US20050224204A1 - Method and arrangement for controlling short circulation in a paper machine or the like - Google Patents

Method and arrangement for controlling short circulation in a paper machine or the like Download PDF

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Publication number
US20050224204A1
US20050224204A1 US10/467,637 US46763703A US2005224204A1 US 20050224204 A1 US20050224204 A1 US 20050224204A1 US 46763703 A US46763703 A US 46763703A US 2005224204 A1 US2005224204 A1 US 2005224204A1
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Prior art keywords
fiber
consistency
containing pulp
white water
diluted
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Abandoned
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US10/467,637
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English (en)
Inventor
Matti Hietaniemi
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.)
Valmet Automation Oy
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Metso Automation Oy
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Assigned to METSO AUTOMATION OY reassignment METSO AUTOMATION OY ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: HIETANIEMI, MATTI
Priority to US11/211,760 priority Critical patent/US7566382B2/en
Publication of US20050224204A1 publication Critical patent/US20050224204A1/en
Abandoned legal-status Critical Current

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    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21G—CALENDERS; ACCESSORIES FOR PAPER-MAKING MACHINES
    • D21G9/00—Other accessories for paper-making machines
    • D21G9/0009—Paper-making control systems
    • D21G9/0027—Paper-making control systems controlling the forming section
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F1/00—Wet end of machines for making continuous webs of paper
    • D21F1/08—Regulating consistency
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F1/00—Wet end of machines for making continuous webs of paper
    • D21F1/66—Pulp catching, de-watering, or recovering; Re-use of pulp-water

