EP0357574B1 - Procédé de fabrication de papier - Google Patents

Procédé de fabrication de papier Download PDF

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Publication number
EP0357574B1
EP0357574B1 EP89850252A EP89850252A EP0357574B1 EP 0357574 B1 EP0357574 B1 EP 0357574B1 EP 89850252 A EP89850252 A EP 89850252A EP 89850252 A EP89850252 A EP 89850252A EP 0357574 B1 EP0357574 B1 EP 0357574B1
Authority
EP
European Patent Office
Prior art keywords
colloid
process according
aluminate
anionic
cationic
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.)
Expired - Lifetime
Application number
EP89850252A
Other languages
German (de)
English (en)
Other versions
EP0357574A2 (fr
EP0357574A3 (fr
Inventor
Hans Erik Johansson
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.)
Nouryon Pulp and Performance Chemicals AB
Original Assignee
Eka Nobel AB
Eka Chemicals AB
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
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Application filed by Eka Nobel AB, Eka Chemicals AB filed Critical Eka Nobel AB
Priority to AT89850252T priority Critical patent/ATE99010T1/de
Publication of EP0357574A2 publication Critical patent/EP0357574A2/fr
Publication of EP0357574A3 publication Critical patent/EP0357574A3/fr
Application granted granted Critical
Publication of EP0357574B1 publication Critical patent/EP0357574B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/33Synthetic macromolecular compounds
    • D21H17/46Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/54Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/33Synthetic macromolecular compounds
    • D21H17/34Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/41Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups
    • D21H17/44Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups cationic
    • D21H17/45Nitrogen-containing groups
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/63Inorganic compounds
    • D21H17/67Water-insoluble compounds, e.g. fillers, pigments
    • D21H17/68Water-insoluble compounds, e.g. fillers, pigments siliceous, e.g. clays

Definitions

  • the amount of anionic colloid which is added to the stock should suitably be within the range of from 0.005 to 2 per cent by weight, preferably from 0.01 to 0.4 per cent by weight, based on dry cellulose fibres and optional fillers.
  • the concentration of the colloid, preferably colloidal silica, in the sol added to the stock is not critical. From a practical point of view it is suitable that the sols at the addition to the stock have a concentration of from 0.05 to 5.0 per cent by weight.
  • the anionic colloid was an alkali stabilized silica sol with a specific surface area of 500 m2/g.
  • the cationic synthetic polymer was a cationic polyacrylamide of medium cationicity sold by Allied Colloids under the name Percol 292.
  • the sodium aluminate was added in the form of a 0.025% aqueous solution and the given amounts of aluminate are expressed as kg Al2O3.
  • the additions of chemicals were made to 1 l diluted stock (about 0.3%) with intervals of 15 seconds under agitation in the order aluminate, cationic polymer, inorganic colloid.
  • the flocked stock was transferred to the freeness apparatus and measurements were made 15 seconds after the last addition.
  • the water which is collected is a measurement of the dewatering effect and is expressed in ml Canadian Standard Freeness (CSF).
  • CSF Canadian Standard Freeness
  • a groundwood stock was used which did not contain any fillers.
  • the cationic polymer was the same polyacrylamide as in Example 1.
  • the anionic colloid was an aluminum modified, 15% alkali stabilized, silica sol where the surface of the colloidal particles had been modified with 9% aluminum atoms and the surface area of the particles was 500 m2/g.
  • the order of addition was sodium aluminate, cationic polymer followed by anionic colloid. Tests were made both with a stock pH of 6 and a stock pH of 7.5 whereby the pH had been adjusted with diluted H2SO4 and diluted NaOH respectively.
  • Example 3 a groundwood stock with addition of 0.5 g/1 of Na2SO4.10H2O was used as in Example 3.
  • the pH of the stock was 6.5 and the added chemicals were sodium aluminate, a cationic polyethylene imine sold by BASF under the name Polymin SK and an anionic colloid which was a bentonite colloid having a specific surface area of from about 400 to 800 m2/g in water.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Paper (AREA)
  • Making Paper Articles (AREA)
  • Diaphragms For Electromechanical Transducers (AREA)
  • Polarising Elements (AREA)
  • Electronic Switches (AREA)

