EP1052327A1 - Siebwasserkreislauf und Verfahren zur Wasserzirkulation einer Papiermaschine - Google Patents
Siebwasserkreislauf und Verfahren zur Wasserzirkulation einer Papiermaschine Download PDFInfo
- Publication number
- EP1052327A1 EP1052327A1 EP00108222A EP00108222A EP1052327A1 EP 1052327 A1 EP1052327 A1 EP 1052327A1 EP 00108222 A EP00108222 A EP 00108222A EP 00108222 A EP00108222 A EP 00108222A EP 1052327 A1 EP1052327 A1 EP 1052327A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- white water
- filler
- pigment
- water
- application
- Prior art date
- 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.)
- Granted
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Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
- D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
- D21H23/22—Addition to the formed paper
- D21H23/24—Addition to the formed paper during paper manufacture
- D21H23/26—Addition to the formed paper during paper manufacture by selecting point of addition or moisture content of the paper
- D21H23/28—Addition before the dryer section, e.g. at the wet end or press 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
- D21F1/66—Pulp catching, de-watering, or recovering; Re-use of pulp-water
Definitions
- the invention relates to a white water circuit of a paper machine, which at least one application device for applying a pigment and / or filler Mass on a not yet completely drained fiber web in the wet area has, which further with a first white water cycle, the one Headbox supplied with white water, and a second white water circuit, the forms the rest of the white water cycle. Furthermore, the Invention a method for water circulation of a paper machine with a Wet part, in which an emerging fiber web on at least one surface a pigment and / or filler-containing mass is applied and the forming fibrous web white water is withdrawn.
- the white water I is part of the White water, which on modern paper machines on a forming roller, a Top suction box, a forming shoe or other suction elements, taking no account of any existing, upstream application is taken from filler or pigment.
- This white water I is without treatment performed in a short cycle and for the dilution of the thick matter Machine chest used right before the headbox.
- the amount of water on the wet vacuum cleaners, flat vacuum cleaners and suction screen rollers are typically recorded as white water II.
- the clear water will then used for spray pipes and the like.
- the inventors have thus recognized that it is to solve the above Problem is the white water cycle of a paper machine and that Process for water circulation of the paper machine so that the Water cycle, which includes the headbox of the paper machine, is fed exclusively from dewatering units, which the fiber web dewater at a stage where pigment and / or filler-containing mass on the fiber web in the process of formation has been applied.
- Each drainage element which in the Following the application of the filler or pigments of the web moisture withdrawn, is consequently enriched with high pigment or filler proportions, so that this water leads to a steady increase in the filler content would lead the headbox formed layer.
- the collection devices of cleaning liquid also count the sieves that come in with the pigment and / or filler application Have come into contact because they also have an increased filler or Pigment content are contaminated.
- the inventors therefore propose a white water cycle a paper machine which has at least one application device for application a mass containing pigment and / or filler on a not yet completely dewatered Has fiber web in the wet area, which continues with a first White water cycle, which supplies a headbox with white water, and continues with a second white water circuit, which absorbs the rest of the white water, is equipped to further develop such that the first white water cycle is fed exclusively by drainage elements, which in the Manufacturing process before the application of the pigment and / or filler Mass are arranged.
- An advantageous embodiment of this white water cycle can be that part of the white water of the second white water circuit for feeding the application of the pigment and / or filler-containing mass is used. Since the invention second white water cycle at least mainly of aggregates is fed that emit water with a high pigment and / or filler content, this cycle is particularly well suited to the water cycle for the applicator or applicators of the pigment- or filler-containing mass serve.
- the rest not to feed the application the white water of the second serving the pigment- and / or filler-containing mass White water cycle with a Entstoffungsvorraum, preferably one Microflotation device that is processed to clear filtrate.
- This so created Clear filtrate from the second white water cycle can be used later in the manufacturing process the paper web can be used anywhere.
- the presence of a de-emptying device, preferably a microflotation device is particularly advantageous if the white water of the second white water circuit is provided with binder, in particular starch, since this binder is then removed from the white water by the de-emptying device discharged and thus an accumulation of binder in the middle Fiber layer of the finished paper can be avoided.
- a microflotation device is present and possibly a disk thickener
- the part of the white water, which the application of the pigment and / or filler-containing mass supplied is, from the flotate of the microflotation device and / or from the overflow of the disk thickener is removed. This ensures that each the proportion of white water containing pigment and / or filler for application is supplied, which is provided with a higher pigment and / or filler content is and thus to a maximum possible return to pigment or Filler leads.