Definitions

  • the present invention relates to a method and arrangement for controlling the short circulation in a paper machine or the like, as defined in the preambles of the independent claims presented below.
  • the short circulation in a paper machine includes especially the following stages:
  • the pulp fed from the headbox of a paper machine onto the wire contains, in addition to the actual fiber material consisting of long fibers, a large amount of other solids, such as fiber-based fines and filler.
  • Filler is added to the pulp to improve the properties of the paper, such as paper formation, surface properties, opacity, brightness and printability, and to lower the paper manufacturing costs.
  • various minerals can be used, such as kaolin, calcium carbonate, titanium oxide or talc.
  • the fiber-based fines originate from the virgin stock conveyed to the paper machine and from the broke pulp added to the virgin stock.
  • the amount of fines varies due to variations in the process conditions or the quality of the fiber material fed. Variations in the amount of fiber-based fines in high-consistency stock chiefly derive from the disc filter, but changes in the composition of the broke added to the pulp and in the grinding of the virgin stock also have an effect. Fines refers to material that passes through a 200 mesh wire or that has a length of ⁇ 1 mm, typically ⁇ 0.2 mm.
  • the filler particles and fiber-based fines do not flow with the water through the fiber network forming on the wire and through the wire itself, they are bound to the fiber material by means of retention aids, such as polyacrylamide. Because of this, the properties of the paper, such as the amount of filler and fiber-based fines in the paper, can be controlled by regulating the feed of retention aid.
  • the retention aid is fed into the diluted pulp being fed into the headbox typically in the vicinity of the machine screen, but it may also be fed elsewhere.
  • the conventional method for monitoring the wire retention of paper and board machines is based on sampling and laboratory determination of consistencies. This method is sufficiently accurate as such, but the procedure is time-consuming and rather laborious. Analyses are probably made at intervals of a few hours. Information obtained after several hours' delay does not provide the required information on the process status at a particular time. This type of monitoring does not, therefore, allow active control of the process.
  • Retention control has also been successfully combined with multivariable control, in which variations in ash can also be controlled.
  • multivariable control in which variations in ash can also be controlled.
  • From international patent application WO 99/27182 it is known, for example, to adjust the properties of paper by controlling simultaneously the flow of the retention aid on the basis of the measurement of the variable describing the amount of filler in the white water, and the flow of filler on the basis of the measurement for the ash content of the paper and/or pulp. Since it has thereby also been possible to measure the ash content of the high-consistency pulp, it has been possible to combine the ash disturbances in the high-consistency pulp with filler feed regulation. The above-mentioned measurements and controls are, however, not always sufficient for retention control.
  • Patent publication EP 62620 discloses a method for measuring the amount of fiber-based fines.
  • the pulp grinding process can be controlled on the basis of the measurement.
  • Control of retention or the amount of filler based on measurements made from the white water or paper is based on measurements that are incorporated in the process at too late a stage for faults in the machine to be corrected quickly before web formation.
  • a fault in the amount of fines appears as changes, for example, in the ret ntion, basis weight and moisture content of the paper.
  • the aim of the present invention is to provide an improved method and arrangement for controlling the short circulation in a paper machine or the like.
  • the aim is then also to provide a method and arrangement by means of which the required change in retention aid and/or filler feed in the short circulation can be predicted.
  • a further aim is to provide a method and arrangement that make possible multivariable control with improved retention and/or white water consistency control.
  • the invention relates to an arrangement at the wet end of a paper machine or the like, in the short circulation of the machine, in which pulp diluted with white water from high-consistency fiber-containing pulp, so-called thick stock, is conveyed to the headbox, to which diluted pulp is typically added a retention aid, such as polyacrylamide or other agent affecting retention, for retaining the fiber-containing fines which are contained in the pulp, and other fines, typically a filler improving the properties of the pulp.
  • a retention aid such as polyacrylamide or other agent affecting retention
  • the process at the wet end and the properties of the diluted fiber-containing pulp to be conveyed to the headbox can be controlled in a known manner by control means based on consistency measurements or determinations performed in the paper, high-consistency fiber-containing pulp, diluted fiber-containing pulp and/or the white water.
  • the solution according to the invention can, therefore, typically be applied in controlling the short circulation to control retention in such a way that
  • the invention can thus be applied in such a way that the amount of fiber-based fines to be retained is measured at such an early stage that there will be time to correct possible fault situations on the basis of the measurement, in other words, there will be time to control the retention aid or filler feed to correspond to the new situation before the fault reaches the headbox.
  • the change in the retention aid feed and/or filler feed is advantageously to take place at the point of time when the change in fiber-based fines in the pulp flow has proceeded to the retention aid or filler feed point.
  • the aim is to keep the basis weight of the pulp retained on the wire constant.
  • the amount of fiber-based fines in the web affects the moisture content of the web and thus the runnability of the web. It would, therefore, often be desirable also to be able to keep the amount of fiber-based fines constant.
  • the control principle applied depends on how the consistency of the high-consistency pulp fed to the short circulation has been controlled before feeding.
  • the consistency of the high-consistency pulp may, for example, be controlled to be constant on the basis of the fiber fraction, that is, the fiber content, and disregarding the fiber-based fines.
