EP1156155A2 - Section de séchage - Google Patents

Section de séchage Download PDF

Info

Publication number
EP1156155A2
EP1156155A2 EP01105067A EP01105067A EP1156155A2 EP 1156155 A2 EP1156155 A2 EP 1156155A2 EP 01105067 A EP01105067 A EP 01105067A EP 01105067 A EP01105067 A EP 01105067A EP 1156155 A2 EP1156155 A2 EP 1156155A2
Authority
EP
European Patent Office
Prior art keywords
web
dryer
section according
dryer section
guiding device
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
Application number
EP01105067A
Other languages
German (de)
English (en)
Other versions
EP1156155A3 (fr
EP1156155B1 (fr
Inventor
Peter Kahl
Markus Oechsle
Roland Mayer
Eddie Bowden
Robert Procter
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.)
Voith Patent GmbH
Original Assignee
Voith Paper Patent GmbH
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Voith Paper Patent GmbH filed Critical Voith Paper Patent GmbH
Publication of EP1156155A2 publication Critical patent/EP1156155A2/fr
Publication of EP1156155A3 publication Critical patent/EP1156155A3/fr
Application granted granted Critical
Publication of EP1156155B1 publication Critical patent/EP1156155B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F5/00Dryer section of machines for making continuous webs of paper
    • D21F5/18Drying webs by hot air
    • D21F5/185Supporting webs in hot air dryers
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F5/00Dryer section of machines for making continuous webs of paper
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F5/00Dryer section of machines for making continuous webs of paper
    • D21F5/18Drying webs by hot air

