EP1702109A2 - Chemische verbesserung bei der papierherstellung - Google Patents

Chemische verbesserung bei der papierherstellung

Info

Publication number
EP1702109A2
EP1702109A2 EP04805226A EP04805226A EP1702109A2 EP 1702109 A2 EP1702109 A2 EP 1702109A2 EP 04805226 A EP04805226 A EP 04805226A EP 04805226 A EP04805226 A EP 04805226A EP 1702109 A2 EP1702109 A2 EP 1702109A2
Authority
EP
European Patent Office
Prior art keywords
paper
alkyl ketene
acid anhydride
maleic acid
styrene maleic
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.)
Withdrawn
Application number
EP04805226A
Other languages
English (en)
French (fr)
Inventor
Anna-Liisa Tammi
Mika Laitila
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.)
BASF Schweiz AG
UPM Kymmene Oy
Original Assignee
Ciba Spezialitaetenchemie Holding AG
Ciba SC Holding AG
UPM Kymmene Oy
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 Ciba Spezialitaetenchemie Holding AG, Ciba SC Holding AG, UPM Kymmene Oy filed Critical Ciba Spezialitaetenchemie Holding AG
Publication of EP1702109A2 publication Critical patent/EP1702109A2/de
Withdrawn legal-status Critical Current

Links

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
    • D21H17/71Mixtures of material ; Pulp or paper comprising several different materials not incorporated by special processes
    • D21H17/72Mixtures of material ; Pulp or paper comprising several different materials not incorporated by special processes of organic material
    • 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
    • D21H21/00Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/14Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
    • D21H21/16Sizing or water-repelling agents
    • 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
    • D21H11/00Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
    • D21H11/08Mechanical or thermomechanical pulp
    • 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
    • D21H17/03Non-macromolecular organic compounds
    • D21H17/05Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
    • D21H17/17Ketenes, e.g. ketene dimers
    • 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
    • D21H17/37Polymers of unsaturated acids or derivatives thereof, e.g. polyacrylates