  • the control is carried out using the type of consistency measurement that only takes into account fiber consistency. This type of measurement can be carried out, for example, by means of a blade consistency meter based on shear force.
  • the consistency of high-consistency pulp is controlled to be constant—in this case on the basis of the fiber fraction alone—the amount of fiber-based fines in the high-consistency pulp or diluted pulp can be measured in accordance with the invention and this result can be used for controlling the short circulation.
  • the consistency of high-consistency pulp may also be controlled to be constant on the basis of the total fiber fraction.
  • a consistency meter is used that takes into account the total fiber consistency, that is, the fiber consistency and the consistency of fiber-based fines.
  • the total fiber consistency may be measured, for example, with a consistency meter based on microwaves.
  • the total fiber consistency of the high-consistency pulp can also be obtained by calculation, that is, by adding the measured amount of fiber-based fines to the reading given by the fiber consistency meter, whereby the result obtained can be used for consistency control.
  • the consistency of the high-consistency pulp is controlled to be constant on the basis of the fiber fraction alone, that is, disregarding the fiber-based fines, and the measurement of the fiber-based fines according to the invention shows that the amount of fiber-based fines has increased, depending on the case, either
  • the consistency of the high-consistency pulp is controlled to be constant on the basis of the total fiber fraction, that is, by taking into account the fiber-based fines, and the measurement of the fiber-based fines according to the invention shows that the share of fiber-based fines increases and the share of fibers decreases correspondingly, and if the aim is to keep the total fiber amount retained on the web constant, the feed of retention aid can be increased in the short circulation in such a way that a correspondingly greater amount of the more poorly retained fiber-based fines are retained on the web. No changes will take place in the white water with regard to the amount of fibers.
  • the addition of retention aid and the increase in the amount of fiber-based fines increases the retention of filler, in which case filler feed should be temporarily reduced.
  • the ash contained in the high-consistency pulp can in addition be taken into account in controlling the consistency of high-consistency pulp.
  • the invention also makes possible the control of white water consistency, whereby measurements of the amount of fiber-based fines to be retained, present in the white water, are utilised.
  • the addition of an agent affecting retention and/or a filler or the like can then be controlled on the basis of the need indicated by the measurements.
  • the feed of retention aid can be linked with multivariable control, where the retention aid feed, filler feed, or feed of other similar agent is linked with the same control system.
  • other changes taking place in the process can also be taken into account in the feed of these substances. If necessary, it is then also possible to take into account separately in control the amount of fiber-based fines in both high-consistency pulp and white water.
  • the determination of fiber-based fines in white water may correspondingly be performed on the basis of the difference between the total consistency of the white water and ash consistency, which represents the amount of fiber-based fines in the white water.
  • the content of fiber-based fines can, on the other hand, also be measured by means of a separate meter, which measures fiber length distribution.
  • the different fines shares can then be calculated and weighted in the control by the probability with which they will appear in the wire pit, whereby the particularly poorly retained fiber fraction would be taken into account best in control.
  • An increase in retention aid also increases the retention of filler.
  • the filler feed In order to keep the consistency of the white water constant, in at least some cases, the filler feed must be controlled at the same time in such a way that the filler feed is momentarily reduced to obtain suitable filler consistency in the short water circulation of the wet end.
  • the properties of the diluted pulp can be controlled by regulating the amount of fiber-containing fines in the short circulation, for example, by separately adding fines fibers to the circulation.
  • Fines fibers can be obtained, for example, from fiber recovery, white water purification, such as micro-flotation, etc.
  • control according to the invention it is possible to stabilise the wet end of the paper machine and to give the operator the opportunity to control events at the wet end more efficiently. In this way, the runnability of the paper machine can be improved and breaks can be reduced and the time required for grade changes can be shortened. Furthermore, the uniformity of paper quality, such as basis weight and moisture content, can be improved.
  • FIG. 1 shows diagrammatically a previously known solution for retention aid control at the wet end of a paper machine
  • FIG. 2 shows diagrammatically the solution according to the invention for retention aid control at the wet end of a paper machine
  • FIG. 3 shows, in accordance with FIG. 2 , another solution according to the invention for retention aid control
  • FIG. 4 shows, in accordance with FIG. 2 , a solution according to the invention for simultaneously controlling retention and controlling filler feed;
  • FIG. 5 shows, in accordance with FIG. 2 , a solution according to the invention for controlling retention and filler feed
  • FIG. 6 shows, in accordance with FIG. 2 , measuring devices for fiber-based fines fitted at the wet end of a paper machine.
  • FIG. 1 shows a part known as such of the pulp feed and white water system at the wet end of a paper machine, where the white water 14 removed from the fiber pulp fed onto the wire 12 from the headbox 10 , which white water containing filler, fiber-based fines and retention aid, is conveyed to the wire pit 16 . From the machine chest 18 to the wire pit is conveyed, along line 20 , high-consistency pulp, so-called thick stock containing, among other things, virgin stock and broke pulp, which also contains fiber-based fines.
  • the high-consistency pulp is diluted with white water essentially to the consistency of the pulp fed to the headbox and conveyed as diluted pulp along line 24 to a centrifugal cleaner 26 , from where the purified diluted pulp is conveyed along line 28 to the headbox 10 .
  • the total consistency or ash consistency is measured from the white water by means of a measuring device 30 .