Definitions

  • the invention relates to a dryer section of a machine for production a material web, in particular a paper or cardboard web. It affects also a floating dryer for such a dryer section.
  • the aim of the invention is to provide a dryer section of the type mentioned to create with both at high machine speed the best possible drying rate at the beginning of drying as well as secure web guidance is guaranteed.
  • a for such a dryer section suitable float dryer can be created.
  • Drying section is at least one designed as a floating dryer pressurized gas-operated web guiding device is provided. So in particular such a floating dryer directly after the press section and be provided in front of the first drying cylinder. As a result of the combination a float dryer with a dryer can also reduce the web Strength (e.g. at high humidity such as before cylinder drying) be dried.
  • the screen in the respective compressed gas-operated web guiding device usually an at least essentially straight line Course on.
  • the web guiding device comprises for pressurizing the Material web expediently several in a row in the direction of web travel arranged nozzles, preferably on both sides of the material web such nozzles are provided.
  • nozzles preferably on both sides of the material web such nozzles are provided.
  • several nozzle bars each extending in the direction of the web width be provided.
  • the dryer section is at least one pressurized gas-operated web guiding device arranged in front of the first drying cylinder.
  • Air can in particular be provided as the compressed gas.
  • baffle dryer is provided through which Hot air and / or hot steam impingement flow can be applied to the material web is.
  • the material web is preferably at least a larger support roller in particular with an associated impingement dryer guided.
  • Such a baffle dryer is preferably again before arranged first drying cylinder.
  • the web of material Before the web of material has a smooth heated surface for the first time is withdrawn, so it can by at least one float dryer and, if necessary, pre-dried at least one impingement flow dryer.
  • the gas or air drying expediently takes place until a sufficient dryness is reached at which the required web tension is reached can be easily applied.
  • the material web has when draining from the first drying cylinder or when starting for the first time Pulling off a smooth heated surface already a dry matter, which is higher than about 58 to about 65 °.
  • part of the gas or air drying also by an impingement dryer or an impingement hood.
  • the press section is advantageously connected to the last press nip initially at least one pressurized gas-operated web guiding device intended.
  • the material web in the connection to the last press nip of a press section first by at least a pressurized gas powered web guiding device and in the connection attached to it via at least one, in particular larger, support roller assigned impact flow dryer is performed before the first Drying cylinder is fed.
  • the drying speed in the area of each, as a floating dryer executed web guiding device or a respective one Impingement dryer is advantageously over the pressure gas temperature, speed and / or humidity adjustable.
  • Air permeability of a respective compressed gas powered Sieve assigned to the web guiding device is preferably possible chosen high. This is the case in a preferred embodiment Air permeability of the respective sieve is greater than approximately 300 cfm and preferably greater than about 500 cfm.
  • the web of material can pass through the last press nip of the press section guided felt (top or bottom felt) can be removed. It is but also an acceptance directly from one of the last press nips of the press section assigned press roll conceivable.
  • a respective compressed gas-operated web guiding device can be horizontal, be arranged vertically or at an angle. In the latter case, the Material web in the inclined pressure gas operated web guiding device generally obliquely upwards or generally obliquely downwards be led below.
  • pressurized gas-operated web guiding devices are provided, so can at least part of these web guiding devices each have their own sieve.
  • suction rolls To hold the web of material on the screen can before and / or after assigned pressurized gas-operated web guiding device and / or between successive web guiding devices, suction rolls, Transfer foils and / or suction boxes can be provided.
  • the roller following the last levitation dryer can be assigned to the web transfer partially by the levitation dryer Sieve can be wrapped, or the web can be covered by a suction roller can be transferred to a subsequent dryer fabric.
  • the web guiding device is expediently attached to the Sieve pressed and / or sucked. This is possible, for example, that the web to be transferred in a respective pressurized gas Web guiding device only on its side facing away from the wire and in the web running direction with compressed gas and / or from the Vacuum side is applied.
  • the transfer through the gas or air dryer is preferably done through the air dryer.
  • the transfer can also partially or entirely with transfer belt and corresponding transfer zones in suction and blow boxes.
  • transfer belt be sure that the rest of the web is in front of the corresponding gas or felt or sieve air dryer with an additional removal device can be driven into the pulper or cellar.
  • At least one Web guiding device is provided through which the material web with Low temperature compressed gas preferably in the range of about 20 to about 150 ° can be applied. This is particularly the use of a such pressurized gas-operated web guiding device as a pure transfer element possible.
  • the levitation dryer according to the invention is characterized in that it comprises a screen serving to support the web.
  • the invention designed for example as a floating dryer Compressed gas operated levitation system (possibly in connection with at least one impingement flow dryer) can be used especially at the beginning the drying between the press and the first drying cylinder, preferably in Combination with a tandem NipcoFlex press or DuoCentri press with tape around the central roller or other press configurations, at where the web is not pulled off a smooth roller become.
  • Use within the (pre) drying section is also conceivable, shrinking in the cross-machine direction as freely as possible allow and so slight differences in cross shrinkage to reach between edge and middle.
  • the web guiding device even with a low gas or air temperature, for example operate in the range of about 20 to about 150 ° C.
  • the leadership facility can be used as a pure transfer element be used.
  • Figure 1 shows a schematic partial representation of one with compressed gas, here Compressed air, operated web guiding device 10, which in particular as Floating dryer can be executed.
  • the web guide device 10 is used to support the web Assigned screen 12, which together with the material web 14 through the Web guide device 10 is passed.
  • the material web 14 can in particular be a paper or cardboard web.
  • the material web 14 is thus also Compressed air pressures that they alternate in the web running direction L from Sieve 12 is lifted up and abuts against it. Because of the air permeability has the screen 12 within the web guiding device at least essentially a straight line.
  • the Web guiding device 10 For the appropriate loading of the material web 14 includes the Web guiding device 10 several in a row in the web running direction L. arranged nozzles 16. There are 12 on both sides of the sieve and 14 nozzles 16 are provided corresponding to the material web. In the present Case are on both sides, each facing each other the width of the nozzle bar 16 is provided.
  • the air permeability of the screen 12 is advantageously greater than about 300 cfm, and preferably greater than about 500 cfm.
  • the nozzles 16 can be designed and / or controlled so that that for transferring the material web 14, the web 14 in the web guiding device 10 only on their side facing away from the screen 12 and in Compressed gas, here compressed air, is applied to the web running direction L.
  • Compressed gas here compressed air
  • For Transfer of the material web 14 can also be the material web 14 from the sieve side through the sieve 12 through with negative pressure become. You can do this between those provided on the lower side of the sieve Nozzle bar 16 vacuum boxes (not shown) arranged his.
  • the web guiding device 10 Pressurized gas, especially compressed air, low temperature in the range of preferably operate from about 20 to about 150 °.
  • This web guiding device 10 can thus in particular also as a pure transfer element be used.
  • Figures 2 and 3 each show a purely schematic representation Dryer section 18 of a machine for producing a material web, at which can in particular be a paper or cardboard web.
  • impingement flow dryer 28 through which the material web 14 with a hot air and / or hot steam impingement flow is acted upon.
  • the material web 14 is with a special sieve 30 assigned to impingement flow dryer 28 over a larger one with the dryer hood 26 provided support roller 32.
  • the drying speed in the range of a particular, for example web guiding device 10, 10 'or a floating dryer of the impingement flow dryer provided in the embodiment according to FIG. 2 28 is about the compressed air temperature, speed and / or moisture adjustable. It can in the different embodiments drying, for example, take place so that the material web 14 (cf. also FIG. 1) when the first drying cylinder 18 runs off or when pulling off a smooth, heated surface for the first time already has a dry matter content that is preferably higher than about 60 up to about 65%.
  • the two web guiding devices 10, 10 'a common sieve 12 out.
  • the web of material 14 is in the area of a suction roller 36 from through the last Press nip 20 of the press section 22 guided bottom felt 34 removed.
  • the screen 12 is between the two web guiding devices 10, 10 ′ passed over a further suction roller 38.
  • a suction roller 40 is provided, via the the sieve 12 is guided.
  • the material web 14 by the screen 30 assigned to the impingement dryer 28 At the takeover point, for example, a transfer foil 44, a suction box 46 or the like can be provided.
  • a transfer foil 44, a suction box 46 or the like At the takeover point, for example, a transfer foil 44, a suction box 46 or the like can be provided.
  • the material web 14 from the wire 30 to a drying wire 44 passed, through which the web finally the first drying cylinder 18 is supplied.
  • the material web is 14 in the first web guiding device 10 generally obliquely down and in the second web guiding device 10 'in general led diagonally upwards.
  • the transfer of the material web 14 from the screen 12 to the through the second web guiding device 10 'guided sieve 12' takes place in the area of another, the sieve Suction roller 54 assigned to 12 '.
  • the sieve 12' also serves as a drying sieve, through which the material web 14 following the second Web guiding device 10 'via a further suction roller 56 to the first one Drying cylinder 18 is supplied.

