent side of pump 15 opens responsively to the rise of the recycle stock pool level in chamber 7, permitting recycle stock to ilow from the chamber at a greater rate. The recycle stock is fed back to receiver 1 through pump 4, a lesser amount of white water being drawn from wire pit 3. Should control 18 have overcompensated so that the level of the pool in chamber 7 falls below a predetermined level, valve 21 will be responsively closed partially. In this manner the level of the recycle stock pool in leg 7 is held at a predetermined point or within predetermined limits.
  • the present invention serves to maintain a constant level of stock in receiver 1 when the system is in equilibrium, and it further causes the system repaidly to be restored to equilibrium when such equilibrium is disrupted as by a change in setting of papermakers valve 26. Achieving a new balance of ilow to the papermaking machine requires a discrete amount of time, during which no useful production can be achieved. It is consequently of great importance that the system of the present invention rapidly restores the system to equilibrium.
  • receiver 1 has a diameter of 6 feet and a length of 14 feet and a pond capacity of 3500 gallons.
  • the upper terminus 9 0f weir 6 is located approximately 3 inches below the center line of the receiver.
  • the maximum liquid level over the top of the weir is approximately 6 inches, and the minimum approximately 1 inch, with the normal liquid level approximately 3 inches above the top of the Weir.
  • the pool capacity of the chamber 7 is about 250 gallons.
  • the average ilow of stock over the weir into chamber 7 is approximately 10-15% of the total flow and the balance of ow through port 10 to pump 12 is about 85-90% of the total flow.
  • FIGS. 2 and 3 are shown equivalent arrangements of weir means within the receiver.
  • the weir is probe-shaped and its upper surface 9 may have a channel or may be provided with slots or holes through which recycle stock flows to chamber 7.
  • Sensor 17 is provided to sense the level of the pool of recycle stock in chamber 7.
  • FIG. 3 chamber 7 is located within receiver 1 and the weir 6 is provided with apertures communicating with the chamber to permit accesses of recycle stock thereto.
  • Sensor 17 is indicated as mounted on the outside wall of the receiver but communicating with chamber 7 to sense the level of the pool of recycle stock therein.
  • FIG. l An optional arrangement is shown in FIG. l whereby a conduit 2S shunts a portion of the product deaerated stock from conduit 25 to the intake side of pump 4, the amount so diverted being regulated by valve 27.
  • Stock so delivered is recycled to receiver 1 and the use of a portion of the product stock for recycle decreases the amount of the recycle stock overflowing weir 6 and passing through pump 15.
  • This arrangement takes part of the load orT pump 15 and permits use of a less expensive, lower capacity pump in the 15 position.
  • a method of treating papermaking stock suspension which comprises admitting an air-containing aqueous suspension of papermaking stock as an atomized spray to an evacuated space within an enclosed stock receiver maintained under a vacuum sutlicient to deaerate stock sprayed thereinto, collecting stock suspension thereby deaerated as a pond in the receiver, withdrawing, deaerated stock suspension from the pond at a lesser rate than the rate at which the aqueous stock suspension is admitted to the receiver, conveying the deaerated stock suspension withdrawn from the pond to a point of use, maintaining the pond of collected deaerated stock suspension at a constant level by weir means dening the maximum height of the pond, and recycling suspension overowing the Weir to the pond in the receiver.
  • a method for providing a constant flow of deaerated aqueous papermaking stock from a stock deaerating station which comprises maintaining an enclosed stock receiver under a vacuum suicient to deaerate papermaking stock subsequently sprayed thereinto, pumping a mixture of fresh air-containing aqueous papermaking stock and a recycle stock to the receiver and spraying said stock mixture into the upper portion of the receiver, collecting the stock sprayed into the receiver as a pond within the lower portion of the receiver, withdrawing collected stock from the pond at a lesser rate than the rate at which stock is sprayed into the receiver and conveying the withdrawn collected stock to a point of use, admitting stock from the pond overllowing a weir within the receiver to a chamber also maintained under vacuum suicient to deaerate papermaking stock, withdrawing overowed stock from the chamber and returning the Withdrawn overlowed stock to the receiver as the recycle stock and mixing the withdrawn overowed stock with fresh air-containing aqueous papermaking stock to provide the mixture being pumped to the