  • Ash consistency refers mainly to filler consistency.
  • the amount of fiber-based fines is not measured separately.
  • the measurement is transmitted to a control unit 32 , which with a valve 34 regulates the feed 36 of retention aid to the diluted pulp line 28 .
  • FIG. 2 shows a part of the pulp feed and white water system at the wet end of a paper machine applying the solution according to the invention. Where applicable, the same reference numerals are used in FIG. 2 as in FIG. 1 .
  • the white water removed from the pulp fed onto the wire 12 from the headbox 10 which white water contains filler and fiber-based fines that have separated from the pulp fed to the headbox and drained through the wire, is conveyed by means 15 to the wire pit 16 , and from there, mixed with fiber pulp, further along diluted pulp line 24 , through the centrifugal cleaners 26 and deaeration devices 22 by means of a pump to the machine screen 29 , from which the finished paper pulp is conveyed along line 28 to the headbox 10 .
  • High-consistency pulp so-called thick stock, which typically contains both virgin stock and broke, is conveyed to the system from a machine chest (not shown) along line 20 , to which is connected a feedforward solids flow measuring and control unit 38 , known as such, which controls the flow of total solids so as to be constant.
  • the purpose of the constant flow is to keep the total consistency constant in the diluted flow following the wire pit 16 in line 24 .
  • a measuring device 40 is connected to the high-consistency pulp line 20 for measuring the amount of fiber-based fines or the amount of total fines, which measuring device is connected according to the invention to a retention control unit 42 controlling the addition of retention aid by means of a flow rate controller 44 at control valve 34 to the diluted pulp to be conveyed to the machine screen 29 or elsewhere in the headbox.
  • the retention aid feed can, in accordance with the invention, be maintained at such level that, of the pulp fed onto the wire, the desired total amount of fiber material, long fibers and fiber-based fines is retained on the wire, even when the ratio of the amounts of long and short fiber fractions to each other changes.
  • the measuring device 40 measuring the amount of fines
  • a device which enables determination of the amount of different fiber fractions, for example, fibers of different lengths, in the pulp.
  • the different fiber fractions can be given different weightings when determining the addition of retention aid.
  • FIG. 3 shows an arrangement according to FIG. 2 , using the same reference numerals where applicable.
  • the consistency meter 48 in the solids flow measurement and control unit, and not the consistency of all solids. This measurement can be carried out by means of a blade consistency meter or other corresponding measuring device known as such, by which consistency is determined by means of the shear force.
  • the measuring device 48 measuring the consistency of the fiber fraction can be connected to a measuring device 40 measuring the amount of fiber-based fines, as shown by the broken line, whereby total fiber flow can be calculated.
  • the retention aid feed is regulated in the manner shown in FIG. 2 , based on measurement of the amount of fiber-based fines.
  • FIG. 4 shows an arrangement according to FIG. 2 , where filler feed control is connected to retention aid feed control 42 , 44 .
  • filler feed control is connected to retention aid feed control 42 , 44 .
  • FIG. 4 the same reference numerals are used as in the previous Figures, where applicable.
  • filler is fed from the filler line 50 to the diluted pulp line 24 immediately after the wire pit 16 .
  • Filler feed is regulated by means of a constant flow valve 52 , a valve 54 , or a pump.
  • both the retention aid feed and the filler feed that is, the ash in the paper
  • both the retention aid feed and the filler feed can be controlled on the basis of the fines measurement 40 .
  • the amount of fiber-based fines in the high-consistency pulp increases, and the amount of long fibers in relation to fiber-based fines decreases, a greater amount of fines can be retained on the web by adding retention aid, and the total fiber flow from the wire section to the press section, that is, the long fibers and fiber-based fines, can be kept constant.
  • retention aid a greater part of the fiber-based fines, of which there is now more and which is retained more poorly than the long fibers, can now be kept in the paper than before.
  • retention aid would, however, at the same time initially bind more filler to the paper than before, and due to the thus reduced amount of filler, less filler would remain in the water circulation of the wet end than before.
  • the amount of filler added to the pulp can be controlled according to the respective situation.
  • filler feed can be increased in order to reach a suitable balance in filler feed.
  • FIG. 4 the amounts of fiber-based fines, filler and retention aid on a time axis are shown by the “Fines share”, “Filler flow” and Ret. Aid Flow” curves.
  • FIG. 5 shows, in accordance with FIG. 4 , another arrangement according to the invention for feeding retention aid and filler to the water circulation at the wet end of a paper machine.
  • the same reference numerals are used as in FIG. 4 , where applicable.
  • the high-consistency pulp fiber fraction is controlled to be constant by means of a control 38 , using a blade consistency meter 48 .
  • the consistency of the diluted pulp is thus controlled to be constant on the basis of the fiber fraction, disregarding the fines.
  • the fines content in the high-consistency pulp is measured by means of the measuring device 40 .
  • retention aid feed can be decreased by means of the control 42 , 44 , whereby the filler feed does not need to be changed.
  • FIG. 6 shows the short circulation of a paper machine according to FIG. 2 , to which are fitted, by way of an example, measuring devices for fiber-based fines at different points.
  • a measuring device 56 In the diluted pulp line 24 , immediately after the wire pit, is fitted a measuring device 56 .
  • a measuring device 58 In front of the machine screen 29 is fitted a measuring device 58 .
  • a measuring device 60 In the bypass manifold 11 of the headbox 10 or its bypass circulation is fitted a measuring device 60 .
  • a measuring device 62 Also in the duct 15 leading from the wire to the wire pit 16 is fitted a measuring device 62 .
  • the measuring devices for measuring the amount of fiber-based fines can be fitted at all such points in the short circulation, from which information is required on the consistency of the fines.
  • the measuring devices are connected in a manner known as such to the desired control units.

