EP0733735A2 - Partie humide d'une machine à papier - Google Patents
Partie humide d'une machine à papier Download PDFInfo
- Publication number
- EP0733735A2 EP0733735A2 EP96102508A EP96102508A EP0733735A2 EP 0733735 A2 EP0733735 A2 EP 0733735A2 EP 96102508 A EP96102508 A EP 96102508A EP 96102508 A EP96102508 A EP 96102508A EP 0733735 A2 EP0733735 A2 EP 0733735A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- lines
- white water
- machine
- water
- consistency
- 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
Links
Images
Classifications
-
- 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
-
- 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
Definitions
- the invention relates to a wet end of a paper machine according to the preamble of claim 1.
- the most important quality requirements relate to the fiber orientation in the material jet leaving the outlet nozzle and thus in the paper web after its completion, as well as the basis weight profile, i.e. the distribution of the basis weight transversely to the running direction of the paper web as well as lengthways to it.
- White water is preferably used as the dilution water, ie the water which is separated from the fibrous materials in the sheet formation process. This white water is collected in a collecting trough, the so-called screen ship, from where it reaches a white water chest of relatively large volume.
- the use of white water is cheaper than the use of fresh water for various reasons. This means saving fresh water.
- the valuable fibers and fillers still contained in the white water are reused.
- connecting lines are provided which provide a conductive connection between the Establish the white water chest and the partial flow lines to the flow chamber.
- the invention has for its object to design a wet end according to the preamble of claim 1 such that fluctuations in basis weight are largely suppressed.
- the dilution water line is instead connected directly to the collecting trough, this means that when the retention and thus the consistency of the dilution water obtained change, the dilution water reaches the partial flow lines directly, with the "correct" consistency.
- FIG. 1 A wet section of a paper machine is shown there. The following elements can be seen in FIG. 1:
- a distributor 1 with a vertical longitudinal axis has a connection 1.1 for supplying a main stream of a stock suspension. This main stream comes from a stock preparation system, not shown here.
- the distributor has a circular cross section.
- the distributor 1 also has a multiplicity of connections which are located in one and the same plane. In the present case, only the connections 1.2 and 1.3 can be seen.
- a hose line is led from each connection - see hose lines 1.22, 1.33, 1.44 and 1.55. These hose lines lead to a machine-wide flow chamber 2. This has corresponding connecting pieces 2.2, 2.3, 2.4 and 2.5, and - on the outlet side - an outlet nozzle 2.1. See also Figure 2.
- hose lines 1.22, 1.33, 1.44 and 1.55 are considerably more numerous than shown here, and they expediently all have the same length.
- the inlet ports to the nozzle chamber 2 are in turn in one and the same horizontal plane. They are preferably at the same mutual distance.
- the inside of the nozzle chamber 2 can have dividing walls, which are only shown in broken lines here, and which lie in vertical planes. If they are provided, they either extend over the entire length of the nozzle chamber 2 or only over a part thereof.
- the wire section 3 comprises in a known manner a fourdrinier wire 3.1, a breast roller 3.2, a deflection roller 3.3 and a plurality of guide rollers 3.4.
- the white water is known to be used to dilute the main stream of the stock suspension. In the present case, according to the invention, it is discharged from the collecting trough at a very specific point - see connection point 4.1. The removal takes place by means of a pump 6 to which a pressure line 6.1 is connected.
- the pressure line 6.1 branches into lines 6.2, 6.3, 6.4 and 6.5.
- Line 6.2 opens into hose line 1.22, line 6.3 into hose line 1.33, line 6.4 into hose line 1.44 and line 6.5 into hose line 1.55.
- the branching lines of the white water namely the lines 6.2, 6.3, 6.4 and 6.5, contain valves with which the inflow of the white water serving for dilution to the hose lines 1.22, 1.33, 1.44 and 1.55 can be regulated Way can be set.
- valves can also be provided in the hose lines. The individual partial streams guided in the hose lines thus reach the flow chamber 2, whereby they have exactly the right fiber content.
- connection point 4.2 Due to the location of the connection point 4.2, the white water is led to the consumption points in a very narrow circuit according to the invention.
- the regulation is very quick, i.e. without great time lag, so that one could speak of a dynamic self-regulating effect.
- the dilution water lines and / or the partial flow lines of the main and / or mixture flow have connections for introducing chemicals, such as retention aids, or of additional fiber suspensions or suspensions containing fine particles.
