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EP0418015A1 - Active sizing compositions - Google Patents

Active sizing compositions Download PDF

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Publication number
EP0418015A1
EP0418015A1 EP90309876A EP90309876A EP0418015A1 EP 0418015 A1 EP0418015 A1 EP 0418015A1 EP 90309876 A EP90309876 A EP 90309876A EP 90309876 A EP90309876 A EP 90309876A EP 0418015 A1 EP0418015 A1 EP 0418015A1
Authority
EP
European Patent Office
Prior art keywords
sizing
anionic
composition according
composition
dispersant
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Withdrawn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
EP90309876A
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German (de)
French (fr)
Inventor
Lawrence Forrester Watson
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.)
Eka Nobel Landskrona AB
Original Assignee
Albright and Wilson Ltd
Eka Nobel Landskrona AB
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Publication of EP0418015A1 publication Critical patent/EP0418015A1/en
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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
    • D21H17/03Non-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
    • D21H17/21Macromolecular organic compounds of natural origin; Derivatives thereof
    • D21H17/23Lignins

Definitions

  • This invention relates to active sizes containing a reactive sizing agent and a dispersant.
  • paper is used in this specification to mean any form of paper, paperboard and related products, the manufacture of which involves the action of a sizing agent upon cellulosic or other fibres.
  • Previous ketene dimer sizes have contained, as dispersant, cationic components such as starches, polyamines, polyamides and polyacrylamides. These emulsifiers and dispersants are homogenised in situ with the ketene dimer to form cationically stabilised emulsions.
  • the present invention provides an active sizing composition which comprises an aqueous emulsion of a reactive sizing agent and an anionic dispersant and/or emulsifier serving to stabilise the emulsion, the reactive sizing agent comprising at least one compound according to the formula wherein R1 and R2 are, independently of each other, hydrocarbon radicals having at least six carbon atoms, more preferably alkyl, alkenyl, cycloalkyl, aryl, aralkyl or alkaryl radicals.
  • Sizing agents of the invention can offer advantages especially in systems where cationic charged fillers e.g., precipitated calcium carbonates are present or in systems using cationic components e.g., retention aids of polyacrylamide, polyamine, PEI, etc. in furnishes consisting of groundwood, thermomechanical pulps or chemical thermomechanical pulps where limited hydroxyl (OH ⁇ ) sites are available for AKD attachment and reactivity.
  • cationic charged fillers e.g., precipitated calcium carbonates are present
  • cationic components e.g., retention aids of polyacrylamide, polyamine, PEI, etc. in furnishes consisting of groundwood, thermomechanical pulps or chemical thermomechanical pulps where limited hydroxyl (OH ⁇ ) sites are available for AKD attachment and reactivity.
  • compositions of the invention are particularly suitable for use as an internal size in sizing operations carried out at the wet end of a paper-making process.
  • R1 and R2 are, independently of each other, C12 to C22 alkyl groups, C14 to C19 alkyl groups being especially preferred.
  • the compounds in which R1 and R2 are each C14H29 or C16H33 are most highly preferred and are referred to hereinafter as "palmitic-stearic dimer".
  • active sizing compositions according to the invention can be effective in their sizing properties, particularly when used in highly-cationic environments, such as those encountered in wet-end sizing in the manufacture of liquid packaging papers and photographic papers as mentioned above, and those, also mentioned above, when the active size is used in connection with fluorescent whitening agents.
  • papers using cationic fillers such as precipitated calcium carbonate can be sized efficiently using an anionically charged alkyl ketene dimer size of the present invention.
  • compositions of the invention can be effective sizing agents is the more surprising because it has previously been supposed in the art that an anionically stabilised sizing agent would lack the necessary affinity with the hydroxyl groups of the cellulose and that a cationically stabilised emulsion was necessary to provide the necessary retention of the sizing agent by reaction with the hydroxyl groups.
  • the dispersant and/or emulsifier stabilising the emulsion can be any suitable anionic dispersant or emulsifier.
  • Sodium lignosulphonate, calcium lignosulphonate and the sodium salt of naphthalene sulphonic acid, and mixtures thereof, are examples of suitable dispersants.
  • the dispersant and/or emulsifier is preferably used in a total amount of 0.5% to 10% based on the weight of the reactive sizing agent, the actual amount used in any particular composition being that which imparts a desired anionic charge to the dispersed sizing agent.
  • the anionic charge density in the sizing compositions of the invention can be extended or modified using components such as anionic polyacrylamides, anionic starch or colloidal silica as emulsifiers.
  • the sizing agent is preferably present in the sizing composition in an amount of 5% to 20% by weight, more preferably 10% to 15% by weight, of the sizing composition.