Claims (10)

  1. Procédé pour la production du papier par formation et élimination de l'eau d'une suspension de cellulose contenant des fibres sur une toile, caractérisé en ce que la formation et l'élimination de l'eau sont effectuées en présence d'un colloïde inorganique anionique, sous la condition que le colloïde inorganique anionique ne soit pas un acide silicique polymère ayant une aire de surface spécifique d'au moins 1050 m²/g,avec un aluminate et un polymère synthétique cationique.
  2. Procédé selon la revendication 1, caractérisé en ce que le colloïde anionique est un colloïde à base de silice.
  3. Procédé selon la revendication 1 ou 2, caractérisé en ce que le colloïde est un sol de silice, un sol de silice avec des particules ayant au moins une couche superficielle de silicate d'aluminium ou un sol de silice modifié par de l'aluminium.
  4. Procédé selon la revendication 1, 2 ou 3, caractérisé en ce que les particules du colloïde ont une aire de surface spécifique dans la plage allant de 50 à 1000 m²/g.
  5. Procédé selon la revendication 3, caractérisé en ce que la taille des particules du colloïde est au plus égale à 20 nm.
  6. Procédé selon la revendication 1, caractérisé en ce que le polymère synthétique cationique est un polyacrylamide cationique, une polyéthylèneimine, une polyamine ou une polyamidoamine.
  7. Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce que l'aluminate est ajouté à la suspension fibreuse avant le colloïde inorganique anionique et le polymère synthétique cationique.
  8. Procédé selon l'une quelconque des revendications 1, 2, 3, 4 ou 5, caractérisé en ce que la quantité de colloïde inorganique anionique est comprise dans la plage allant de 0,005 à 2 pour cent en poids, en se fondant sur des fibres sèches ou des charges facultatives.
  9. Procédé selon la revendication 1 ou 6, caractérisé en ce que la quantité de polymère synthétique cationique est comprise dans la plage allant de 0,01 à 3 pour cent en poids, en se fondant sur des fibres sèches ou des charges facultatives.
  10. Procédé selon la revendication 1, caractérisé en ce que le rapport de poids de l'aluminate, exprimé en Al₂O₃, par rapport au colloïde inorganique anionique, est compris dans la plage allant de 0,01:1 à 3:1.
EP89850252A 1988-09-01 1989-08-09 Procédé de fabrication de papier Expired - Lifetime EP0357574B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT89850252T ATE99010T1 (de) 1988-09-01 1989-08-09 Verfahren zur papierherstellung.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE8803065 1988-09-01
SE8803065A SE467627B (sv) 1988-09-01 1988-09-01 Saett vid framstaellning av papper

Publications (3)

Publication Number Publication Date
EP0357574A2 EP0357574A2 (fr) 1990-03-07
EP0357574A3 EP0357574A3 (fr) 1991-10-23
EP0357574B1 true EP0357574B1 (fr) 1993-12-22

Family

ID=20373187

Family Applications (1)

Application Number Title Priority Date Filing Date
EP89850252A Expired - Lifetime EP0357574B1 (fr) 1988-09-01 1989-08-09 Procédé de fabrication de papier

Country Status (13)

Country Link
EP (1) EP0357574B1 (fr)
JP (1) JP2521539B2 (fr)
AT (1) ATE99010T1 (fr)
AU (1) AU605997B2 (fr)
BR (1) BR8904283A (fr)
CA (1) CA1334324C (fr)
DE (1) DE68911626T2 (fr)
ES (1) ES2048323T3 (fr)
FI (1) FI90448C (fr)
NO (1) NO171567C (fr)
NZ (1) NZ230427A (fr)
PT (1) PT91611B (fr)
SE (1) SE467627B (fr)