  • Apparatus for providing a constant ow of deaerated aqueous papermaking stock to a point of use comprising an enclosed stock receiver adapted to collect deaerated papermaking stock as a pond therein and provide a space above the pond, evacuating means in communication with the space above the pond in said receiver for maintaining the receiver under a vacuum suiiicient to deaerate papermaking stock subsequently sprayed there into, means for spraying air-containing aqueous papermaking stock into the evacuated space in said receiver, means for withdrawing deaerated stock collected as a pond in said receiver and for conveying the withdrawn stock to said point of use, means communicating with the receiver for withdrawing stock from the pond including weir means maintained under a vacuum suiTicient to deaerate paper making stock by said evacuating means defining the maximum height of the pond of collected stock, and means for returning stock overflowing said Weir means to the pond of deaerated stock collected in said receiver.
  • the means for returning stock overiiowing said weir Ameans to the pond of deaerated stock collected in said receiver includes pump means, a barometric drop leg connecting said receiver to the input side of said pump means and adapted to convey stock overflowing said Weir means to said pump means, and conduit means connecting the output side of said pump means to said means for spraying air-containing aqueous papermaking stock into the evacuated space in said receiver.
  • the means for returning stock overowing said Weir means to the pond of deaerated stock collected in said receiver includes rst pump means, iirst conduit means connecting said receiver to the intake side of said first pump means and adapted to convey stock overflowing said weir means to said iirst pump means, second pump means, second conduit means connecting the output side of said rst pump means to the input side of said second pump means, and third conduit means connecting the output side of said second pump means to said spraying means.
  • Apparatus according to claim 3 including bathe means cooperating with said Weir means to prevent surface stock, foam and spray from overiiowing said weir means.
  • Apparatus for providing a constant flow of deaer ated papermaking stock from a stock deaerating station comprising an enclosed stock receiver, evacuating means in communication with the upper interior portion of said receiver lfor maintaining said receiver under a vacuum suiiicienty to deaerate papermaking stock sprayed thereinto, means for spraying papermaking stock into the upper portion of said receiver, compartment means in the lower portion of said receiver adapted to collect as a pond stock sprayed into the upper portion of said receiver, means for withdrawing stock from the pond thereof collected in said compartment means and for conveying stock so Withdrawn to a point of use, a chamber closed to the atmosphere and maintained under vacuum suiiicient to deaerate papermaking stock by said evacuating means, means deiining a flow way between the receiver compartment means and the chamber including Weir means permitting overiiow ⁇ of stock from the pond to the chamber, and means for returning overiiowed stock from the chamber to the receiver compartment means.
  • Apparatus according to claim 7 including baiiie means cooperating with said weir means to prevent surface stock, foam and spray from overflowing said weir means.
  • Apparatus for providing a constant flow of deaerated aqueous papermaking stock from a stock deaerating station comprising an enclosed stock receiveradapted to collect deaerated stock as a pond therein, evacuating means in communication with said receiver for maintaining the receiver under a vacuum suiiicient to deaerate papermaking stock subsequently sprayed thereinto, means for spraying air-containing aqueous papermaking stock into said receiver above the pond of deaerated stock collected therein and cooperating stock-feeding pump means and associated conduit means for conveying air-containing aqueous papermaking stock to said spraying means, a discharge conduit from said receiver for withdrawing and conveying to a point of use deaerated stock from the pond thereof collected in said receiver, weir means ⁇ in said receiver having an upper terminus slightly below the desired level of the pond of collected deaerated stock, a chamber closed to the atmosphere and maintained under vacuum by said evacuating means and communicating with said receiver and adapted to receive and collect as a
  • Apparatus for providing a constant flow of deaerated aqueous papermaking stock from a stock deaerating station to a point of use comprising an enclosed stock receiver adapted to collect deaerated stock as a pond in its lower portion, evacuating means in communication with the upper portion of said receiver for maintaining the receiver under a vacuum sufficient to deaerate papermaking stock subsequently sprayed thereinto, hydrocyclone means adapted to classify aqueous papermaking stock into dirt-rich and dirt-poor fractions and spray the dirt-poor fraction into the upper portion of said receiver, stockeeding pumpvmeans and cooperating conduit means for supplying air-containing aqueous papermaking stock to said hydrocyclone means, conduit means from said receiver and cooperating pump means and ⁇ valve means for regulatably conveying deaerated stock from a pond thereof cggected in the lower portion of said receiver to said point of use, a chamber closed to the atmosphere and maintained under vacuum sufficient to deaerate papermaking stock by said evacuating means,