- retention agent is added in accordance with the second main claim, this occurs for the following reasons: the retention agent must preferably be associated with those constituents which have poor retention behavior; In the white water stream, there are particularly high levels of fines and fillers.
- the retention agent is preferably added in the ratio of the fine and fillers in the main stream and in the dilution stream in the main and dilution water stream.
- the invention can be used in wet sections in which two or more distributors are assigned to a single nozzle chamber, in a multi-layer headbox. It is also possible to apply the invention to multi-layer headboxes in which a first layer of fibrous material is first formed, onto which a second layer is placed, produced by a secondary headbox, etc.
Landscapes
- Paper (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19509522A DE19509522C2 (de) | 1995-03-20 | 1995-03-20 | Naßpartie einer Papiermaschine |
DE19509522 | 1995-03-20 |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0733735A2 true EP0733735A2 (fr) | 1996-09-25 |
EP0733735A3 EP0733735A3 (fr) | 1998-01-14 |
EP0733735B1 EP0733735B1 (fr) | 2001-01-24 |
Family
ID=7756830
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP96102508A Expired - Lifetime EP0733735B1 (fr) | 1995-03-20 | 1996-02-20 | Partie humide d'une machine à papier |
Country Status (4)
Country | Link |
---|---|
US (1) | US5958189A (fr) |
EP (1) | EP0733735B1 (fr) |
AT (1) | ATE198917T1 (fr) |
DE (2) | DE19509522C2 (fr) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998024973A1 (fr) * | 1996-12-06 | 1998-06-11 | Eka Chemicals Ab | Procede de fabrication de papier |
WO1998041684A1 (fr) * | 1997-03-18 | 1998-09-24 | Valmet Corporation | Systeme de traitement et de circulation de l'eau de dilution pour la caisse de tete d'une machine a papier |
EP0989230A1 (fr) * | 1998-09-24 | 2000-03-29 | Voith Sulzer Papiertechnik Patent GmbH | Procédé et dispositif pour tenir propre ou pour nettoyer le conduit de la faible consistance d'un système de caisse de tête |
Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19627669C2 (de) * | 1996-07-10 | 2001-03-01 | Stora Enso Publication Paper A | Verfahren zur Verbesserung von Druckpapieren |
FI115646B (fi) * | 1996-11-26 | 2005-06-15 | Metso Paper Inc | Paperikoneen/kartonkikoneen monikerrosperälaatikko |
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 |
FI103822B (fi) * | 1998-06-16 | 1999-09-30 | Valmet Corp | Menetelmä flokkisuuden optimoimiseksi |
DE19859770A1 (de) * | 1998-06-29 | 1999-12-30 | Voith Sulzer Papiertech Patent | Verfahren und Vorrichtung zum Mischen von Sroffsuspension |
ATE262611T1 (de) | 1998-06-29 | 2004-04-15 | Voith Paper Patent Gmbh | Verfahren und vorrichtung zur durchmissung von faserstoffsuspensionen |
DE19830600A1 (de) | 1998-07-09 | 2000-01-13 | Voith Sulzer Papiertech Patent | Misch- und Rezirkulationskreislauf |
FI116078B (fi) | 1998-12-30 | 2005-09-15 | Metso Paper Inc | Menetelmä massan syöttämiseksi perälaatikkoon |
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 |
US6270625B1 (en) * | 1999-06-29 | 2001-08-07 | The Mead Corporation | Method for manufacturing colored stripped paper |
DE29916787U1 (de) * | 1999-09-23 | 1999-12-30 | Voith Sulzer Papiertech Patent | Vorrichtung zum Führen von an einer Papiermaschine anfallendem Siebwasser |
FI109712B (fi) * | 2000-09-14 | 2002-09-30 | Metso Paper Inc | Menetelmä ja laitteisto massan fraktioinnissa paperi- tai kartonkikoneessa |
PL1987329T3 (pl) * | 2006-02-01 | 2011-12-30 | Astenjohnson Inc | Skrzynia przelewowa i system dostarczania surowca w maszynie do produkcji papieru |