  • the sizing compositions may be used in conjunction with effective quantities of material such as retention aids, dry strength agents and drainage aids, for example alum which acts both as a drainage aid and as a scavenger for anionic colloidal debris.
  • material such as retention aids, dry strength agents and drainage aids, for example alum which acts both as a drainage aid and as a scavenger for anionic colloidal debris.
  • the sizing compositions of the invention can be made by any convenient process, but preferably are made by homogenising the reactive sizing agent in liquid form (if necessary after heating to melt the material) with the dispersant and/or emulsifier and the appropriate amount of water to form an aqueous emulsion.
  • the dispersant and/or emulsifier is dissolved in water at 65 to 80°C to which is added molten ketene dimer premelted at 65 to 80°C.
  • the resultant mix is homogenised at 2500 to 3500 psi to form a stable emulsion.
  • the sheets were then dried by passing them four times around a photographic drum dyer operated at 105°C, giving a residence time of 3.3 minutes, followed by 5.0 minutes in a forced-draught oven at 105°C. After cooling for at least 10 minutes, the sheets were roughly cut, laminated and finely cut to a final size of 5.0 cm x 12.5 cm.
  • Examples 5 to 10 are comparison examples employing cationically-stabilised AKD sizing agents.
  • Keydime SP1 is a dispersant containing sodium lignosulphonate and the sodium salt of naphthalene sulphonic acid. It is available from Albright & Wilson Limited. Keydime D10 and Keydime D125 are cationically stabilised AKD sizing agents containing, on a dry weight basis, 10% AKD (the palmitic-stearic compound mentioned above) and, respectively, 2.5% and 1.25% cationic polymer. Keydime D10 and Keydime D125 are also available from Albright & Wilson Limited.
  • the AKD was added together with the Keydime SP1 (in examples 1 to 4) and as a component of the Keydime D10 or D125 (in examples 5 to 10), an AKD-Keydime SP1 emulsion having been formed by melting the AKD at 65 to 80°C, dissolving the molten AKD in water at 65 to 80°C and homogenising the mixture with Keydime SP1 at 2500 to 3000 psi.
  • Examples 1 to 4 when compared with Examples 5 to 10, show fluid pick-ups (edgewick) with anionic agents comparable to or better than those of cationic agents. Examples 4 and 8 show that better results can be attained with recirculation which most realistically simulates the papermaking process.
  • the sheets were dried at 105°C for 8 minutes then oven cured for 5 minutes.
  • Lactic acid immersion tests were carried out on the sheets.
  • the sheets were coated with tape and cut to 12.5cm x 5cm strips. These strips were weighed before immersion in 2.5cm of 1% lactic acid for 16 hours. The strips were then reweighed and the pickup calculated in grams. The average of 3 results was taken for each sizing composition.
  • Example 16 is a comparison example using Keydime D10.
  • composition 1 2 3
  • Additive/Dispersant Naphthalene Sulphonic Acid 1.25 1.25 1.25 Na Lignosulphonate 4.5 4.5
  • the process water was acidified prior to the addition of dispersants.
  • the mixture was heated to 70°C before addition to a laboratory homogenizer which was preheated to the same temperature. Homogenization pressure was adjusted to 3500 psig (24 M Pa) (ideally 2500 to 5000 psig (17 to 34 M Pa)). Molten alkyl ketene dimer wax was added at 70°C and allowed three theoretical passes plus one to discharge. Upon discharge, the product was passed through a 200 mesh filter and the temperature rapidly reduced to below 20°C.
  • the precipitated calcium carbonate used for this work was a commercially available grade Albacar HO made at 20% solids with no dispersant added. Particle size averaged 2.7 microns with a Zeta potential of +5 mV.
  • the size test employed in this work was a 2-minutes Cobb test under standard conditions.
  • Anionic size composition (1) of Example 11 was tested against a competitive, cationically stabilized size, Aquapal C348 supplied commercially by Hercules Powder Co. Sizing was measured to a standard 1-min. Cobb test. Machine Furnish on 60g/m2 Wove grade Fibrous - Chemithermal mechanical pulp 50% White Offcuts 17% White Letter Waste 17% White Waste Rejects 8% Own Broke 8%
  • Retention Aid - Cationic Polyacrylamide Nalfloc 4662 commercially available from Nalco Ltd. Fillers - Calcium carbonate addition to a specified sheet ash of 23% w.o.f. Size Type Size Addition % as Received Retention Acid Addition g/tonne % Sheet Ash Sizing/mm Cobb Oven Cured 3 min at 105°C Aquapel C348 3.7 257 23.4 17.7 Composition(1) 1.6 257 22.9 16.9

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  • Detergent Compositions (AREA)

Abstract

The compositions comprise an aqueous emulsion containing a ketene dimer reactive sizing agent and an anionic dispersant or emulsifier such as sodium lignosulphonate, calcium lignosulphonate or the sodium salt of naphthalene sulphonic acid. In addition an extender or modifier such as an anionic polyacrylamide, an anionic starch or colloid silica can be present to extend or modify the anionic charge density of the composition. The compositions are particularly effective in sizing systems containing cationically charged fillers, or cationic additives such as certain retention aids and fluorescent whitening agents.