Definitions

  • the invention relates to an improvement in the printability of uncoated mechanical pulp paper grades, especially to an improvement in the printability of supercalen- dered (SC) papers, particularly in rotogravure printing.
  • Objects of the invention are a method for improving the printability of uncoated mechanical pulp paper grades, the use of a combination of alkyl ketene dimer and styrene maleic acid anhydride copolymer in said method, and paper prepared by said method.
  • SC paper grades comprise various newsprint grades, SC paper grades, and coated mechanical paper grades.
  • Supercal- endered (SC) papers contain 70-90% mechanical and/or recycled pulp and 10-30% chemical pulp and do not have any surface coating. Instead, they can contain up to 35% minerals as fillers, relative to the amount of fibrous raw materials which is marked as 100. Paper quality of SC papers is largely based on the quality of fibrous raw materials and fillers and their treatment and processing.
  • SC paper printability properties have been affected by including in the pulp such chemicals which provide the paper with strength (such as starch) and hydrophobicity (such as alkyl ketene dimer (AKD), alkenyl succinic anhydride (ASA), styrene maleic anhydride (SMA)).
  • the filler can be pretreated, for example to have a hy- drophobic character.
  • the web is passed through one or several nips for achieving the desired quality properties, especially as regards final thickness, gloss and smoothness.
  • Supercalenders have a plurality of rolls arranged one above the other and nips provided between the rolls through which the paper web travels.
  • a super- calender is usually arranged separately from the paper machine. It is also possible to calender the web 'on-line', which means that the calender is connected to the paper machine.
  • the web Before (super)calendering the web is usually wetted to a suitable calendering moisture by means of water and/or steam.
  • an arrangement for calendering a board web wherein a liquid containing a protein or a chemical that has properties similar to protein can be transferred on the board web via a moistening means before calendering.
  • the moistening means are arranged so that the board web can be surface-sized and moistened simultaneously, or a coating containing a pigment can be transferred on the board web.
  • US 6494988 discloses a process for improving the surface of offset paper wherein a binding agent is applied across a moving paper web in a drying section or in a calender.
  • a process for on-line manufacture of SC-A paper (a subgrade within SC papers) is disclosed wherein tensides are added to the moistening water in order to produce a spray mist water having a reduced surface tension.
  • US 6013359 discloses different polyacrylamides as surface treatment agents for improving surface strength and releasing property of printing papers.
  • Too strong and effective calendering can cause "blackening" (reduced brightness) of the paper which should be avoided.
  • Supercalendering under high pressure and temperature also takes off bulkiness of paper which is not a desirable effect.
  • the porosity of SC papers should preferably be decreased, thus making the paper surface more dense, in order to improve the paper quality for printing purposes.
  • the rotogravure printing process is generally most suited to those applications in which a very large number of copies is required to be printed, because the process by which the surface of a rotogravure printing cylinder is prepared is expensive relative to the cost of preparing surfaces of printing cylinders for use in other methods of printing.
  • a rotogravure printing cylinder has on its surface a matrix of cells or depressions which vary in depth according to the quantity of ink which is required to be transferred to the paper from each individual cell. Because of the large number of copies to be printed, it is generally advantageous to run the printing process at high speed.
  • Alkyl ketene dimer (AKD) and alkenyl succinic acid anhydride (ASA) are hydro- phobing sizing agents used in internal and surface sizing of paper and paperboard under neutral or alkaline conditions.
  • AKD is used as a minor component together with starch (for example below 5%, often 1-3% by weight of starch), polyvinyl alcohol (PNA), carboxy methyl cellulose (CMC) or other polymer in liquid form.
  • Structurally alkyl ketene dimers are unsaturated lactones.
  • Technical grade saturated fatty acids usually stearic acid, are used in the synthesis of AKD waxes.
  • the waxes Prior to use, the waxes need to be converted into tiny particles dispersed in water by melting and emulsifying the wax. AKD sizes are usually provided in the form of anionic or cationic starch-stabilized dispersions.
  • Styrene maleic acid anhydride (SMA) is a copolymer of styrene and maleic acid anhydride. SMA-based hydrophobic surface sizing agents are used as additives in surface sizes to improve the hydrophobic properties of fine papers (woodfree papers), which contain no or very little mechanical pulp.
  • the present invention is based on the finding that the printability of uncoated mechanical pulp paper is improved by applying a combination of alkyl ketene dimer dispersion and styrene maleic acid anhydride copolymer solution onto the paper web, particularly before supercalendering.
  • it is an object of the invention to provide a method for improving printability of uncoated mechanical pulp paper which method comprises applying a combination of alkyl ketene dimer and styrene maleic acid anhydride copolymer onto at least one side of the paper web, preferably before supercalendering, and calendering the paper web.
  • a further object of the invention is the use of a combination of alkyl ketene dimer and styrene maleic acid anhydride copolymer on paper surface for improving the printability of uncoated mechanical pulp paper grades.
  • Still another object of the invention is paper, preferably supercalendered paper or newsprint paper, prepared by a method wherein a combination of alkyl ketene dimer and styrene maleic acid anhydride copolymer is applied onto the paper web in connection with, preferably before, calendering or supercalendering, and its use in a rotogravure printing process.
  • the above defined method is carried out by using any suitable application method, e.g. film transfer, blade, spray, moisturizing, or curtain application method.
  • a “paper” is meant paper or paperboard or any material, preferably cellulosic material, which is suitable for printing. All weight ratios are calculated as dry weight and all percentages are percentages by weight.
  • the weight ratio of alkyl ketene dimer to styrene maleic acid anhydride copolymer in the combination to be applied onto the paper web as a mixture or separately is pref- erably about 1:1, but it may vary within the range 1:5 - 2:1.