- the inventors propose a method for water circulation Paper machine with a wet part, in which an emerging fiber web at least one surface applied a pigment and / or filler-containing mass and white water is removed from the fibrous web that forms further develop that only the white water, which is not with pigments and / or fillers from the pigment and / or filler application is fed to the headbox.
- An advantageous embodiment of the method provides that only white water, which with pigments and / or fillers from the pigment and / or Filler application is loaded, the application of the pigment and / or filler Mass is supplied.
- a degassing device preferably a microflotation device
- clear filtrate can be returned at any point on the paper machine. If binders are present in the white water of the second white water circuit, the above statements apply.
- Another advantageous embodiment of the method provides that the white water, which the application of the pigment and / or filler-containing mass is supplied, from the overflow of the microflotation device and / or if necessary existing disk thickener is removed.
- This configuration of the procedure has the effect that only the substantial part of the White water is fed into the return line to the application, and thus the amount of the necessary new pigment and / or filler can be reduced.
- FIG. 1 shows a white water circuit according to the invention of a paper machine in a schematic representation. From the paper machine is essentially the sheet formation section 2 with the upstream headbox 1 and the press section 3 indicated below. The white water rivers are drawn as arrows.
- the illustration shows a hybrid former, with a headbox 1, its Stock suspension coming from stock preparation 14 onto first screen 10.1 gives up.
- a first dewatering unit 2.1 is provided, which introduces the collected white water into a white water tank 4.
- a second sieve 10.2 which from above onto the suspension layer is launched.
- another drainage element 2.2 the top of the screen, whose removed white water is also in the white water tank 4 is supplied.
- a further suction roller 12 is attached again causes dewatering of the fiber web and the removed, with White water loaded with pigment and filler.
- white water II which consists of the drainage units 2.3, 2.4, 2.5 and 12 is taken, collected and together to a disc thickener 6 passed and thus kept away from the screen circuit of the headbox 1.
- the cleaning water which is in a drip pan 2.6 is collected, fed to the white water I and the disc thickener because there is a high proportion of pigments and fillers in this cleaning water is included.
- the disc thickener 6 gives its thin material via line 16 to one Microflotation device 7 and its thick matter via line 15 to one White water tank 5, which also contains the flotate from the microflotation device 7 is conducted via line 17.
- the Pigment and filler preparation 8 with a high pigment and filler content Water fed, in which also the necessary amount of fresh pigment and Filling material is fed via the feed 8.1.
- the pigment and filler preparation 8 then gives the finished pigment and Filler slurry on to applicators 11.1 and 11.2, where they focus on the resulting Fiber web is applied.
- the clear filtrate which is obtained from microflotation 7, is discharged via line 18 in a clear filtrate container 9 is stored and faces the papermaking process again as clear water to be used at any point.
- the white water cycle of a paper machine shown above and the method of water circulation in a paper machine achieved that enrichment even when the paper machine is in operation for a long time the inner layer of the paper produced with filler and / or pigment is avoided.
Landscapes
- Paper (AREA)
Abstract
Description
Bei Vorhandensein von Bindemittel im Siebwasser des zweiten Siebwasserkreislaufes gelten die obigen Ausführungen.