Description

  • This invention relates to active sizes containing a reactive sizing agent and a dispersant.
  • For convenience, the term "paper" is used in this specification to mean any form of paper, paperboard and related products, the manufacture of which involves the action of a sizing agent upon cellulosic or other fibres.
  • Traditionally, paper has been sized with rosin in conjunction with alum, which acts as a precipitant. More recently, reactive sizes have been introduced, in which a sizing agent reacts directly with the cellulose of the paper. One class of reactive sizes in common use is the ketene dimer sizes. These are typically used as emulsions in water in conjunction with dispersants and emulsifiers, which serve to stabilise the emulsion.
  • Previous ketene dimer sizes have contained, as dispersant, cationic components such as starches, polyamines, polyamides and polyacrylamides. These emulsifiers and dispersants are homogenised in situ with the ketene dimer to form cationically stabilised emulsions.
  • Whilst satisfactory in many applications, the known cationically stabilised ketene dimer sizes give rise to problems in certain applications. In particular, certain grades of paper for liquid packaging and the manufacture of photographic papers involve, in their manufacture, the use of large quantities of cationic polyamide amine epichlorohydrin resin, in order to produce favourable wet-strength properties in the finished paper. In a wet-end process, the resin is normally added to the thickstock. The resin has a high substantivity to cellulose, in order to produce sufficient coverage of the fibre. The introduction of further cationic components, such as starch, dry-­strength resin and cationically stabilised ketene dimer size can lead to poor retention of the components by the cellulose and result in slow drainage, poor strength properties and low sizing efficiency.
  • Problems can also arise in surface sizing processes, particularly because the trend in the manufacture of fine speciality papers is to apply the cationic starch-stabilised ketene dimer size to the surface of the paper sheet in conjunction with a fluorescent whitening agent (FWA). Such agents are usually anionic in nature and their use in conjunction with cationic-stabilised sizes can lead to a reduction in the effectiveness of the FWA and cause a quenching effect which gives rise to a yellower paper.
  • The present invention provides an active sizing composition which comprises an aqueous emulsion of a reactive sizing agent and an anionic dispersant and/or emulsifier serving to stabilise the emulsion, the reactive sizing agent comprising at least one compound according to the formula
    Figure imgb0001
    wherein R₁ and R₂ are, independently of each other, hydrocarbon radicals having at least six carbon atoms, more preferably alkyl, alkenyl, cycloalkyl, aryl, aralkyl or alkaryl radicals.
  • Sizing agents of the invention can offer advantages especially in systems where cationic charged fillers e.g., precipitated calcium carbonates are present or in systems using cationic components e.g., retention aids of polyacrylamide, polyamine, PEI, etc. in furnishes consisting of groundwood, thermomechanical pulps or chemical thermomechanical pulps where limited hydroxyl (OH⁻) sites are available for AKD attachment and reactivity.
  • The compositions of the invention are particularly suitable for use as an internal size in sizing operations carried out at the wet end of a paper-making process.
  • In particularly preferred sizing agents, R₁ and R₂ are, independently of each other, C₁₂ to C₂₂ alkyl groups, C₁₄ to C₁₉ alkyl groups being especially preferred. The compounds in which R₁ and R₂ are each C₁₄H₂₉ or C₁₆H₃₃ are most highly preferred and are referred to hereinafter as "palmitic-stearic dimer". The latter compounds can be regarded as the cycloaddition products of one ketene molecule of the formula R₁-CH=C=0 and one ketene molecule of the formula R₂-CH=C=0, wherein R₁ and R₂ are each C₁₄H₂₉ or C₁₆H₃₅.