  • the ratio of alkyl ketene dimer to styrene maleic acid anhydride copolymer is within the range of 1:1...2.
  • the styrene maleic acid anhydride copolymer is preferably provided as the ammo- niutn salt form of SMA, for example as 10% aqueous solution. Also other salt forms of SMA, such as sodium, potassium, etc. are possible.
  • the share of styrene in the styrene maleic acid anhydride copolymer is over 50%.
  • the ratio of maleic acid anhydride units to styrene units is generally in the range of from 10:90 to 45:55, preferably 20:80 - 40:60.
  • styrene maleic acid anhydride copoly- mers having a molecular weight from 5000 to 500000.
  • the styrene maleic acid anhydride copolymer is prepared in a known manner, for example by polymerizing the monomers in organic solution.
  • the alkyl ketene dimer can be supplied as an aqueous dispersion which usually con- tains starch or another polymer in liquid form as stabiliser.
  • the AKD content of said dispersion may be for example from 60 to 95%.
  • Alkyl ketene dimers with a melting point within the range of 15-70°C are suitable.
  • a mixture of low melting ( ⁇ 30°C) and high melting (>50°C) alkyl ketene dimers wherein for example ⁇ 30% of alkyl ketene dimers are low melting and >70% high melting alkyl ketene dimers.
  • Starch or other polymer in liquid form may be used as a protective colloid to stabilize the dispersion in an amount of 5-40% of the total dispersion, especially in an amount of 10-20%.
  • the combination of alkyl ketene dimer and styrene maleic acid anhydride can be applied onto the paper web as a mixture or as two separate dispersions.
  • the mixture of alkyl ketene dimer and styrene maleic acid anhydride copolymer is a dispersion with a dry matter content of 5-15%. If the two chemicals are applied separately, AKD may be applied as an AKD dispersion (for example as 18% dispersion) and SMA as a SMA solution (for example as 10% solution), one after the other.
  • the combination of alkyl ketene dimer and styrene maleic acid anhydride copolymer is applied onto the paper web before calendering.
  • Calendering may take place either "on-line" at the paper machine or at a separate calendering unit.
  • the combination of AKD and SMA can be applied onto the web at a separate (su- per)calender before or during calendering, or at the paper machine before or during on-line (super)calendering.
  • Another alternative is to apply the combination of AKD and SMA at the (dry end of) paper machine and then pass the web to a separate (su- ⁇ per)calender.
  • the web Before applying the combination of AKD and SMA, the web can be dried to a suitable moisture content, which is preferably ⁇ 20%, more preferably ⁇ 15%.
  • a further embodiment of the invention is to apply a mixture of alkyl ketene dimer and styrene maleic acid anhydride copolymer onto the paper web together with moistening water before or during calendering.
  • the mixture is applied onto the wet or dry web, the web is possibly dried to desired moisture, and then the web is passed to a calender, preferably to a supercalender. It is also possible to apply the mixture onto paper which has already been calendered, before an additional (super)calendering. In the recently developed new calendering units it may also be possible to apply the mixture in between two stacks of calender rolls.
  • AKD is preferably applied first, as SMA is a better film forming agent than AKD.
  • AKD and SMA improves the printability of uncoated mechanical pulp paper even if the paper web is not (superjcalendered after applying the combination of AKD and SMA to the web.
  • the paper web may, if desired, be calendered before the combination of AKD and SMA is applied on the web.
  • paper quality improving agents such as optical bright- eners, pH regulators, lubricating agents, etc. may be added together or separately with the combination of alkyl ketene dimer and styrene maleic acid anhydride.
  • alkyl ketene dimer and styrene maleic acid anhydride.
  • alkyl ketene dimer and styrene maleic acid anhydride copolymer is applied onto the paper web in an amount which is less than or about 1 gm 2 , preferably about 0.5 g/m 2 , or from 0.05 to 0.8 g/m 2 .
  • a further advantage of the use of a combination of alkyl ketene dimer and styrene maleic anhydride is that there is no need for "over-effective" calendering, which means that no blackening effect appears and the bulkiness of paper is not decreased.
  • Uncalendered mechanical base paper was processed with different chemicals so that applied weight was about 0.5 g/m 2 .
  • the paper was calendered in a laboratory calender in paper moisture of 9.5% under pressure of 50 bar and at a temperature of 90°C.
  • the calendered paper was tested for printability in rotogravure printing.
  • the chemicals used were water, alkyl ketene dimer (AKD) dispersion, styrene maleic anhydride copolymer (SMA) solution, polyethylene glycol (PEG) and a mixture of AKD and SMA.
  • the SMA copolymer contained 28% maleic acid anhydride and 72% styrene.
  • the AKD dispersion was a mixture of low melting (20%) and high melting (80%) alkyl ketene dimers.
  • Commercial SC paper was used as a reference. Styrene acrylate latex was also tested but it stuck tightly on the calender roll and could not be analysed.
  • the number of missing dots is a traditional measure of rotogravure printability of paper.
  • the so-called Heliotest indicates the number of missing dots.
  • the Heliotest fitting developed by Centre Technique dumaschine is used here with an IGT AC2 laboratory printer.
  • the test figure is 110 mm long with an 8 mm wide raster where the tone changes from dark to light.
  • the size of the dots is constant over the entire printing area.
  • the num- ber of missing dots is defined as a distance from the dark end of the printed image within which 20 missing dots can be detected. The longer the distance the better the rotogravure printability of the paper.
  • a dot where more than half of the dot area is missing is considered as a missing dot.
  • SC paper The surface of usual SC paper was processed with different chemicals to about 0.5 g/m 2 .
  • the paper was calendered in a moisture of -5.5%.
  • the temperature was 90°C and a pressure of 40 bar was used.
  • the calendered paper was tested for printability in rotogravure printing. Reference was usual SC paper.
  • the mixture of AKD and SMA provides better print density and printed gloss than the reference or water processed SC paper. Heliotest is clearly better in missing dots appearance. Especially the printed gloss achieved by using a mixture of alkyl ketene dimer and styrene maleic acid anhydride as described in this invention is better than that achieved by any of its components alone. Polyethylene glycol (PEG) was not used because it adhered to calender roll.

