NZ541746A

NZ541746A - Modification of paper coating rheology

Info

Publication number: NZ541746A
Application number: NZ541746A
Authority: NZ
Inventors: Howard Roger Dungworth; David Petty; Olli Juhani Jokinen
Original assignee: Ciba Spec Chem Water Treat Ltd
Priority date: 2003-02-26
Filing date: 2004-02-16
Publication date: 2008-02-29
Also published as: KR20050104398A; TW200427901A; WO2004076743A2; JP2006519280A; EP1611283A2; NO20053948L; CN1754023A; AU2004215224A1; AR043384A1; RU2005129548A; US20060148938A1; CA2517055A1; PL377002A1; BRPI0407872A; GB0304354D0; CN100385074C; MXPA05009109A; CL2004000332A1; WO2004076743A3

Abstract

Disclosed is a paper coating composition which includes a thickener composition for modifying the rheology of paper coatings, the thickener composition comprising an associative thickener, wherein the associative monomer content of the thickener is below 10%, the molecular weight of the thickener is below about 1 million and the acid content is at least 10% by weight.

Description

<div class="application article clearfix" id="description"> WO 2004/076743 PCT/EP2004/001426 Modification of Paper Coating Rheoloav This invention relates to paper coating and more particularly the modification of paper coating rheology. 5 Various types of polymeric thickeners are well documented in the prior art. Often these are in the form of aqueous emulsions which are either alkali soluble or alkali swellable. 10 WO-A-OO/34361 describes a comb polymer comprising a backbone of hydrophilic units and dihalogeno compounds and a moiety contain pendent hydrophobe, being particularly suited as a thickener for latex paints. The hydrophobic group is attached to the backbone of the preformed polymer. 15 W0-A-02/12360 describes an aqueous dispersion of copolymeric microparticles, useful as an associative thickener in coating compositions such as paints. The thickeners exemplified include at least 10% by weight associative monomer. 20 US 5478602 describes coating a substrate by applying an aqueous coating composition containing an alkali swellable complex hydrophobe associative thickener. Since the polymer is alkali swellable it must be so substantially cross-linked that the polymer is not soluble. 25 it is well known that associative thickeners bring about low high shear viscosity at small dosages. They can thus give an economic advantage over other types of synthetic thickeners. However an equally well known problem with associative thickeners is that they provide poor water retention. So the economic advantage of associative thickeners is normally only obtained in 30 conditions where water retention is not important. WO 2004/076743 PCT/EP2004/001426 2 Water retention of coating colours has a profound influence on the runnability of the paper coating process. The coating colour loses a large proportion of the water that it contains as soon as it comes into contact with the surface of the paper owing to capillary action, the extent of which depends on the absorbency 5 of the substrate. The pressure in the nip and under the blade also promotes dewatering. The release of water from the coating colour can have the following consequences: The solids content of the wet coating increases which modifies the rheology of 10 the coating before it comes into contact with the blade. In the worst case the coating can form a thick, immobile "filter cake" which can cause streaking and might even cause the web to break. The water taken up by the paper causes a reduction in its internal bonding 15 strength which causes it to tear more easily under tension. The solids content of the coating colour re-circulated from the coater head can increase by 5% and more over a period of a few hours because the concentration of water soluble polymer in the coating colour is also much lower 20 if too much water is released. This phenomenon is often observed at the precoating stage. It becomes