  • It has surprisingly been found that, contrary to expectations, active sizing compositions according to the invention can be effective in their sizing properties, particularly when used in highly-cationic environments, such as those encountered in wet-end sizing in the manufacture of liquid packaging papers and photographic papers as mentioned above, and those, also mentioned above, when the active size is used in connection with fluorescent whitening agents. In addition, papers using cationic fillers such as precipitated calcium carbonate can be sized efficiently using an anionically charged alkyl ketene dimer size of the present invention. That the compositions of the invention can be effective sizing agents is the more surprising because it has previously been supposed in the art that an anionically stabilised sizing agent would lack the necessary affinity with the hydroxyl groups of the cellulose and that a cationically stabilised emulsion was necessary to provide the necessary retention of the sizing agent by reaction with the hydroxyl groups.
  • The dispersant and/or emulsifier stabilising the emulsion can be any suitable anionic dispersant or emulsifier. Sodium lignosulphonate, calcium lignosulphonate and the sodium salt of naphthalene sulphonic acid, and mixtures thereof, are examples of suitable dispersants. The dispersant and/or emulsifier is preferably used in a total amount of 0.5% to 10% based on the weight of the reactive sizing agent, the actual amount used in any particular composition being that which imparts a desired anionic charge to the dispersed sizing agent.
  • If desired, the anionic charge density in the sizing compositions of the invention can be extended or modified using components such as anionic polyacrylamides, anionic starch or colloidal silica as emulsifiers. The sizing agent is preferably present in the sizing composition in an amount of 5% to 20% by weight, more preferably 10% to 15% by weight, of the sizing composition.
  • The sizing compositions, if desired, may be used in conjunction with effective quantities of material such as retention aids, dry strength agents and drainage aids, for example alum which acts both as a drainage aid and as a scavenger for anionic colloidal debris.
  • The sizing compositions of the invention can be made by any convenient process, but preferably are made by homogenising the reactive sizing agent in liquid form (if necessary after heating to melt the material) with the dispersant and/or emulsifier and the appropriate amount of water to form an aqueous emulsion. For example, the dispersant and/or emulsifier is dissolved in water at 65 to 80°C to which is added molten ketene dimer premelted at 65 to 80°C. The resultant mix is homogenised at 2500 to 3500 psi to form a stable emulsion.
  • The invention will now be described further by way of examples.
  • EXAMPLES 1 to 4 and COMPARISON EXAMPLES 5 to 10
  • In the experimental work which is described hereafter, all sizing tests were carried out on a 50:50 dry weight mixture of bleached HW and SW kraft pulp which had been simultaneously beaten to a 40°SP endpoint in an experimental-scale valley beater. The sizing test employed was a 16 hour, 1.0% w/v lactic acid edgewick test.
  • Sample preparation without recirculation.
  • 1000cm³ of 1.0% consistency stock was placed in a 1500cm³ beaker, to which the necessary amounts of chemicals (see Table 2) were added sequentially at 30-second intervals using plastics syringes with an accuracy of ±0.1cm³. The 30-­second interval was extended to 60 seconds after addition of the Kymene 557. The pH of the mixture was adjusted to 7.5 by addition of sodium bicarbonate immediately after addition of the Kymene 557. Mixing of the components was accomplished with a mechanical stirrer operated at 100 rpm. Sheets were produced from the final mixture in a British Standard handsheet mould and pressed in a pneumatically operated Voith handsheet press for 5 minutes at a pressure of 50 psig (345 k Pa). The sheets were then dried by passing them four times around a photographic drum dyer operated at 105°C, giving a residence time of 3.3 minutes, followed by 5.0 minutes in a forced-draught oven at 105°C. After cooling for at least 10 minutes, the sheets were roughly cut, laminated and finely cut to a final size of 5.0 cm x 12.5 cm.
  • Sample preparation with recirculation.
  • 3500cm³ of 2.79% consistency stock was placed in a ten-litre pail. Both Kymene 557 and AKD size were then added to this suspension. The pH was adjusted to 7.5 by addition of sodium bicarbonate. Next, sufficient of this "thickstock" to contain 10g of dry fibre was diluted to a total volume of 1000cm³. This resulted in a "thinstock" having a consistency of 1.03%. Next, alum, Accostrength 85 and Staklok 400 were added to the thinstock. This thinned suspension was drained through a Messmer consistency apparatus. The retained solid was discarded and the filtrate was then used to dilute more of the thickstock, so that further additions of alum, Accostrength 85 and Staklok 400 could be made. This cycle of dilution, drainage and addition of alum, Accostrength 85 and Staklok 400 was repeated until it had been carried out nine times before handsheet manufacture. Just prior to sheet formation, the pH was again adjusted to 7.5 by addition of further sodium bicarbonate. Thorough mixing of the components was accomplished manually. Sheets were produced as described above.