Landscapes

  • Paper (AREA)
EP04805226A 2003-12-23 2004-12-22 Chemische verbesserung bei der papierherstellung Withdrawn EP1702109A2 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI20031896A FI20031896A0 (fi) 2003-12-23 2003-12-23 Kemiallinen parannus paperinvalmistuksessa
PCT/FI2004/050195 WO2005061796A2 (en) 2003-12-23 2004-12-22 Chemical improvement in paper making

Publications (1)

Publication Number Publication Date
EP1702109A2 true EP1702109A2 (de) 2006-09-20

Family

ID=29763585

Family Applications (1)

Application Number Title Priority Date Filing Date
EP04805226A Withdrawn EP1702109A2 (de) 2003-12-23 2004-12-22 Chemische verbesserung bei der papierherstellung

Country Status (5)

Country Link
US (1) US20070107865A1 (de)
EP (1) EP1702109A2 (de)
CA (1) CA2549247A1 (de)
FI (1) FI20031896A0 (de)
WO (1) WO2005061796A2 (de)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FI123421B (fi) 2008-05-09 2013-04-30 Upm Kymmene Corp Painettavaksi soveltuva tuote ja menetelmä painettavaksi soveltuvan tuotteen valmistamiseksi
US20120107511A1 (en) 2010-11-01 2012-05-03 Georgia-Pacific Consumer Products Lp Method Of Applying Fugitive Hydrophobic Treatment To Tissue Product
US20120138249A1 (en) * 2010-12-02 2012-06-07 Patrick Sundholm Method for improving paper and board's resistance to the penetration of liquids

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FI64202C (fi) * 1981-10-27 1983-10-10 Valmet Oy Limpress
US5223473A (en) * 1990-11-21 1993-06-29 Xerox Corporation Self-cleaning carbonless paper
US6315824B1 (en) * 1996-02-02 2001-11-13 Rodrigue V. Lauzon Coacervate stabilizer system
SE508593C2 (sv) * 1996-03-29 1998-10-19 Stora Kopparbergs Bergslags Ab Limningskomposition samt förfarande för användning därav vid framställning av papper
FR2749328B1 (fr) * 1996-05-31 1998-07-17 Atochem Elf Sa Collage du papier au moyen de dispersions-latex de copolymeres monomeres hydrophobes/polymeres de type styrene- anhydride maleique a faible masse moleculaire
US6140406A (en) * 1996-06-28 2000-10-31 Consolidated Papers, Inc. High solids interactive coating composition, ink jet recording medium, and method
US6162328A (en) * 1997-09-30 2000-12-19 Hercules Incorporated Method for surface sizing paper with cellulose reactive and cellulose non-reactive sizes, and paper prepared thereby
CA2328872A1 (en) * 1998-04-22 1999-10-28 Hercules Incorporated Paper size dispersions
SE513602C2 (sv) * 1999-02-17 2000-10-09 Stora Kopparbergs Bergslags Ab Limningskomposition, metod för framställning av limmat papper eller limmad kartong, samt limmat papper eller limmad kartong
JP2000247018A (ja) * 1999-03-02 2000-09-12 Oji Paper Co Ltd インクジェット記録媒体
US7279071B2 (en) * 2001-04-11 2007-10-09 International Paper Company Paper articles exhibiting water resistance and method for making same
TW200504265A (en) * 2002-12-17 2005-02-01 Bayer Chemicals Corp Alkenylsuccinic anhydride surface-applied system and uses thereof
US7943789B2 (en) * 2002-12-17 2011-05-17 Kemira Oyj Alkenylsuccinic anhydride composition and method of using the same

Non-Patent Citations (1)

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Title
See references of WO2005061796A3 *

Also Published As

Publication number Publication date
WO2005061796A3 (en) 2005-09-09
FI20031896A0 (fi) 2003-12-23
US20070107865A1 (en) 2007-05-17
CA2549247A1 (en) 2005-07-07
WO2005061796A2 (en) 2005-07-07

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