- 1
- Stoffauflauf
- 2
- Blattbildungssektion
- 2.1 - 2.5
- Entwässerungselemente
- 2.6
- Auffangvorrichtung für Reinigungswasser
- 3
- Pressensektion
- 4
- Siebwasserbehälter
- 5
- Siebwasserbehälter
- 6
- Scheibeneindicker
- 7
- Mikroflotationsvorrichtung
- 8
- Pigment- und Füllstoffaufbereitung
- 8.1
- Zuführung
- 9
- Klarfiltratbehälter
- 10.1
- Erstes Sieb
- 10.2
- Zweites Sieb
- 11.1
- Erster Applikator
- 11.2
- Zweiter Applikator
- 12
- Saugwalze
- 13
- Siebreinigungsvorrichtung
- 14
- Leitung für Stoffaufbereitung
- 15
- Leitung für Dickstoff des Scheibeneindickers
- 16
- Leitung für Dünnstoff des Scheibeneindickers
- 17
- Leitung für Flotat
- 18
- Leitung für Klarfiltrat
Claims (10)
- Siebwasserkreislauf einer Papiermaschine, welche mindestens eine Auftragsvorrichtung zur Applikation einer pigment- und/oder füllstoffhaltigen Masse auf eine noch nicht fertig entwässerte Faserbahn im Naßbereich aufweist, welche weiterhin mit einem ersten Siebwasserkreislauf, der einen Stoffauflauf mit Siebwasser versorgt, und weiterhin einem zweiten Siebwasserkreislauf, der den Rest des Siebwassers aufnimmt, ausgestattet ist,
dadurch gekennzeichnet, daß
der erste Siebwasserkreislauf ausschließlich durch Entwässerungselemente (2.1, 2.2) gespeist wird, die im Herstellungsprozeß vor der Applikation der pigment- und/oder füllstoffhaltigen Masse angeordnet sind. - Siebwasserkreislauf gemäß dem voranstehenden Anspruch 1,
dadurch gekennzeichnet, daß
ein Teil des Siebwassers des zweiten Siebwasserkreislaufes zur Speisung der Applikation der pigment- und/oder füllstoffhaltigen Masse dient. - Siebwasserkreislauf gemäß dem voranstehenden Anspruch 2,
dadurch gekennzeichnet, daß
das restliche, nicht zur Speisung der Applikation der pigment- und/oder füllstoffhaltigen Masse dienende, Siebwasser des zweiten Siebwasserkreislaufes mit einer Entstoffungsvorrichtung, vorzugsweise einer Mikroflotationsvorrichtung (7), zu Klarfiltrat verarbeitet wird. - Siebwasserkreislauf gemäß einem der voranstehenden Ansprüche 2 bis 3,
dadurch gekennzeichnet, daß
vor der Entstoffungsvorrichtung ein Scheibeneindicker (6) vorgeschaltet ist. - Siebwasserkreislauf gemäß einem der voranstehenden Ansprüche 3 bis 4,
dadurch gekennzeichnet, daß
der Teil des Siebwassers des zweiten Siebwasserkreislaufes, welcher der Applikation der pigment- und/oder füllstoffhaltigen Masse zugeführt wird, aus dem Überlauf des Scheibeneindickers (6) und/oder dem Flotat der Mikroflotationsvorrichtung (7) entnommen wird. - Verfahren zur Wasserzirkulation einer Papiermaschine mit einem Naßteil, in welchem einer entstehenden Faserbahn auf mindestens eine Oberfläche eine pigment- und/oder füllstoffhaltige Masse appliziert und der sich bildenden Faserbahn Siebwasser entzogen wird,
dadurch gekennzeichnet, daß
ausschließlich das Siebwasser, welches nicht mit Pigmenten und/oder Füllstoffen aus der Pigment- und/oder Füllstoffapplikation belastet ist, dem Stoffauflauf (1) zugeführt wird. - Verfahren gemäß dem voranstehenden Anspruch 6,
dadurch gekennzeichnet, daß
ausschließlich Siebwasser, welches mit Pigmenten und/oder Füllstoffen aus der Pigment- und/oder Füllstoffapplikation belastet ist, der Applikation der pigment- und/oder füllstoffhaltigen Masse zugeführt wird. - Verfahren gemäß dem voranstehenden Anspruch 7,
dadurch gekennzeichnet, daß
das restliche nicht zur Speisung der Applikation der pigment- und/oder füllstoffhaltigen Masse dienende Siebwasser und das nicht dem Stoffauflauf zugeführte Siebwasser mit einer Entstoffungsvorrichtung, vorzugsweise einer Mikroflotationsvorrichtung (7), zu Klarfiltrat verarbeitet wird. - Verfahren gemäß dem voranstehenden Anspruch 8,
dadurch gekennzeichnet, daß
vor einer Mikroflotationsvorrichtung (7) eine Vorreinigung durch einen Scheibeneindicker (6) stattfindet. - Verfahren gemäß einem der voranstehenden Ansprüche 8 bis 9,
dadurch gekennzeichnet, daß