  • Sample Testing:
  • All samples were weighed and then placed 2.5cm below the surface of a 1.0% w/v lactic acid solution. After 16 hours, the samples were removed, dried and reweighed. The results are shown in Table 1. TABLE 1
    Example Dispersant Sample Preparation Fluid Pick-up (g)
    1 Keydime SP1 S1 0.3860
    2 Keydime SP1 S2 0.4013
    3 Keydime SP1 S3 0.4299
    4 Keydime SP1 S1-R 0.32
    5 Keydime D10 S1 0.3612
    6 Keydime D10 S2 0.4088
    7 Keydime D10 S3 0.4330
    8 Keydime D10 S1-R 0.32
    9 Keydime D125 S2 0.4102
    10 Keydime D125 S3 0.4191
  • Examples 5 to 10 are comparison examples employing cationically-stabilised AKD sizing agents.
  • The codes S1, S2, S3 and S1-R describe the sample preparation techniques used:
  • Keydime SP1 is a dispersant containing sodium lignosulphonate and the sodium salt of naphthalene sulphonic acid. It is available from Albright & Wilson Limited. Keydime D10 and Keydime D125 are cationically stabilised AKD sizing agents containing, on a dry weight basis, 10% AKD (the palmitic-stearic compound mentioned above) and, respectively, 2.5% and 1.25% cationic polymer. Keydime D10 and Keydime D125 are also available from Albright & Wilson Limited.
  • TABLE 2 Addition sequence
    • S1
      • (1) 8.0lb/T (4.0 kg/t) Kymene 557 (polyamide amine epichlorohydrin, available from Hercules Powder Co.)
      • (2) 7.0lb/T (3.5 kg/t) AKD (palmitic-stearic dimer)
      • (3) 1.0lb/T (0.5 kg/t) alum
      • (4) 4.0lb/T (2.0 kg/t) Accostrength 85 (an anionic dry strength agent comprising polyacrylamide dry polymer on dry fibre)
      • (5) 10.0lb/T (5.0 kg/t) Staklok 400 (cationic corn starch, available from Staley Manufacturing Co.)
    • S2
      • (1) 8.0lb/T (4.0 kg/t) Kymene 557
      • (2) 7.0lb/T (3.5 kg/t) AKD (as above)
      • (3) 1.0lb/T (0.5 kg/t) alum
      • (4) 10.0lb/T (5.0 kg/t) Staklok 400
      • (5) 4.0lb/T (2.0 kg/t) Accostrength 85
    • S3
      • (1) as S1
      • (2) 7.0lb/T (3.5 kg/t)AKD (as above) and 10.10lb/T (5.0 kg/t) Staklok 400, premixed
      • (3) 1.0lb/T (0.5 kg/t) alum
      • (4) 4.0lb/T (2.0 kg/t) Accostrength 85
  • S1-R as S1 but with recirculation
  • In each addition sequence, the AKD was added together with the Keydime SP1 (in examples 1 to 4) and as a component of the Keydime D10 or D125 (in examples 5 to 10), an AKD-Keydime SP1 emulsion having been formed by melting the AKD at 65 to 80°C, dissolving the molten AKD in water at 65 to 80°C and homogenising the mixture with Keydime SP₁ at 2500 to 3000 psi.
  • Examples 1 to 4, when compared with Examples 5 to 10, show fluid pick-ups (edgewick) with anionic agents comparable to or better than those of cationic agents. Examples 4 and 8 show that better results can be attained with recirculation which most realistically simulates the papermaking process.
  • EXAMPLES 11 to 15 and COMPARISON EXAMPLE 16
  • Edgwick evaluation tests consisting of two parts:
    • (1) Formation of sheets, and
    • (2) Coating and lactic acid tests
    were carried out on six further sizing compositions. The results are clearly indicative of the fact that anionic active sizing compositions perform well in the tests and are suitable for use in sizing papers for the liquid packaging industry. Procedure
  • Stock used was 50/50 hardwood/softwood beaten to a Schopper Reiglar of 40°.
    Chemical Additions
    Thickstock:
    3.2% A/R Wet strength resin (Kymene 557)
    0.35% AKD/Fibre sizing composition
    Thinstock
    0.05% Dry Alum/Fibre
    2 kg/t Accostrength 85
    1% Dry Stalok 400
  • The procedure was followed for each of five sizing compositions having the following constituents:
    • Example 11
      100g Ketene Dimer (palmitic-stearic)
      1.25g Orotan (surfactant)
      4.5g Wanin (surfactant)
      800g Water
    • Example 12
      100g Ketene Dimer (palmitic-stearic)
      1.25g Orotan
      4.5g Wanin
      1.5g Percol 155 (50% solid Anionic Polyacrylamide)
      800g Water
    • Example 13
      100g Ketene Dimer (palmitic-stearic)
      1.25g Orotan