more difficult to apply an even coat as the solids content of the coating colour increases. The blade pressure often has to be increased in 25 order to maintain a constant coat weight. In the manufacture of paper there is a tendency to seek ever higher coating speeds and this requires lower high shear viscosity. Although low high shear viscosity can be provided by associative thickeners the low water retention of 30 those thickeners can result in water from the coaling permeating the paper thus weakening the paper. This in turn can place an unacceptable limit on the 3 coating speed. In addition rapid release of water from the coating may prevent the desired smoothing of the coating. When the coating composition does not exhibit low high shear viscosity the rod 5 pressure of the coating apparatus can increase significantly. On the other hand when the coating composition results in poor water retention on the rod pressure tends to be unstable. In both instances in this can result in damage to the coated paper and/or poor runnability of the coater. 10 In order to improve the water retention other products need to be added together with the associative thickeners and the economic advantage of those thickeners is no longer obtained. As far as we are aware no proposals have been made for improving water retention when using associative thickeners in paper coating without the addition of an additional water retention aid so as to 15 obtain the economic benefits of using associative thickeners for paper coating. The present invention has been made in order to address this problem, or to at least provide a useful alternative to known coatings. 20 According to the invention there is provided a paper coating composition which includes a thickener composition for modifying the rheology of paper coatings, the thickener composition comprising an associative thickener wherein the associative monomer content of the thickener is below 10%, the molecular weight of the thickener is below about 1 million, and the acid content is at least 25 10% by weight. We have discovered that the adjustment of the three parameters, associative content, molecular weight and acid content within the limits defined above provides an associative thickener composition which results in both low high 30 shear viscosity and good water retention without the necessity for the addition of a water retention aid. INTELLECTUAL PROPERTY OFFICE OF W.Z. - 1 NOV 2007 p p n c \ v/ p O WO 2004/076743 PCT/EP2004/001426 4 It must be understood that while the three above mentioned parameters are seen as essential for obtaining the desired combination of low high shear viscosity and good water retention the dosage of the thickener will also have an effect on the performance of the thickener. For example lowering of the 5 molecular weight may require an increase in the dosage if the desired viscosity is to be obtained. In addition, lowering the acid content can lower the efficiency of the thickener so that an increase in dosage may be needed. Once these consequences have been appreciated the appropriate adjustment becomes a matter for a limited amount of experimentation in order to obtain the desired 10 result Associative thickeners for obtaining low high shear viscosity are well known. They comprise hydrophilic, water soluble polymers with hydrophobic terminal groups or side chains. The hydrophobic terminal groups may be aliphatic or 15 aromatic hydrocarbons and they are water insoluble. They can be joined to the hydrophilic polymer backbone by means of a hydrophilic spacer so that they remain flexible. Their structure is similar to that of surfactants. Interaction > between the hydrophobic groups or side chains is what is considered to provide for very high viscosity at low shear. There are various types of associative 20 thickeners but those which are generally useful for the purpose of the present invention are formed