WO2009021804A1 - Konstantteil für eine papiermaschine - Google Patents
Konstantteil für eine papiermaschine Download PDFInfo
- Publication number
- WO2009021804A1 WO2009021804A1 PCT/EP2008/059364 EP2008059364W WO2009021804A1 WO 2009021804 A1 WO2009021804 A1 WO 2009021804A1 EP 2008059364 W EP2008059364 W EP 2008059364W WO 2009021804 A1 WO2009021804 A1 WO 2009021804A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- consistency
- consistency stream
- stream
- low
- headbox
- Prior art date
Links
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 method for producing a finished pulp suspension for producing a paper, board, tissue or another fibrous web by mixing at least one, made of recycled fiber and filler high consistency flow with at least one of fresh water, white water o.a. formed low-consistency stream in a machine for producing the fibrous web.
- the invention also relates to an arrangement for producing a finished pulp suspension for producing a paper, board, tissue or another fibrous web from at least one, formed by newly processed fiber and filler high-consistency stream and at least one, preferably fresh water, white water o.a. formed low-consistency stream in the constant part of a machine for producing the fibrous web, wherein at least the high-consistency stream is passed through a cleaning device, in particular for carrying out the method.
- the highly consistent accept is diluted with the white water collected in the paper machine and then fed to the headbox. Before the headbox, however, the pulp suspension must at least be cleaned. This is relatively expensive and requires a lot of space.
- the object of the invention is therefore to reduce the effort and the space required for the constant part.
- the object was achieved with regard to the method in that at least the high-consistency stream is cleaned and at least part of the low-consistency stream is added to it only after the high-consistency stream has been cleaned. Since the dilution of the high-consistency stream takes place only after the cleaning, the cleaning device can be designed for a correspondingly lower throughput. This also applies to any existing, more of the high-consistency stream before dilution passed devices, such as degassing.
- cleaning devices such as cleaners or sorters are often suitable for relatively high consistency streams without taking advantage of this potential.
- the high-consistency stream after the cleaning device is led to a mixing device with at least part of the low-consistency stream.
- the consistency of the high-consistency stream required for the headbox should already be achieved. This allows the high consistency stream to be fed directly to a head box of the machine after admixing in the mixing device.
- the high-consistency stream is passed through a degassing device before admixing and the content of free air is reduced to less than 1, in particular less than 0.6,% by volume in the head box.
- the admixed low-consistency stream is cleaned before admixing by a cleaning device and / or degassed via a degassing device.
- the respective cleaning device of the streams should comprise at least at least one sorter and / or cleaner.
- the admixing takes place via an injection of the low consistency stream, wherein the inlet velocity of the low consistency stream should preferably be 3 to 15 times the flow velocity of the high consistency stream.
- the maximum consistency depends on the freeness and / or the filler content of the high consistency stream. A lower degree of grinding and / or a low filler content are associated with a lower maximum consistency. - A -
- the consistency of the high consistency flow should prior to the admixture at a freeness of the pulp suspension below 50 0 SR, preferably less than 35 ° SR at least 0.6%, in particular at least 1, be 2%.
- the advantages of a high consistency are particularly clear when the consistency of the high consistency stream prior to blending is at least 1.2%, preferably at least 1.6% and especially at least 2.1% and at most 4%, preferably at most 3.5%.
- the stock consistency of the high consistency stream in% before admixture should be greater than 0.025 times the freeness measured in 0 SR minus 0.2 and less than 0.04 times the freeness measured in 0 SR plus 0 Be 8.
- the high-consistency stream is not diluted further after the admixture or else a further part of the low-consistency stream is fed into a headbox of the machine and mixed with the high-consistency stream.
- Figure 1 a schematic representation of the constant part of a paper machine and Figure 2: another constant part.
- the high-consistency stream 1 is prepared in a manner known per se from fibrous materials and fillers in accordance with the specifications of the papermaker, i. in predetermined mixing ratios in a mixing chest 5 merged and mixed.
- the paper machine begins with the headbox 3 and the adjoining former 11 to form the fibrous web 9.
- the finished pulp suspension is applied via one or more nozzles of the headbox 3 on the Formersieb 10.
- the white water is collected and returned to the constant part.
- the use of white water to form the low-consistency stream 2 is not only associated with savings compared to the use of fresh water, but it can also be reused in the white water contained fiber and fillers.
- the high-consistency stream 1 coming from the mixing chest 5 is diluted, as shown in FIG. 1, in a mixing device 8 with a part of the low-consistency stream.
- the consistency of the high consistency stream 1 is after this dilution between 1, 6 and 4%, preferably between 2.1 and 3.5%.
- the relatively high consistency significantly reduces the expense of cleaning and degassing due to the lower throughput.
- the high-consistency stream 1 is passed through a first cleaning device 4 in the form of a cleaner, a degassing device 6 and a cleaning device 4 in the form of a sorter.