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US10/467,637 2001-02-23 2002-02-22 Method and arrangement for controlling short circulation in a paper machine or the like Abandoned US20050224204A1 (en)

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FI20010360 2001-02-23
FI20010360A FI115539B (fi) 2001-02-23 2001-02-23 Menetelmä ja järjestelmä paperikoneen tai vastaavan lyhyen kierron säädössä
PCT/FI2002/000147 WO2002072948A1 (en) 2001-02-23 2002-02-22 Method and arrangement for controlling short circulation in a paper machine or the like

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US11/211,760 Expired - Fee Related US7566382B2 (en) 2001-02-23 2005-08-26 Method and arrangement for controlling short circulation in a paper machine or the like

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CA (1) CA2439232A1 (fi)
DE (1) DE10296378B4 (fi)
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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070095495A1 (en) * 2005-10-28 2007-05-03 Jorg Reuter Method and apparatus for producing a fibrous web
US20110011548A1 (en) * 2008-02-22 2011-01-20 Jouni Matula Method of and an arrangement for proportioning thick stock to a short circulation of fiber web machine
US20130213596A1 (en) * 2010-09-20 2013-08-22 Voith Patent Gmbh Method for regulating the formation of a fibrous web
CN104165270A (zh) * 2014-08-19 2014-11-26 云南大红山管道有限公司 一种管道输送铁精矿浆体稀释控制系统及其控制方法
CN105381872A (zh) * 2015-12-15 2016-03-09 吴振宇 一种扇形布料器
WO2018146379A1 (en) * 2017-02-08 2018-08-16 Valmet Automation Oy Method and apparatus for determining degree of breaking down of fiber particles into fines in pulp
US11352749B2 (en) * 2019-06-28 2022-06-07 Wetend Technology Oy Method of and an arrangement for adding a chemical to an approach flow system of a fiber web machine

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FI113971B (fi) * 2003-02-11 2004-07-15 Metso Paper Inc Laitteisto ja menetelmä paperikoneen tai vastaavan perälaatikolle johdetun massan käsittelyssä
DE102005010404B4 (de) * 2005-03-07 2009-07-09 Siemens Ag Verfahren zur Regelung eines Dosiersystems bei der Papierherstellung und Vorrichtung hierzu
CN201785656U (zh) * 2007-06-01 2011-04-06 沃依特专利有限责任公司 用于制造纤维幅面的设备
DE102010038694A1 (de) * 2010-07-30 2012-02-02 Voith Patent Gmbh Konstantteil
US9309625B2 (en) 2012-10-18 2016-04-12 Honeywell Asca Inc. Concept to separate wet end and dry end paper machine control through estimation of physical properties at the wire
CN103734892A (zh) * 2013-12-13 2014-04-23 云南中烟昆船瑞升科技有限公司 一种造纸法再造烟叶浆料流送系统