from ethylenically unsaturated monomers such as (meth) acrylic acid, (meth) acrylates, maleic acid or anhydride, maleates, itaconic acid, itaconates, allyl ethers and vinyl esters. Ideally the choice of monomers is such that the polymer is insoluble in water and at neutral pHs, but dissolves under 25 alkali conditions, for instance pH 8 to 10 or higher. The polymers are typically made by aqueous emulsion polymerisation of the monomers to form an aqueous emulsion of a polymer. Polymers of particular interest in connection with the present invention are the hydrophobic alkali-soluble emulsions in which the hydrophilic polymer backbone comprises an alkali-soluble polyacrylate 30 derived from monomers such as alkyl acrylates for example ethyl acrylate, acrylic acid and methacrylic acid. The hydrophibic side chains are attached to WO 2004/076743 PCT/EP2004/001426 5 the polymer backbone by, for example, a poiyoxyethylene oxide spacer. Normally the hydrophobic side chains are provided by including ethylenically unsaturated monomers that contain the hydrophobic side chains. Typically the hydrophobic side chains are C8-C30 alkyl groups. Thus the hydrophobic side 5 chain moiety can be bonded to ethylenically unsaturated components such as acrylamido, acrylate or allyloxy etc.The thickening effect can be adjusted by altering the ratios of the monomers. All this is well known. Examples of associative thickeners used as paint thickeners, printing pastes and the like are disclosed in European Patent Specification 0 216 479 A1. Other associative 10 thickeners are described in detail in European Patent Specification 0 013 836 A1 and 0 011 806 A1. These can be used in the present invention subject to their being modified in accordance with the definition of the invention as set out above. 15 We have found that associative thickeners must have the special combination of an acid content of at least 10% by weight and an associative monomer content of below 10% of molecular weight below 1 million. Molecular weights of below 700,000 have been found to be particularly suitable for use in the present invention. An especially preferred molecular weight range is 70,000 to 150,000, 20 and most preferably 70,000 to below 100,000. The polymers may be made by the inclusion of branching or cross-linking agents and/or chain transfer agents. However, it is preferred that the amounts of branching or cross-linking agents are used in amounts such that the polymer 25 is substantially soluble in at least in alkali. Thus the polymer may be substantially linear, branched or slightly cross-linked. Nevertheless, the polymers desirably should not be so cross-linked that it is insoluble. The amount of cross linking agent is generally below 2000 ppm (by weight) and preferably below 1000 ppm. Typically the amount of cross-linking agent will be 30 below 500 ppm, for instance in the range of 1 or 2 ppm up to for instance 100 ppm, preferably 5 ppm up to 20 or 30 ppm. The cross-linking agent can be a WO 2004/076743 PCT/EP2004/001426 6 polyethylenically unsaturated monomer, for instance methylene bis acrylamide, butane diol diacrylate and tetra allyl ammonium chloride. Preferred thickeners for use in the invention are alkali soluble aqueous 5 emulsions of ethyl acrylate/methacrylic acid/steareth 10 mole ethoxylate allyl ether and having a molecular weight below 1 million and preferably in the range 10,000 to 700,000 and more preferably in the range 50,000 to 200,000 or 250,000, and most preferably 70,000 and to below 100,000. Cross linkers and initiators can be included if desired. 