US8715466B1 (en) * | 2012-10-19 | 2014-05-06 | Theodore Caouette | Method and system for reducing water loss in a paper mill |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4239647A1 (de) * | 1992-11-26 | 1994-06-01 | Voith Gmbh J M | Verfahren und Vorrichtung zur Vergleichmäßigung des Flächengewichtsquerprofils mittels Siebkreislaufsektionierung |
EP0600251A1 (fr) * | 1992-11-05 | 1994-06-08 | J.M. Voith GmbH | Procédé pour uniformiser la composition d'un bande de papier |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3296066A (en) * | 1963-11-13 | 1967-01-03 | Black Clawson Co | Headbox for papermaking machine and stock distributor thereto |
GB1179847A (en) * | 1966-09-01 | 1970-02-04 | St Annes Board Mill Co Ltd | Flowbox |
US4021295A (en) * | 1975-05-05 | 1977-05-03 | Beloit Corporation | Method and apparatus for supplying white water from a single silo in the formation of a multi-ply web |
DE3028186C2 (de) * | 1980-07-25 | 1982-07-08 | J.M. Voith Gmbh, 7920 Heidenheim | Stoffauflauf für Papiermaschinen |
SE428811B (sv) * | 1981-12-03 | 1983-07-25 | Karlstad Mekaniska Ab | Forfarande och anordning for framstellning av en flerskiktad pappersbana |
DE4211291C3 (de) * | 1992-04-03 | 2001-06-07 | Voith Gmbh J M | Mischeinrichtung und Verfahren zum Mischen von zwei Flüssigkeiten bei konstantem Gemischvolumenstrom zur Versorgung des Stoffauflaufs einer Papiermaschine |
DE4402273C2 (de) * | 1994-01-27 | 1995-11-23 | Voith Gmbh J M | Papiermaschine zur Herstellung mehrlagiger Papierbahnen |
US5505819A (en) * | 1994-03-31 | 1996-04-09 | Macmillan Bloedel Limited | Neutral papermaking |
-
1995
- 1995-03-20 DE DE19509522A patent/DE19509522C2/de not_active Expired - Fee Related
-
1996
- 1996-02-20 AT AT96102508T patent/ATE198917T1/de not_active IP Right Cessation
- 1996-02-20 DE DE59606354T patent/DE59606354D1/de not_active Expired - Fee Related
- 1996-02-20 EP EP96102508A patent/EP0733735B1/fr not_active Expired - Lifetime
- 1996-03-20 US US08/618,748 patent/US5958189A/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0600251A1 (fr) * | 1992-11-05 | 1994-06-08 | J.M. Voith GmbH | Procédé pour uniformiser la composition d'un bande de papier |
DE4239647A1 (de) * | 1992-11-26 | 1994-06-01 | Voith Gmbh J M | Verfahren und Vorrichtung zur Vergleichmäßigung des Flächengewichtsquerprofils mittels Siebkreislaufsektionierung |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998024973A1 (fr) * | 1996-12-06 | 1998-06-11 | Eka Chemicals Ab | Procede de fabrication de papier |
AU723127B2 (en) * | 1996-12-06 | 2000-08-17 | Eka Chemicals Ab | A process for the production of paper |
US6113741A (en) * | 1996-12-06 | 2000-09-05 | Eka Chemicals Ab | Process for the production of paper |
CN1094540C (zh) * | 1996-12-06 | 2002-11-20 | 埃卡化学公司 | 一种造纸方法 |
EP1586705A1 (fr) * | 1996-12-06 | 2005-10-19 | Eka Chemicals AB | Procédé de production de papier |
NO326717B1 (no) * | 1996-12-06 | 2009-02-02 | Eka Chemicals Ab | Fremgangsmåte ved fremstilling av papir |
WO1998041684A1 (fr) * | 1997-03-18 | 1998-09-24 | Valmet Corporation | Systeme de traitement et de circulation de l'eau de dilution pour la caisse de tete d'une machine a papier |
EP0989230A1 (fr) * | 1998-09-24 | 2000-03-29 | Voith Sulzer Papiertechnik Patent GmbH | Procédé et dispositif pour tenir propre ou pour nettoyer le conduit de la faible consistance d'un système de caisse de tête |
US6214170B1 (en) | 1998-09-24 | 2001-04-10 | Voith Sulzer Papiertechnik Patent Gmbh | Process for cleaning or maintaining the cleanliness of the low-consistency branch of a headbox system |
Also Published As
Publication number | Publication date |
---|---|
DE19509522C2 (de) | 1999-03-11 |
ATE198917T1 (de) | 2001-02-15 |
DE59606354D1 (de) | 2001-03-01 |
DE19509522A1 (de) | 1996-09-26 |
EP0733735A3 (fr) | 1998-01-14 |
US5958189A (en) | 1999-09-28 |
EP0733735B1 (fr) | 2001-01-24 |
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