das Siebwasser, welches der Applikation der pigment- und/oder füllstoffhaltigen Masse zugeführt wird, aus dem Überlauf des Scheibeneindickers (6) und/oder dem Flotat der Mikroflotationsvorrichtung (7) entnommen wird.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19922391 | 1999-05-14 | ||
DE19922391A DE19922391A1 (de) | 1999-05-14 | 1999-05-14 | Siebwasserkreislauf und Verfahren zur Wasserzirkulation einer Papiermaschine |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1052327A1 true EP1052327A1 (de) | 2000-11-15 |
EP1052327B1 EP1052327B1 (de) | 2004-07-21 |
Family
ID=7908161
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP00108222A Expired - Lifetime EP1052327B1 (de) | 1999-05-14 | 2000-04-14 | Siebwasserkreislauf und Verfahren zur Wasserzirkulation einer Papiermaschine |
Country Status (4)
Country | Link |
---|---|
US (1) | US6497788B1 (de) |
EP (1) | EP1052327B1 (de) |
AT (1) | ATE271627T1 (de) |
DE (2) | DE19922391A1 (de) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8715466B1 (en) | 2012-10-19 | 2014-05-06 | Theodore Caouette | Method and system for reducing water loss in a paper mill |
CN106758476B (zh) * | 2017-03-21 | 2018-03-09 | 李飞 | 一种制浆造纸白水的封闭循环系统及处理方法 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1341327A (fr) * | 1962-12-18 | 1963-10-25 | Borax Cons Ltd | Perfectionnements apportés aux propriétés d'incombustibilité du carton isolant par introduction d'une solution d'un composé ignifuge dans le carton pendant qu'il est à l'état humide |
DE3406808A1 (de) * | 1984-02-24 | 1985-09-12 | Steinbeis Papier GmbH, 7121 Gemmrigheim | Verfahren zur applikation von hilfs- oder veredelungsmitteln sowie farbstoffen auf der papiermaschine, vorrichtung zur durchfuehrung desselben sowie anwendungsverfahren |
WO1991010500A1 (en) * | 1990-01-19 | 1991-07-25 | Yit-Yhtymä Oy | Method for recovering coating slip waste |
WO1993023612A1 (en) * | 1992-05-19 | 1993-11-25 | Pom Technology Oy Ab | Process and apparatus for circulating backwater in a papermaking machine |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1950351A (en) * | 1931-08-07 | 1934-03-06 | Mead Corp | Paper manufacture |
US5152872A (en) * | 1990-10-15 | 1992-10-06 | Stone-Consolidated Inc. | Apparatus for the wet end coating of paper |
DE4401761C2 (de) * | 1994-01-22 | 1997-04-24 | Voith Gmbh J M | Verfahren und Vorrichtung zur Verbesserung der Papierqualität von Mehrschicht- und Mehrlagenpapieren |
-
1999
- 1999-05-14 DE DE19922391A patent/DE19922391A1/de not_active Withdrawn
-
2000
- 2000-04-14 EP EP00108222A patent/EP1052327B1/de not_active Expired - Lifetime
- 2000-04-14 DE DE50007102T patent/DE50007102D1/de not_active Expired - Lifetime
- 2000-04-14 AT AT00108222T patent/ATE271627T1/de active
- 2000-05-12 US US09/570,376 patent/US6497788B1/en not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1341327A (fr) * | 1962-12-18 | 1963-10-25 | Borax Cons Ltd | Perfectionnements apportés aux propriétés d'incombustibilité du carton isolant par introduction d'une solution d'un composé ignifuge dans le carton pendant qu'il est à l'état humide |
DE3406808A1 (de) * | 1984-02-24 | 1985-09-12 | Steinbeis Papier GmbH, 7121 Gemmrigheim | Verfahren zur applikation von hilfs- oder veredelungsmitteln sowie farbstoffen auf der papiermaschine, vorrichtung zur durchfuehrung desselben sowie anwendungsverfahren |
WO1991010500A1 (en) * | 1990-01-19 | 1991-07-25 | Yit-Yhtymä Oy | Method for recovering coating slip waste |
WO1993023612A1 (en) * | 1992-05-19 | 1993-11-25 | Pom Technology Oy Ab | Process and apparatus for circulating backwater in a papermaking machine |
Also Published As
Publication number | Publication date |
---|---|
EP1052327B1 (de) | 2004-07-21 |
ATE271627T1 (de) | 2004-08-15 |
US6497788B1 (en) | 2002-12-24 |
DE50007102D1 (de) | 2004-08-26 |
DE19922391A1 (de) | 2000-11-16 |
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