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Paper (AREA)
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US142987A 1961-10-04 1961-10-04 Deaerated stock flow control Expired - Lifetime US3206917A (en)

Priority Applications (8)

Application Number Priority Date Filing Date Title
US142987A US3206917A (en) 1961-10-04 1961-10-04 Deaerated stock flow control
SE10525/62A SE317254B (enrdf_load_stackoverflow) 1961-10-04 1962-10-01
JP37042722A JPS4827204B1 (enrdf_load_stackoverflow) 1961-10-04 1962-10-02
FI1765/62A FI43675B (enrdf_load_stackoverflow) 1961-10-04 1962-10-02
DK427662AA DK115897B (da) 1961-10-04 1962-10-03 Apparat til tilvejebringelse af en praktisk taget konstant strom af vandig papirmasse.
AT781562A AT252709B (de) 1961-10-04 1962-10-03 Verfahren und Vorrichtung zur gleichmäßigen Beschickung von Papiermaschinen
NO145949A NO131467C (enrdf_load_stackoverflow) 1961-10-04 1962-10-03
GB37573/62A GB975207A (en) 1961-10-04 1962-10-04 Deaerated stock flow control

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Application Number Priority Date Filing Date Title
US142987A US3206917A (en) 1961-10-04 1961-10-04 Deaerated stock flow control

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US3206917A true US3206917A (en) 1965-09-21

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US142987A Expired - Lifetime US3206917A (en) 1961-10-04 1961-10-04 Deaerated stock flow control

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US (1) US3206917A (enrdf_load_stackoverflow)
JP (1) JPS4827204B1 (enrdf_load_stackoverflow)
AT (1) AT252709B (enrdf_load_stackoverflow)
DK (1) DK115897B (enrdf_load_stackoverflow)
FI (1) FI43675B (enrdf_load_stackoverflow)
GB (1) GB975207A (enrdf_load_stackoverflow)
NO (1) NO131467C (enrdf_load_stackoverflow)
SE (1) SE317254B (enrdf_load_stackoverflow)

Cited By (34)