- a first cleaning device 4 in the form of a cleaner
- a degassing device 6 and a cleaning device 4 in the form of a sorter.
- the cleaner and the degassing device 6 can also be dispensed with.
- headboxes are particularly suitable in which streams of different consistency are mixed to regulate the basis weight transverse profile, as described, for example, in EP 1 645 684.
- the supply of at least one stream 1, 2 should be regulated for Basisthesquerprofiltechnik the fibrous web 9.
- the part of the low-consistency part 2 supplied to the mixing device 7 and the headbox 3 is guided by a degassing device 6 and a cleaning device 4 in the form of a sorter.
- the white water is brought to boiling under reduced pressure. In this case, even slight impurities can be eliminated.
Landscapes
- Paper (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN200880103200A CN101784724A (zh) | 2007-08-11 | 2008-07-17 | 造纸机的上浆系统 |
EP08786203A EP2179086A1 (de) | 2007-08-11 | 2008-07-17 | Konstantteil für eine papiermaschine |
BRPI0813620-3A BRPI0813620B1 (pt) | 2007-08-11 | 2008-07-17 | Método para produção de suspensão de polpa acabada e instalação para produção de rede de material fibroso para produção de papel, papelão e tecido |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE200710038090 DE102007038090A1 (de) | 2007-08-11 | 2007-08-11 | Konstantteil IV |
DE102007038090.0 | 2007-08-11 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2009021804A1 true WO2009021804A1 (de) | 2009-02-19 |
Family
ID=39767095
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2008/059364 WO2009021804A1 (de) | 2007-08-11 | 2008-07-17 | Konstantteil für eine papiermaschine |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP2179086A1 (de) |
CN (1) | CN101784724A (de) |
BR (1) | BRPI0813620B1 (de) |
DE (1) | DE102007038090A1 (de) |
WO (1) | WO2009021804A1 (de) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103154362A (zh) * | 2010-07-30 | 2013-06-12 | 沃依特专利有限责任公司 | 用于制备纤维幅的机器的进入系统 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE29909960U1 (de) * | 1998-06-10 | 1999-09-09 | Valmet Corp | Prozeßanordnung des primären Kreislaufs einer Papier- oder Kartonmaschine |
DE10050109A1 (de) * | 2000-10-09 | 2002-04-11 | Voith Paper Patent Gmbh | Verfahren und Mischvorrichtung zur Erzeugung einer fertigen Faserstoffsuspension |
WO2002097191A1 (en) * | 2001-05-29 | 2002-12-05 | Metso Paper, Inc. | Stock feed arrangement in a paper or board machine |
WO2003093574A1 (en) * | 2002-05-02 | 2003-11-13 | Metso Paper, Inc. | Process arrangement in the short circulation of a paper machine |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10017037A1 (de) | 2000-04-05 | 2001-10-11 | Voith Paper Patent Gmbh | Vorrichtung zum Entgasen von Faserstoffsuspension |
DE102004049261A1 (de) | 2004-10-09 | 2006-04-13 | Voith Paper Patent Gmbh | Verfahren und Vorrichtung zur Regelung des Flächengewichtsquerprofils einer Faserstoffbahn |
-
2007
- 2007-08-11 DE DE200710038090 patent/DE102007038090A1/de not_active Withdrawn
-
2008
- 2008-07-17 EP EP08786203A patent/EP2179086A1/de not_active Withdrawn
- 2008-07-17 CN CN200880103200A patent/CN101784724A/zh active Pending
- 2008-07-17 WO PCT/EP2008/059364 patent/WO2009021804A1/de active Application Filing
- 2008-07-17 BR BRPI0813620-3A patent/BRPI0813620B1/pt not_active IP Right Cessation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE29909960U1 (de) * | 1998-06-10 | 1999-09-09 | Valmet Corp | Prozeßanordnung des primären Kreislaufs einer Papier- oder Kartonmaschine |
DE10050109A1 (de) * | 2000-10-09 | 2002-04-11 | Voith Paper Patent Gmbh | Verfahren und Mischvorrichtung zur Erzeugung einer fertigen Faserstoffsuspension |
WO2002097191A1 (en) * | 2001-05-29 | 2002-12-05 | Metso Paper, Inc. | Stock feed arrangement in a paper or board machine |
WO2003093574A1 (en) * | 2002-05-02 | 2003-11-13 | Metso Paper, Inc. | Process arrangement in the short circulation of a paper machine |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103154362A (zh) * | 2010-07-30 | 2013-06-12 | 沃依特专利有限责任公司 | 用于制备纤维幅的机器的进入系统 |
Also Published As
Publication number | Publication date |
---|---|
BRPI0813620A2 (pt) | 2015-12-15 |
DE102007038090A1 (de) | 2009-02-12 |
CN101784724A (zh) | 2010-07-21 |
BRPI0813620B1 (pt) | 2018-07-10 |
EP2179086A1 (de) | 2010-04-28 |
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