10 These polymers are mildly associative their associative content being preferably not above 5% and more preferably below 2.5%. The acid functionality may be provided by any suitable acid, methacrylic acid, 15 acrylic acid or a mixture thereof being preferred. The acid content can be from 10 to 70%, preferably 20 to 50% by weight (based on the weight of polymer). As already indicated the precise values of the above parameters are chosen • having regard to the viscosity and water retention that the particular coating operation demands and to the dosage of the thickener in the coating 20 composition. In use the thickener of the invention is included in a conventionally formulated coating composition for a pre-coat or top coat. The dosage of the thickener of the invention in the coating composition is kept as low as possible consistent 25 with the required viscosity being obtained. For example, in many top coat formulations a dosage of thickener of 0.2pph will give a target Brookfield viscosity of about 1000 to 1400 mPas at 100 rpm (typical for "roll and blade" coating method) in combination with good water retention of the order of 100 g/m2 or lower. Unless otherwise stated the viscosity is measured at 25°C. 30 WO 2004/076743 PCT/EP2004/001426 10 The target viscosity will to some extent be chosen having regard to the coating method that is to be used. Thus for film press a target Brookfield viscosity is of the order of 700 to 1000 mPas whereas for a jet applicator the target Brookfield viscosity is of the order of 2000 to 2500 mPas. In some instances the dosage may need to be altered in order to obtain the required viscosity. Of course, changing the dosage of thickener to obtain the desired viscosity can also change the water retention. However adjustment of the acid content of the thickener can, in those circumstances, be used in order to secure good water retention. When used the coating composition is preferably mildly alkaline, of the order of pH 8 to 10, preferably 8.5 to 9.5. Where necessary the pH can be adjusted for example by the addition of an alkali such as sodium hydroxide. 15 The invention also provides a method of modifying the rheology of a paper coating composition comprising adding to the coating composition a thickener as defined above. Further the invention provides a paper coating method comprising coating paper 20 or paperboard with a paper coating composition, said composition including a thickener as defined above. The thickeners of the invention can be used in all methods of paper coating and at all possible coating weights for example from 2 to 25 g/m2. The thickeners 25 can be used in coating compositions for pre-coat, middle coat and top coat and can be used with any pigments and binders. The following examples further illustrate the invention: 30 WO 2004/076743 PCT/EP2004/001426 8 Example 1 Preparation of associative thickener. 5 into a 700ml resin pot fitted with stirrer, thermometer, nitrogen inlet and outlet, condenser and feed lines was placed 157.62gms deionised water and 10.5gms Disponil FES993 (Alkylether sulphate, sodium salt). The contents of the resin pot were heated to 85°C and then degassed with 10 nitrogen for 30 minutes. An aqueous emulsion was prepared by mixing 143.75gms ethyl acrylate, 100.00gms methacrylic acid, 6.25gms steareth-10 ethoxylate allyl ether and 1.25gms n-dodecyl mercaptan into 10.5gms Disponil FES993 in 162.62gms 15 deionised water. An initiator feed was prepared by dissolving 0.50gms ammonium persulphate in 37.5gms water. 20 After degassing, 0.25gms ammonium persulphate dissolved in 5gms water was added to the reactor followed by the start of the emulsion and initiator feeds over 2 and 3 hours respectively. The contents of the reactor were held between 83 and 87°C during the feed 25 time and held for a further 1 hour at 85°C to reduce residual monomer content. The contents were then cooled to <40°C and filtered. This resulted in an aqueous emulsion polymer having a molecular weight of 30 about 150,000 with a solids content of 41.0%. WO 2004/076743 PCT/EP2004/001426 9 Example 2 A top coat was prepared according to the following recipe: 5 Mix @ 1200cps 60 parts CaCCk (Carbital 95) 40 parts Clay (Suprawhite 95) 10 parts SB latex (DL 950) Solids content: 60% 10 Different thickeners were added to the mix and the pH adjusted by the addition of 1.0% sodium hydroxide solution. The dosages of thickener and the high shear viscosity and water retention obtained are set out in the following Table 1. 