Landscapes

  • Paper (AREA)
  • Drying Of Solid Materials (AREA)
EP01105067A 2000-05-17 2001-03-02 Section de séchage d'une machine de fabrication de papier ou carton Expired - Lifetime EP1156155B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10024358 2000-05-17
DE10024358A DE10024358A1 (de) 2000-05-17 2000-05-17 Trockenpartie

Publications (3)

Publication Number Publication Date
EP1156155A2 true EP1156155A2 (fr) 2001-11-21
EP1156155A3 EP1156155A3 (fr) 2003-11-12
EP1156155B1 EP1156155B1 (fr) 2007-02-14

Family

ID=7642516

Family Applications (1)

Application Number Title Priority Date Filing Date
EP01105067A Expired - Lifetime EP1156155B1 (fr) 2000-05-17 2001-03-02 Section de séchage d'une machine de fabrication de papier ou carton

Country Status (4)

Country Link
US (1) US6493962B2 (fr)
EP (1) EP1156155B1 (fr)
CA (1) CA2347611A1 (fr)
DE (2) DE10024358A1 (fr)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1564329A1 (fr) * 2004-02-14 2005-08-17 Voith Paper Patent GmbH Section de post-séchage
EP1895048A1 (fr) * 2006-08-30 2008-03-05 Voith Patent GmbH Installation de séchage
WO2011006176A1 (fr) 2009-07-15 2011-01-20 Andritz Ag Dispositif de production d'une bande de matière fibreuse