      4.5g Wanin
      666g BMA (contains anionic silica) (15% solids)
      133g Water
    • Example 14
      100g Ketene Dimer (palmitic-stearic)
      1.25g Orotan
      4.5g Wanin
      333g 1/2 BMA
      166g Water
    • Example 15
      100g Ketene Dimer (palmitic-stearic)
      1.25g Orotan
      4.5g Wanin
      2.5g Lab 998 (ex Roquette) Anionic Starch
      425g Water
  • After combination of the above materials, further water was added to adjust the compositions to an AKD solids content of 10% by weight.
  • The tests consisted of two parts:
  • Part 1:
  • 250 gsm sheets were produced on laboratory sheet-­forming apparatus and the consistency of the thinstock was 0.5%.
  • The sheets were dried at 105°C for 8 minutes then oven cured for 5 minutes.
  • Part 2:
  • Lactic acid immersion tests were carried out on the sheets. The sheets were coated with tape and cut to 12.5cm x 5cm strips. These strips were weighed before immersion in 2.5cm of 1% lactic acid for 16 hours. The strips were then reweighed and the pickup calculated in grams. The average of 3 results was taken for each sizing composition.
  • The edgewick tests gave the following results:
    Example Edgewick (g) % Pickup
    11 0.227 6.8
    12 0.174 7.2
    13 0.316 12.7
    14 0.317 12.8
    15 0.185 7.6
    16 0.181 7.9
    Example 16 is a comparison example using Keydime D10. These results overall indicate that anionic AKD sizing compositions perform as well if not slightly better than compositions in situations where high levels of cationicity are present. The compositions are therefore suitable for use in the liquid packaging industry.
  • EXAMPLES 17 to 19
  • A series of anionic size compositions were prepared and tested:
    Composition 1 2 3
    Additive/Dispersant:
    Naphthalene Sulphonic Acid 1.25 1.25 1.25
    Na Lignosulphonate 4.5 4.5 4.5
    Anionic Polyacrylamide - 1.2 -
    Colloidal Silica - - 37.5
    Alkyl Ketene Dimer (Palmitic/Stearic) 100 100 100
  • All amounts are expressed as dry grams of material.
  • Emulsion Manufacture Procedure
  • In each case the process water was acidified prior to the addition of dispersants. The mixture was heated to 70°C before addition to a laboratory homogenizer which was preheated to the same temperature. Homogenization pressure was adjusted to 3500 psig (24 M Pa) (ideally 2500 to 5000 psig (17 to 34 M Pa)). Molten alkyl ketene dimer wax was added at 70°C and allowed three theoretical passes plus one to discharge. Upon discharge, the product was passed through a 200 mesh filter and the temperature rapidly reduced to below 20°C.
  • Laboratory Procedures a) Stock Preparation
  • All work was performed on a 50:50 mixture of hardwood and softwood beaten in a Valley Beater to 40°SR (300 CSF).
  • b) Chemical Additives
  • Chemical additions were made using syringes having an accuracy of ± 0.1 cm³. All chemical additives except precipitated calcium carbonate were diluted prior to use for accuracy of addition.
  • The precipitated calcium carbonate used for this work was a commercially available grade Albacar HO made at 20% solids with no dispersant added. Particle size averaged 2.7 microns with a Zeta potential of +5 mV.
  • c) Size Testing
  • The size test employed in this work was a 2-minutes Cobb test under standard conditions.
  • Results
  • Chemical Additions - lbs/ton dry basis on fibre
    Example Thickstock Starch Filler Size/Comp Thinstock Retention Aid 2-Min. Off Dryer Cobb Oven Cured Sizing g/m² Natural Cured
    17 10.0 300 3.0(1) 0.5 40 40 41
    18 10.0 300 3.0(2) 0.5 36 36 37
    19 10.0 300 3.0(3) 0.5 44 41 38
  • Machine Trial Data
  • Anionic size composition (1) of Example 11 was tested against a competitive, cationically stabilized size, Aquapal C348 supplied commercially by Hercules Powder Co. Sizing was measured to a standard 1-min. Cobb test.
    Machine Furnish on 60g/m² Wove grade
    Fibrous - Chemithermal mechanical pulp 50%
    White Offcuts 17%
    White Letter Waste 17%
    White Waste Rejects 8%
    Own Broke 8%
  • Chemicals
  • Retention Aid - Cationic Polyacrylamide Nalfloc 4662 commercially available from Nalco Ltd.
    Fillers - Calcium carbonate addition to a specified sheet ash of 23% w.o.f.
    Size Type Size Addition % as Received Retention Acid Addition g/tonne % Sheet Ash Sizing/mm Cobb Oven Cured 3 min at 105°C
    Aquapel C348 3.7 257 23.4 17.7
    Composition(1) 1.6 257 22.9 16.9
  • These results are averaged over a period of 5 hours of continuous machine operation.