15 Table 1 Parity Amount AA- Cone Sample Dose (against pH 1% Brookfield GWR(gsm) & (PPh) control) NaOH Viscosity Water Plate, (mis) Retention HSV Blank - - 8.57 4.50 148 232 28 Control 0.60 100 8.67 5.50 1190 155 47 (CMC) A 0.20 33 8.60 9.00 1150 215 43 B 0.315 53 8.54 11.0 1290 153 40 C 0.33 55 8.62 11.0 1140 153 48 D 0.34 57 8.52 11.0 1160 157 35 E 0.45 75 8.45 13.0 1270 146 41 The composition of the control and samples A to E were as follows (all percentages by weight): WO 2004/076743 PCT/EP2004/001426 10 Control: Commercially available carboxymethyl cellulose A: Commercially available hydrophobic alkali swellable emulsion HASE B: Ethyl acrylate 55% methacrylic add 40%; steareth 10 ethoxylate allyl 5 ether 5% C: Ethyl acrylate 57.5% methacrylic acid 40%; steareth 10 ethoxylate allyl ether 2.5% D: Ethyl acrylate 58% methacrylic acid 40%; steareth 25 methacrylate 2% 10 E: Ethyl acrylate 58% methacrylic acid 40%; steareth 10 ethoxylate allyl ether 2% Compositions B to E also included about 5000 ppm of n-dodecyl mercaptan. 15 For the evaluation of the results the compositions of the invention were judged by comparison of their viscosity and water retention with the control sample where the thickener was carboxymethyl cellulose and HASE thickener A. The thickeners of the invention gave lower high shear viscosity than control and about the same water retention. The HASE thickener gave about the same 20 high shear viscosity as the thickeners of the invention, but significantly worse water retention. Note that the dosage of HASE thickeners and the thickeners of the invention was about the same. Water Retention GWR (gsm) 25 The water retention was measured in gsm on a gravimetric water retention meter using the parameters of 2 minutes dwell time, 1.5 bar pressure and 5pm polycarbonate membrane filters. High Shear Viscosity (HSV) 30 The high shear viscosity was measured in mPas on a cone and plate viscometer at 10000s"1- WO 2004/076743 PCT/EP2004/001426 11 Example 3 Certain of the samples used in Example 2 were added to a top coat 5 composition. The dosages and the resultant viscosity and water retention are shown in the following Table 2. Sample Dosage Brookfield ACAV Water Haake PPh Viscosity (100 rpm) 0.6M 1/s Retention 3000 1/s mPas mPas g/m2 mPas Control 0.6 1210 43 88 42 A 0.185 1280 38 123 31 B 0.2 1240 36 100 29 C 0.25 1400 37 93 31 The results confirm the results of Example 2, i.e. with the thickeners of the 10 invention (B and C) it is possible to get low high shear and good water retention. On the other hand typical HASE thickener (A) also gives low high shear viscosity but poor water retention. ACAV measured with a capillary viscometer in which pressure in a cylinder 15 forces the sample through a capillary. By measuring pressure in the cylinder and knowing the flow rate of the sample through the capillary the shear rate and viscosity of the sample can be determined. Water retention was measured on a gravimetric water retention meter using the 20 parameters of 2.0 minutes dwell time, 0.5 bar pressure and 5 micrometer membrane filters using a 20 ml sample. (Water retention was measured in the same way in the following Examples 4 and 5). WO 2004/076743 PCT/EP2004/001426 12 Example 4 A pre-coat formulation was prepared as follows: 100 parts CaC03 5 10 parts SB-latex Solids content: 63.0% pH: 9 The target Brookfield viscosity (100 rpm): 900 mPas 10 Samples were added to the pre-coat formulation in the dosages set out in the following Table 3 which also shows the resultant viscosity and water retention. Table3 15 Sample Dosage Brookfield ACAV Water Haake PPh Viscosity (100rpm) 0.6M 1/s Retention 3000 1/s mPas