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6634120B2 (en) * 2001-03-26 2003-10-21 Voith Paper Patent Gmbh Apparatus for coating moving fiber webs
DE20307055U1 (de) * 2003-05-07 2003-07-17 Schramm, Kurt, 72762 Reutlingen Zellstoffentwässerungsmaschine
WO2007085618A1 (fr) * 2006-01-25 2007-08-02 Nv Bekaert Sa Systeme convectif pour installation de sechage
DE102008041418A1 (de) * 2008-08-21 2010-02-25 Voith Patent Gmbh Vorhang-Auftragsmaschine
CN110552230A (zh) * 2018-06-01 2019-12-10 临泉县高洁卫生用品有限公司 一种卫生纸生产的烘干成型装置
CN112959796A (zh) * 2021-04-09 2021-06-15 广东汕樟轻工股份有限公司 一种全伺服控制高速多功能干式涂布复合机
CN115976871B (zh) * 2023-03-17 2023-05-12 诸城市天工造纸机械有限公司 一种造纸用干燥装置

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2671279A (en) * 1949-11-08 1954-03-09 J O Ross Engineering Corp Drier
GB1323461A (en) * 1970-08-21 1973-07-18 Kobayashi Tadashi Drying apparatus for papermaking
IT1099872B (it) * 1978-10-27 1985-09-28 Sperotto Spa Macchina per l'asciugatura di tessuti,in particolare di tessuti a maglia di tipo jersey
JPH07103517B2 (ja) * 1987-11-26 1995-11-08 バルメット オイ ペーパウェブ等の装置内被覆乾燥の方法および装置
DE3829988A1 (de) * 1988-09-03 1990-03-15 Mtm Obermaier Gmbh & Co Kg Verfahren und vorrichtung zum behandeln von textilen warenbahnen
DE4416585C2 (de) * 1994-05-11 1999-09-02 Voith Gmbh J M Trockenpartie einer Papiermaschine
FI102623B (fi) * 1995-10-04 1999-01-15 Valmet Corp Menetelmä ja laite paperikoneessa
US6004430A (en) * 1995-10-04 1999-12-21 Ilvespaa; Heikki Method and device for enhancing the run of a paper web in a paper machine
DE19544881A1 (de) * 1995-12-01 1997-06-12 Voith Sulzer Papiermasch Gmbh Maschine zur Herstellung einer kontinuierlichen Bahn
DE19605195A1 (de) * 1996-02-13 1997-08-14 Voith Sulzer Papiermasch Gmbh Trockenpartie
US6003245A (en) * 1997-04-22 1999-12-21 Valmet Corporation Method for optimizing of evaporation drying of paper, runnability, and of paper quality as well as dryer section that makes use of the method in a paper machine
DE19723163A1 (de) * 1997-06-03 1998-12-10 Voith Sulzer Papiermasch Gmbh Trockenpartie
DE19935138A1 (de) * 1998-09-11 2000-05-04 Voith Sulzer Papiertech Patent Trockenpartie
DE19841767A1 (de) * 1998-09-11 2000-03-16 Voith Sulzer Papiertech Patent Trockenpartie sowie Konvektionstrockner für eine solche Trockenpartie

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1564329A1 (fr) * 2004-02-14 2005-08-17 Voith Paper Patent GmbH Section de post-séchage
EP1895048A1 (fr) * 2006-08-30 2008-03-05 Voith Patent GmbH Installation de séchage
WO2011006176A1 (fr) 2009-07-15 2011-01-20 Andritz Ag Dispositif de production d'une bande de matière fibreuse

Also Published As

Publication number Publication date
US6493962B2 (en) 2002-12-17
EP1156155A3 (fr) 2003-11-12
EP1156155B1 (fr) 2007-02-14
DE10024358A1 (de) 2001-11-22
CA2347611A1 (fr) 2001-11-17
DE50112021D1 (de) 2007-03-29
US20010042316A1 (en) 2001-11-22

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