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US3421622A (en) * 1965-08-19 1969-01-14 Nichols Eng & Res Corp Cleaning and deaerating paper pulp suspensions
US3432036A (en) * 1964-12-09 1969-03-11 Clark & Vicario Corp Conditioning papermaking stock
US3472371A (en) * 1966-10-04 1969-10-14 Ronald Percy Ayerst Sorting fibrous material
US3488927A (en) * 1967-10-23 1970-01-13 Shell Oil Co Gas-liquid cyclone separator
US3513971A (en) * 1967-02-17 1970-05-26 Nils Anders Lennart Continuous method for degasifying and cleaning aqueous suspensions of fibrous materials
US3538680A (en) * 1967-12-29 1970-11-10 Clark & Vicario Corp Papermaking apparatus and process
US3735869A (en) * 1970-10-29 1973-05-29 Union Carbide Corp Cyclone particle separator
US3779863A (en) * 1969-02-18 1973-12-18 Asea Ab Stock flow control system for feeding a paper machine headbox
US3833468A (en) * 1971-08-27 1974-09-03 Dorr Oliver Inc System for recovery of fiber from paper mill effluent, including a sieve bend screen
DE2950194A1 (de) * 1978-12-14 1980-06-19 Clark & Vicario Corp Verfahren und vorrichtung zum sammeln einer fluessigkeit an einem ort und zum foerdern der fluessigkeit zur verwendung an einem zweiten ort
US4238208A (en) * 1977-11-24 1980-12-09 Ab Celleco Apparatus for degassing paper stock
US4364822A (en) * 1981-04-13 1982-12-21 Rich Jr John W Autogenous heavy medium process and apparatus for separating coal from refuse
US4419109A (en) * 1981-06-05 1983-12-06 Enso-Gutzeit Oy Means for degassing paper pulp stock
US4443232A (en) * 1982-09-29 1984-04-17 Clark & Vicario Corporation Deaerated liquid stock supply
US4478615A (en) * 1982-09-29 1984-10-23 Clark & Vicario Corporation Deaerated liquid stock supply
US5084161A (en) * 1988-07-12 1992-01-28 A. Ahlstrom Corporation Method and apparatus for the removal of light material from a fiber suspension
US5186726A (en) * 1990-05-11 1993-02-16 Ahlstromforetagen Swenska Suspension deaerating process
US5203890A (en) * 1989-08-07 1993-04-20 Okabe Tatsuo Deaerator for removing dissolved oxygen in water
DE4234522A1 (de) * 1991-10-16 1993-04-22 Ahlstroem Oy Entgasungsbehaelter
US5236475A (en) * 1992-11-19 1993-08-17 Lake Superior Paper Industries Papermaking apparatus including baffles
US5268077A (en) * 1991-02-27 1993-12-07 Sulzer Esher Wyss Gmbh Apparatus and method for deaerating or degassing a paper stock suspension
US5819955A (en) * 1993-08-06 1998-10-13 International Fluid Separation Pty Linited Hydrocyclone separators
US5868905A (en) * 1997-04-23 1999-02-09 Voith Sulzer Paper Technology North Amrica Inc. Paper-making machine including a deaerator for a fiber suspension
US5948279A (en) * 1997-09-25 1999-09-07 Ohio University Method and apparatus for controlling macrofoulers in on-demand water conduits
US6096120A (en) * 1995-10-24 2000-08-01 Ahlstrom Machinery Oy Deaeration vessel
US6416632B1 (en) * 1998-01-30 2002-07-09 Metso Paper, Inc. Apparatus for degassing an aqueous suspension containing pulp fibers
US6491744B2 (en) * 2000-04-05 2002-12-10 Voith Paper Patent Gmbh Device for deaerating of fiber stock suspensions
US20030015304A1 (en) * 2001-07-02 2003-01-23 Karl-Heinz Beuermann Method and device for degassing a suspension, specifically a fiber stock suspension
WO2003023135A1 (en) * 2001-09-07 2003-03-20 Metso Paper, Inc. Deaeration arrangement in connection with a paper machine or equivalent
US20040060680A1 (en) * 2000-12-29 2004-04-01 Matti Hietaniemi Apparatus for passing stock into a headbox of a paper machine or equivalent
US6733629B1 (en) * 1999-08-23 2004-05-11 Andritz Oy Method of controlling the operation of an approach system of a paper machine or the like web formation apparatus
US20050139529A1 (en) * 2003-05-20 2005-06-30 Voith Paper Patent Gmbh Plant for cleaning and degassing a fibrous suspension
US20100126686A1 (en) * 2007-04-03 2010-05-27 Andritz Oy Apparatus for removing gas in connection with a paper machine or corresponding
US20210238804A1 (en) * 2016-09-01 2021-08-05 Essity Hygiene And Health Aktiebolag Process and apparatus for wetlaying nonwovens

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DE102016203280A1 (de) * 2016-02-29 2017-08-31 Voith Patent Gmbh Entgasungsvorrichtung