mPas g/m2 mPas Control 0.75 805 33 207 44 A 0.18 900 27 202 29 B 0.3 945 26 137 33 C 0.45 1060 27 120 38 The results show that the control sample and the HASE thickener A provide a poor water retention whereas the thickeners of the invention provide the 20 required viscosity and good water retention. Example 5 A pre-coat formulation was made up as follows: WO 2004/076743 PCT/EP2004/001426 13 100 parts CaC03 6 parts SB latex 6 parts starch 5 Solids content: 62% pH: 8.5 Target Brookfield viscosity (100 rpm): 800mPas 10 Samples of thickener compositions were added to the pre-coat formulation in the dosages shown in Table 4 which also sets out the resultant viscosity and water retention. Table 4 15 Sample Dosage Brookfield ACAV Water PPh Viscosity (100rpm) 0.6M 1/s Retention mPas mPas g/m2 Control 0.2 810 52 116 A 0.15 840 53 88 B 0.25 840 54 64 C 0.29 800 50 65 The results show better water retention for the control and HASE thickener A than in the pre-coat formulation of Example 4, which does not contain starch. 20 However the thickeners of the invention have significantly further improved water retention. WO 2004/076743 PCT/EP2004/001426 14 Example 6 Various coating formulations were prepared employing thickener compositions selected from a commercial HASE thickener, a commercial ASE thickener and 5 in a thickener composition according to the invention. The composition of the coating formulation is a shown in Table 5. Table 5 Materials 1 2 3 4 8 9 10 14 15 16 Premier 75 75 75 75 75 75 75 75 75 75 Hydrocarb 90 25 25 25 25 25 25 25 25 25 25 Dispex N. 40 0.15 0.15 0.15 0.15 0.15 0.15 0.15 0.15 0.15 0.15 TSPP 0.05 0.05 0.05 0.05 0.05 0.05 0.05 0.05 0.05 0.05 Dow 620 16 16 16 16 16 16 16 16 16 16 AZC 0.2 0.2 0.2 0.2 0.2 0.2 0.2 0.2 0.2 0.2 Glosscole 50 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 Commercial HASE thickener 0 0 0 0 0 0 0 0.1 0.2 0.26 Commercial ASE thickener 0 0.1 0.2 0.4 0 0 0 0 0 0 Sample F .. o. 0 0 0 0.1 0.2 0.4 0 0 0 pH 8.5 8.5 8.5 8.5 8.5 8.5 8.5 8.5 8.5 8.5 solids 66 66 66 66 66 66 66 66 66 66 10 Sample F: Ethyl acrylate 57.5% methacrylic acid 40%; steareth 20 ethoxylate allyl ether 2.5% The following tests were carried out on the formulations: WO 2004/076743 PCT/EP2004/001426 15 Measure Brookfield viscosity, 20 rpm, 100 rpm at 4 min. Measure AAGWR at 2 bar pressure for 2 minutes Measure Hercules High Shear viscosity, ( FF bob.6600 rpm, 138,5341/sec). 5 Run twice with 3 minute delay between measurements. The results are shown in Table 6 Table 6 Results 1 2 3 4 8 9 10 14 15 16 %solids 66.57 66.29 66.39 66.37 66.45 66.59 66.2 66.34 66.47 66.67 pH 8.59 8.79 8.45 8.85 8.78 8.75 8.3 8.35 8.37 8.32 Brookfield viscosity 4/20 804 1812 5200 10700 1990 3222 7500 4080 12810 19020 Brookfield viscosity 4/100 289 560 1512 2880 642 1022 2244 1626 3480 5208 Hercules,cps 64.3 61.3 72.5 91.1 60.7 74.8 72.2 72.8 69 77 hysterisis L L L M L M M L M M-H AAGWR (g/m2) 276.4 187.6 143 110.7 195.7 164.1 115 234 173.3 152.4 10 The results show that sample F provides an excellent combination of low high shear viscosity and water retention values. In addition sample F exhibits significantly improved water retention than the conventional associative 15 thickener (commercial HASE). This is also clear from Figure 1. Example 7 WO 2004/076743 PCT/EP2004/001426 16 Thickener composition sample F was used in and in a coating foimulation to coat paper in a pilot trial. Details of the conditions used are as follows: 10 5 Base paper Speed: Coat weight: Coating unit 15 20 Recipes: - Pigment mixture - SB-latex (DL 920) - Starch (Raisamyl 302E) - FWA (Blankophor P) -Sample F The results are shown in Table 7. 