Families Citing this family (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4795531A (en) * 1987-09-22 1989-01-03 Nalco Chemical Company Method for dewatering paper
US4927498A (en) * 1988-01-13 1990-05-22 E. I. Du Pont De Nemours And Company Retention and drainage aid for papermaking
SE500367C2 (sv) * 1989-11-09 1994-06-13 Eka Nobel Ab Silikasoler och förfarande för framställning av papper
JP2521651B2 (ja) * 1991-07-02 1996-08-07 エカ ノーベル アクチェボラーグ 紙の製造方法
DE4437118A1 (de) * 1994-10-05 1996-04-11 Technocell Dekor Gmbh & Co Kg Basispapier für dekorative Beschichtungssysteme
US5846384A (en) * 1995-06-15 1998-12-08 Eka Chemicals Ab Process for the production of paper
SE9502184D0 (sv) * 1995-06-15 1995-06-15 Eka Nobel Ab A process for the production of paper
US5595630A (en) * 1995-08-31 1997-01-21 E. I. Du Pont De Nemours And Company Process for the manufacture of paper
SE9504081D0 (sv) * 1995-11-15 1995-11-15 Eka Nobel Ab A process for the production of paper
US7169261B2 (en) 1999-05-04 2007-01-30 Akzo Nobel N.V. Silica-based sols
NZ514752A (en) 1999-05-04 2004-01-30 Akzo Nobel Nv Two-step alkalization process for the preparation of silica-based sols
US6379501B1 (en) 1999-12-14 2002-04-30 Hercules Incorporated Cellulose products and processes for preparing the same
EP1500745A1 (fr) 2002-04-03 2005-01-26 Seiko PMC Corporation Procede de production de papier et agent pour ameliorer le rendement d'un tel procede
FI121119B (fi) 2003-04-15 2010-07-15 Kemira Oyj Menetelmä paperin valmistamiseksi
WO2008081682A1 (fr) 2006-12-28 2008-07-10 Tokyo Kinzoku Industry Co., Lid. Dispositif de retenue
CN103556532B (zh) * 2013-10-31 2016-01-20 东莞理文造纸厂有限公司 一种造纸用助留剂及其制备方法

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE8403062L (sv) * 1984-06-07 1985-12-08 Eka Ab Forfarande vid papperstillverkning
SE451739B (sv) * 1985-04-03 1987-10-26 Eka Nobel Ab Papperstillverkningsforfarande och pappersprodukt varvid som avvattnings- och retentionsforbettrande kemikalie anvends katjonisk polyakrylamid och en speciell oorganisk kolloid
SE8701252D0 (sv) * 1987-03-03 1987-03-25 Eka Nobel Ab Sett vid framstellning av papper
US4795531A (en) * 1987-09-22 1989-01-03 Nalco Chemical Company Method for dewatering paper
US4927498A (en) * 1988-01-13 1990-05-22 E. I. Du Pont De Nemours And Company Retention and drainage aid for papermaking
SE461156B (sv) * 1988-05-25 1990-01-15 Eka Nobel Ab Saett foer framstaellning av papper varvid formning och avvattning aeger rum i naervaro av en aluminiumfoerening, ett katjoniskt retentionsmedel och en polymer kiselsyra

Also Published As

Publication number Publication date
NO171567C (no) 1993-03-31
SE8803065D0 (sv) 1988-09-01
NO893500D0 (no) 1989-08-31
FI894075A (fi) 1990-03-02
AU605997B2 (en) 1991-01-24
JP2521539B2 (ja) 1996-08-07
JPH0299692A (ja) 1990-04-11
PT91611A (pt) 1990-03-30
PT91611B (pt) 1995-05-31
NO171567B (no) 1992-12-21
EP0357574A2 (fr) 1990-03-07
ES2048323T3 (es) 1994-03-16
DE68911626T2 (de) 1994-04-07
SE467627B (sv) 1992-08-17
FI90448C (fi) 1994-02-10
NZ230427A (en) 1991-06-25
SE8803065L (sv) 1990-03-02
CA1334324C (fr) 1995-02-14
DE68911626D1 (de) 1994-02-03
ATE99010T1 (de) 1994-01-15
NO893500L (no) 1990-03-02
FI894075A0 (fi) 1989-08-30
BR8904283A (pt) 1990-04-17
AU4084089A (en) 1990-03-29
FI90448B (fi) 1993-10-29
EP0357574A3 (fr) 1991-10-23

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