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US4238208A (en) * 1977-11-24 1980-12-09 Ab Celleco Apparatus for degassing paper stock
DE2950194A1 (de) * 1978-12-14 1980-06-19 Clark & Vicario Corp Verfahren und vorrichtung zum sammeln einer fluessigkeit an einem ort und zum foerdern der fluessigkeit zur verwendung an einem zweiten ort
US4364822A (en) * 1981-04-13 1982-12-21 Rich Jr John W Autogenous heavy medium process and apparatus for separating coal from refuse
US4419109A (en) * 1981-06-05 1983-12-06 Enso-Gutzeit Oy Means for degassing paper pulp stock
US4443232A (en) * 1982-09-29 1984-04-17 Clark & Vicario Corporation Deaerated liquid stock supply
JPS5982908A (ja) * 1982-09-29 1984-05-14 クラ−ク・アンド・ビカリオ・コ−ポレ−シヨン 脱気原料を加工機に供給する装置
US4478615A (en) * 1982-09-29 1984-10-23 Clark & Vicario Corporation Deaerated liquid stock supply
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US5268077A (en) * 1991-02-27 1993-12-07 Sulzer Esher Wyss Gmbh Apparatus and method for deaerating or degassing a paper stock suspension
DE4234522A1 (de) * 1991-10-16 1993-04-22 Ahlstroem Oy Entgasungsbehaelter
DE4234522C2 (de) * 1991-10-16 1998-06-04 Ahlstrom Machinery Oy Entgasungsbehälter
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US5819955A (en) * 1993-08-06 1998-10-13 International Fluid Separation Pty Linited Hydrocyclone separators
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US5868905A (en) * 1997-04-23 1999-02-09 Voith Sulzer Paper Technology North Amrica Inc. Paper-making machine including a deaerator for a fiber suspension
US5948279A (en) * 1997-09-25 1999-09-07 Ohio University Method and apparatus for controlling macrofoulers in on-demand water conduits
US6416632B1 (en) * 1998-01-30 2002-07-09 Metso Paper, Inc. Apparatus for degassing an aqueous suspension containing pulp fibers
US6733629B1 (en) * 1999-08-23 2004-05-11 Andritz Oy Method of controlling the operation of an approach system of a paper machine or the like web formation apparatus
US6491744B2 (en) * 2000-04-05 2002-12-10 Voith Paper Patent Gmbh Device for deaerating of fiber stock suspensions
US20040060680A1 (en) * 2000-12-29 2004-04-01 Matti Hietaniemi Apparatus for passing stock into a headbox of a paper machine or equivalent
US7101418B2 (en) * 2001-07-02 2006-09-05 Voith Paper Patent Gmbh Method and device for degassing a suspension, specifically a fiber stock suspension
US20030015304A1 (en) * 2001-07-02 2003-01-23 Karl-Heinz Beuermann Method and device for degassing a suspension, specifically a fiber stock suspension
EP1273697A3 (de) * 2001-07-02 2003-07-23 Voith Paper Patent GmbH Verfahren und Vorrichtung zum Entgasen von Suspension, insbesondere von Faserstoffsuspension
WO2003023135A1 (en) * 2001-09-07 2003-03-20 Metso Paper, Inc. Deaeration arrangement in connection with a paper machine or equivalent
US20050139529A1 (en) * 2003-05-20 2005-06-30 Voith Paper Patent Gmbh Plant for cleaning and degassing a fibrous suspension
US7214257B2 (en) * 2003-05-20 2007-05-08 Voith Paper Patent Gmbh Plant for cleaning and degassing a fibrous suspension
US20100126686A1 (en) * 2007-04-03 2010-05-27 Andritz Oy Apparatus for removing gas in connection with a paper machine or corresponding
US8157966B2 (en) * 2007-04-03 2012-04-17 Andritz Oy Apparatus for removing gas in connection with a paper machine or corresponding
US20210238804A1 (en) * 2016-09-01 2021-08-05 Essity Hygiene And Health Aktiebolag Process and apparatus for wetlaying nonwovens
US11807986B2 (en) * 2016-09-01 2023-11-07 Essity Hygiene And Health Aktiebolag Process and apparatus for wetlaying nonwovens

Also Published As

Publication number Publication date
FI43675B (enrdf_load_stackoverflow) 1971-02-01
SE317254B (enrdf_load_stackoverflow) 1969-11-10
NO131467B (enrdf_load_stackoverflow) 1975-02-24
AT252709B (de) 1967-03-10
DK115897B (da) 1969-11-17
JPS4827204B1 (enrdf_load_stackoverflow) 1973-08-20
GB975207A (en) 1964-11-11
NO131467C (enrdf_load_stackoverflow) 1975-06-04

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