Claims (15)

1. An active sizing composition comprising an aqueous emulsion of a reactive sizing agent and an anionic dispersant and/or emulsifier serving to stabilise the emulsion, the reactive sizing agent comprising at least one compound according to the formula
Figure imgb0002
wherein R₁ and R₂, which may be the same or different, are hydrocarbon radicals each having at least six carbon atoms.
2. A sizing composition according to claim 1, in which R₁ and R₂ are, independently of each other, alkyl, alkenyl, cycloalkyl, aryl, aralkyl or alkaryl radicals.
3. A sizing composition according to claim 2, in which R₁ and R₂ are, independently of each other, C₁₂ to C₂₂ alkyl groups.
4. A sizing composition according to any preceding claim, in which te anionic dispersant or emulsifier comprises one or more of sodium lignosulphonate, calcium lignosulphonate and the sodium salt of the naphthalene sulphonic acid.
5. A sizing composition according to any preceding claim, in which the dispersant or emuslifier is present in an amount of 0.5% to 10% based on the weight of the reactive sizing agent.
6. A sizing composition according to any preceding claim, including at least one substance wich extends or modifies the anionic charge density of the composition.
7. A sizing compositions according to claim 6, in which the extender or modifier comprises one or more anionic polyacrylamides, anionic starch or colloidal silica.
8. A sizing composition according to any preceding claim, containing reactive sizing agent in an amount of 5% to 20% by weight of the composition.
9. A sizing composition according to claim 8, in which the amount is 10% to 15% by weight of the composition.
10. A method of sizing paper, using a composition according to any preceding claim.
11. A method according to claim 10, in which the sizing is carried out in the presence of a cationically charged substance.
12. A method according to claim 11, in which the cationically charged substance is a filler or a retention aid.
13. A method according to claim 10, in which the sizing is carried out in the presence of a fluorescent whitening agent.
14. A method according to any of claims 10 to 13, which is carried out at the wet end of a paper making process.
15. Sized paper made by a method according to any of claims 10 to 14.
EP90309876A 1989-09-11 1990-09-10 Active sizing compositions Withdrawn EP0418015A1 (en)

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GB898920456A GB8920456D0 (en) 1989-09-11 1989-09-11 Active sizing compositions

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BR (1) BR9004518A (en)
CA (1) CA2024975A1 (en)
FI (1) FI904444A0 (en)
GB (1) GB8920456D0 (en)
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ZA (1) ZA907216B (en)