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US4514257A (en) * 1981-03-19 1985-04-30 Svenska Traforskningsinstitutet Method of measuring fines in pulp suspensions
US6328851B1 (en) * 1997-11-25 2001-12-11 Metso Paper Automation Oy Method and equipment for controlling properties of paper

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SE503386C2 (sv) * 1994-09-30 1996-06-03 Skogsind Tekn Foskningsinst Förfarande vid bestämning av mängden fyllmedel i papper
DE19736047A1 (de) 1997-08-20 1999-02-25 Voith Sulzer Papiermasch Gmbh Vorrichtung und Verfahren zur Steuerung oder Regelung des Flächengewichts einer Papier- oder Kartonbahn
FI974327A (fi) * 1997-11-25 1999-05-26 Valmet Automation Inc Menetelmä ja laitteisto paperin ominaisuuksien säätämiseksi
FI982625A (fi) * 1998-12-04 2000-06-05 Valmet Automation Inc Menetelmä ja laitteisto paperin ominaisuuksien säätämiseksi
DE19922817A1 (de) 1999-05-19 2000-11-23 Voith Sulzer Papiertech Patent Vorrichtung und Verfahren zur Steuerung oder Regelung des Flächengewichts einer Papier- oder Kartonbahn
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US3711688A (en) * 1968-06-27 1973-01-16 Bunker Ramo Computer control of paper machine in which basis weight is controlled through control of stock flow
US4514257A (en) * 1981-03-19 1985-04-30 Svenska Traforskningsinstitutet Method of measuring fines in pulp suspensions
US6328851B1 (en) * 1997-11-25 2001-12-11 Metso Paper Automation Oy Method and equipment for controlling properties of paper

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070095495A1 (en) * 2005-10-28 2007-05-03 Jorg Reuter Method and apparatus for producing a fibrous web
US7763148B2 (en) * 2005-10-28 2010-07-27 Voith Patent Gmbh Method and apparatus for producing a fibrous web
US20110011548A1 (en) * 2008-02-22 2011-01-20 Jouni Matula Method of and an arrangement for proportioning thick stock to a short circulation of fiber web machine
US8202397B2 (en) * 2008-02-22 2012-06-19 Wetend Technologies Oy Method of and an arrangement for proportioning thick stock to a short circulation of fiber web machine
US20130213596A1 (en) * 2010-09-20 2013-08-22 Voith Patent Gmbh Method for regulating the formation of a fibrous web
US9096973B2 (en) * 2010-09-20 2015-08-04 Voith Patent Gmbh Method for regulating the formation of a fibrous web
CN104165270A (zh) * 2014-08-19 2014-11-26 云南大红山管道有限公司 一种管道输送铁精矿浆体稀释控制系统及其控制方法
CN105381872A (zh) * 2015-12-15 2016-03-09 吴振宇 一种扇形布料器
WO2018146379A1 (en) * 2017-02-08 2018-08-16 Valmet Automation Oy Method and apparatus for determining degree of breaking down of fiber particles into fines in pulp
SE545617C2 (en) * 2017-02-08 2023-11-14 Valmet Automation Oy Method and apparatus for determining degree of breaking down of fiber particles into fines in pulp
US11352749B2 (en) * 2019-06-28 2022-06-07 Wetend Technology Oy Method of and an arrangement for adding a chemical to an approach flow system of a fiber web machine

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FI115539B (fi) 2005-05-31
US7566382B2 (en) 2009-07-28
DE10296378T5 (de) 2004-07-08
FI20010360A (fi) 2002-08-24
CA2439232A1 (en) 2002-09-19
FI20010360A0 (fi) 2001-02-23
DE10296378B4 (de) 2018-06-14
US20050279477A1 (en) 2005-12-22
WO2002072948A1 (en) 2002-09-19

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