42 g/m2 1820 m/min 7 g/m2/side Film press, one-sided Reference Sample F 100 parts 100 parts 8 parts 8,5 parts 6 parts 3,5 parts 0,6 parts 0,6 parts - 0,2 parts WO 2004/076743 PCT/EP2004/001426 17 Table 7 Reference Sample F Coating color properties - Brookfield, at the beginning 556 540 - Brookfield, in the middle 572 574 - Brookfield, at the end 574 564 - Solids, at the beginning 59.3 59.2 - Solids, in the middle 59.5 59.3 - Solids, at the end 59.6 59.4 - Water retention 111 95 -pH 8.8 8.6 -Temperature 36 33 Rod pressure, bar - 1st side - at the beginning 166 158 - at the end 175 160 - 2nd side - at the beginning 150 130 - at the end 160 130 Observations 1. improved runnability 2. lower high shear viscosity (lower rod pressure) 3. better dynamic water retention (no increase of rod pressure) 4. less misting with sample F 5. It would have been possible to increase solids content of coating color WO 2004/076743 PCT/EP2004/001426 18 Associative thickener composition Sample F provides low high shear viscosity which gives lower rod pressure and better water retention gives more stable rod pressure. 5 Example 8 Thickener composition sample F and various other thickener compositions were used in coating formulations to coat paper in a pre coating pilot trial. 10 Base paper Uncoated, 52 g/m2 (base paper for 90 g/m2 grade) Pre-coating: Recipe: 100 parts NPS CaC03 (Covercarb 60-LV) 8 parts SB-latex (DL 920) 15 4 parts Starch (302 ESP) 0.6 parts FWA (Tinopal ABP-Z) * Pre-coating conditions: pH: ca. 8.5 Solids: 62% 20 Brookfield: 800 - 900 mPas Temperature: 29-31 C Method: Sym-sizer (double side) Speed: 1500m/min Coat weight: 9 g/m2/side 25 Rod diameter 20 mm Moisture: 3.5% The results are shown in Table 8 WO 2004/076743 PCT/EP2004/001426 19 Table 8 Thickener Amount, parts Solids, % Start / End pH Brookfield (100 rpm) mPas Start/End Water retention g/m2 High shear viscosity 1 M 1/s mPas Rod pressure bar Start / End CMC 0.2 61.9/62.0 8.4 480 / 470 162 39 1.3/1.3 Commercial ASE 0.1 61.9/62.0 8.5 370/395 123 41 1.45/1.5 Commercial ASE 0.2 61.9/62.1 8.6 545 / 560 103 48 2.4/2.5 Sample F 0.2 62.1 / 62.2 8.4 430/470 108 39 1.3/1.3 The results show that the thickener according to the present invention exhibits the best combination of low high shear viscosity and water retention over CMC 5 or commercial ASE thickener. It can be seen that the CMC gave low high shear viscosity but poor water retention. The dose of commercial ASE thickener that provides low high shear viscosity gives poor water retention whereas a dose and of the same thickener and that provides good water retention exhibits poor high shear viscosity. Furthermore, the coating composition made using the 10 thickener of the present invention provided better runability and no or low misting. WO 2004/076743 PCT/EP2004/001426 20 Example 9 Thickener composition sample F and various other thickener compositions were used in coating formulations to coat paper in a top coating pilot trial. Base paper Pre-coated, 52 g/m2 (pre-coated paper for 65 g/m2 grade) Recipe: 10 15 20 70 parts fine CaC03 (Covercarb 85) 30 parts fine Clay (Hydragioss 90) 11 parts SB-latex (XZ 96445) 0.6 parts PVA (Airvol 103) 0.6 parts Ca-stearate (Raisacote CAS 50) 0.2 parts hardener (Bacote 20) 0.6 parts FWA (Tinopai ABP-Z) Coating conditions: pH: Solids: Brookfield: Temperature: Method: Speed: Coat weight Blade width: Moisture: ca. 8.5 63% 1200 -1500 mPas 27 - 28 C Opticoat-jet 1500 m/min 9 g/m2/side 0.457 mm 5.0% 25 The results are shown in Table 9. WO 2004/076743 PCT/EP2004/001426 21 Table 9 Thickener Amount, parts Solids, % Start/ End PH Brookfield (100 rpm) mPas Start / End Water retention g/m2 High shear viscosity 1 M 1/s mPas Blade pressure bar Start/End CMC 0.6 63.0/62.8 8.2 1180/1220 122 44 *0.99/0.99 **1.07 /1.03 commercial ASE 0.2 63.0 / 62.8 8.2 680/650 118 44 *0.93/0.95 **0.99/0.97 commercial ASE 0.3 63.2 / 63.0 8.2 985 / 940 111 47 *1.01/1.03 **1.10 /1.08 Sample F 0.3 63.0162.6 8.3 750 / 690 110 39 *0.95/0.94 **0.96 / 0.95 * = first side ** = second side This shows that the associative thickener of the present invention provided the best combination of low high shear viscosity and good water retention. 22 </div>