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DE4227184A1 (en) * 1992-08-17 1994-02-24 Dresden Papier Ag Impregnation agent for the production of papers with high penetration resistance against fats, oils and aqueous media
WO1994013883A1 (en) * 1992-12-04 1994-06-23 Raisio Chemicals Oy Process for the preparation of a hydrophobic sizing agent dispersion
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WO1996017127A1 (en) * 1994-12-02 1996-06-06 Eka Chemicals Ab Sizing dispersions
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WO1997031152A1 (en) * 1996-02-23 1997-08-28 Allied Colloids Limited Sizing of paper
ES2105962A1 (en) * 1995-03-13 1997-10-16 Majo Buj M Teresa Process for the application of lignosulphonates to the mass for the formation of paper
WO1998033980A1 (en) * 1997-02-05 1998-08-06 Akzo Nobel N.V. Aqueous dispersions of hydrophobic material
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US6165259A (en) * 1997-02-05 2000-12-26 Akzo Nobel N.V. Aqueous dispersions of hydrophobic material
US6194057B1 (en) 1998-11-12 2001-02-27 Paper Technology Foundation Inc. Partially impregnated lignocellulosic materials
US6211357B1 (en) 1999-12-09 2001-04-03 Paper Technology Foundation, Inc. Strengthening compositions and treatments for lignocellulosic materials
US6268414B1 (en) 1999-04-16 2001-07-31 Hercules Incorporated Paper sizing composition
US6281350B1 (en) 1999-12-17 2001-08-28 Paper Technology Foundation Inc. Methods for the reduction of bleeding of lignosulfonates from lignosulfonate-treated substrates
US6537616B2 (en) 1998-11-12 2003-03-25 Paper Technology Foundation Inc. Stam-assisted paper impregnation
US6537615B2 (en) 1998-11-12 2003-03-25 Paper Technology Foundation Inc. Steam-assisted paper impregnation
WO2003056099A1 (en) * 2001-12-21 2003-07-10 Akzo Nobel N.V. Aqueous silica-containing composition and process for production of paper
WO2003056100A1 (en) * 2001-12-21 2003-07-10 Akzo Nobel N.V. Aqueous silica-containing composition and process for production of paper
WO2003074787A1 (en) 2002-03-04 2003-09-12 Amcol International Corporation Paper and materials and processes for its production
WO2004022848A1 (en) * 2002-08-14 2004-03-18 Basf Aktiengesellschaft Method for glueing paper, paperboard and cardboard
WO2005042842A1 (en) * 2003-10-23 2005-05-12 Basf Aktiengesellschaft Mixtures of solids, consisting of a reactive sizing agent and starch, method for producing said mixtures and use thereof
US7156955B2 (en) 2001-12-21 2007-01-02 Akzo Nobel N.V. Papermaking process using a specified NSF to silica-based particle ratio
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WO1994013883A1 (en) * 1992-12-04 1994-06-23 Raisio Chemicals Oy Process for the preparation of a hydrophobic sizing agent dispersion
EP0686727A2 (en) * 1994-04-08 1995-12-13 PTS Papiertechnik Beteiligungsgesellschaft mbH Sizing composition for internal and surface sizing of paper
EP0686727A3 (en) * 1994-04-08 1996-03-27 Pts Papiertechnik Beteiligungs Sizing composition for internal and surface sizing of paper
US5876562A (en) * 1994-12-02 1999-03-02 Eka Chemicals Ab Sizing dispersions
WO1996017127A1 (en) * 1994-12-02 1996-06-06 Eka Chemicals Ab Sizing dispersions
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US6284099B1 (en) 1996-02-23 2001-09-04 Ciba Specialty Chemicals Water Treatments Limited Sizing of paper
WO1998033979A1 (en) * 1997-02-05 1998-08-06 Akzo Nobel N.V. Sizing of paper
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US6165259A (en) * 1997-02-05 2000-12-26 Akzo Nobel N.V. Aqueous dispersions of hydrophobic material
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WO2000023651A1 (en) * 1998-10-16 2000-04-27 Basf Aktiengesellschaft Aqueous sizing agent dispersions adjusted to be anionic or cationic and designed for paper sizing
WO2000029670A1 (en) * 1998-11-12 2000-05-25 Paper Technology Foundation Inc. Strengthening compositions and treatments for lignocellulosic materials
US6537616B2 (en) 1998-11-12 2003-03-25 Paper Technology Foundation Inc. Stam-assisted paper impregnation
US6537615B2 (en) 1998-11-12 2003-03-25 Paper Technology Foundation Inc. Steam-assisted paper impregnation
US6194057B1 (en) 1998-11-12 2001-02-27 Paper Technology Foundation Inc. Partially impregnated lignocellulosic materials
US6114471A (en) * 1998-11-12 2000-09-05 The Proctor & Gamble Company Strengthening compositions and treatments for lignocellulosic materials
US6268414B1 (en) 1999-04-16 2001-07-31 Hercules Incorporated Paper sizing composition
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US6458419B2 (en) 1999-12-17 2002-10-01 Paper Technology Foundation Inc. Methods for the reduction of bleeding of lignosulfonates from lignosulfonate-treated substrates
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US6281350B1 (en) 1999-12-17 2001-08-28 Paper Technology Foundation Inc. Methods for the reduction of bleeding of lignosulfonates from lignosulfonate-treated substrates
NO337087B1 (en) * 2001-12-21 2016-01-18 Akzo Nobel Nv Aqueous silica-containing composition and process for making paper
US7156955B2 (en) 2001-12-21 2007-01-02 Akzo Nobel N.V. Papermaking process using a specified NSF to silica-based particle ratio
WO2003056099A1 (en) * 2001-12-21 2003-07-10 Akzo Nobel N.V. Aqueous silica-containing composition and process for production of paper
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US7608644B2 (en) 2001-12-21 2009-10-27 Akzo Nobel N.V. Aqueous silica-containing composition
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WO2003074787A1 (en) 2002-03-04 2003-09-12 Amcol International Corporation Paper and materials and processes for its production
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US7294190B2 (en) 2003-10-23 2007-11-13 Basf Aktiengesellschaft Mixtures of solids, consisting of a reactive sizing agent and starch, method for producing said mixtures and use thereof
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US10144671B2 (en) 2014-10-23 2018-12-04 Basf Se Process for hydrophobization of concrete

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ZA907216B (en) 1991-07-31
BR9004518A (en) 1991-09-10
CA2024975A1 (en) 1991-03-12
AU6231790A (en) 1991-03-14
NO903926L (en) 1991-03-12
JPH03167391A (en) 1991-07-19
FI904444A0 (en) 1990-09-10
GB8920456D0 (en) 1989-10-25
NO903926D0 (en) 1990-09-10

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