Claims

<div class="application article clearfix printTableText" id="claims"> Claims

1. A paper coating composition which includes a thickener composition for modifying the rheology of paper coatings, the thickener composition comprising 5 an associative thickener, wherein the associative monomer content of the thickener is below 10%, the molecular weight of the thickener is below about 1 million and the acid content is at least 10% by weight.

2. A paper coating composition as claimed in claim 1, wherein the associative 10 thickener is a hydrophobic alkali-soluble emulsion.

3. A paper coating composition as claimed in claim 1 or claim 2, wherein the thickener has a molecular weight of from 10,000 to 700,000. 15

4. A paper coating composition as claimed in claim 1 or claim 2, wherein the thickener has a molecular weight of from 70,000 to 150,000.

5. A paper coating composition as claimed in claim 1 or claim 2, wherein the thickener has a molecular weight of from 70,000 to below 100,000. 20

6. A paper coating composition as claimed in any one of the preceding claims, wherein the acid functionality is provided by an acid selected from methacrylic acid, acrylic acid and mixtures thereof. 25

7. A paper coating composition as claimed in any one of the preceding claims, wherein the thickener is branched or cross linked.

8. A paper coating composition as claimed in any one of the preceding claims, wherein the associative content is below 5.0%. 30

9. A paper coating composition as claimed in any one of the preceding claims, wherein the associative content is below 2.5%. 1 INTELLECTUAL PROPERTY OFFICE OF N.Z. - 1 NOV 2007 23

10. A paper coating composition as claimed in any one of the preceding claims, wherein the pH is from 8 to 10. 5

11. A paper coating composition as claimed in any one of the preceding claims, for roll and blade coating, wherein the amount of thickener composition present is chosen to achieve a Brookfield viscosity (100 rpm) of the order of 1000 to 1400 mPas. 10

12. A paper coating composition as claimed in any one of the preceding claims, for coating by film press, wherein the amount of thickener composition present is chosen to achieve a Brookfield viscosity (100 rpm) of the order of 700 to 1000 mPas. 15

13. A paper coating composition as claimed in any one of the preceding claims, for coating by jet applicator wherein the amount of thickener composition present is chosen to achieve a Brookfield viscosity (100rpm) of the order of 2000 to 2500 mPas. 20

14. A paper coating composition as claimed in any one of the preceding claims, wherein the thickener composition is the sole thickener ingredient.

15. A method of modifying the rheology of a paper coating composition comprising adding a thickener composition for modifying the rheology of paper 25 coatings, the thickener composition comprising an associative thickener, wherein the associative monomer content of the thickener is below 10%, the weight of the thickener is below 1 million and the acid content is at least 10% by weight. 30 16. A method as claimed in claim 15, wherein the pH is adjusted to between 8 and 10.

INTELLECTUAL PROPERTY OFFICE OF N.Z. - 1 NOV 2007 pcrcu/t-D 24

17. A method as claimed in claim 15 or claim 16, wherein the thickener composition is added to the paper coating composition in an amount to achieve a Brookfield viscosity (100 rpm) of the order of 1000 to 1400 mPas. 5

18. A method as claimed in claim 15 or claim 16, wherein the thickener composition is added to the paper coating composition in an amount to achieve a Brookfield viscosity (100rpm) of the order of 700 to 1000 mPas.

19. A method as claimed in claim 15 or claim 16, wherein the thickener 10 composition is added to the paper coating composition in an amount to achieve a Brookfield viscosity (100 rpm) of the order of 2000 to 2500 mPas.

20. A method as claimed in any one of claims 15 to 19, wherein the thickener composition of claims 1 to 6 is the sole thickener ingredient. 15

21. A method of coating a sheet of paper comprising applying to the surface of the sheet a coating composition as defined by any one of claims 1 to 14.

22. A paper coating as claimed in any one of claims 1 to 14, substantially as 20 herein described with reference to any one of the Examples and/or the Figure.

23. A method as claimed in any one of claims 15 to 21, substantially as herein described with reference to any one of the Examples and/or the Figure. 25

24. A coated sheet of paper obtained by the method of any one of claims 15 to 21.

25. A coated sheet of paper obtained by applying to the surface of a sheet of paper the coating composition as defined in any one of claims 1 to 14. INTELLECTUAL PROPERTY OFFICE OF N.2. -1 NOV 2007 £2 c" ^ r~" m f ^ </div>