METHOD FOR PRETREATMENT OF FILLER, MODIFIED FILLER WITH A HYDROPHOBIC POLYMER AND USE OF THE HYDROPHOBIC POLYMER

Abstract: A modified filler used in the making of paper or the like, preparation of the filler and its use. The modified filler comprises a filler known as such, e.g. calcium carbonate, kaolin, talc, titanium dioxide, sodium silicate and aluminiumtrihydrate or their mixture, and a hydrophobic polymer made of polymerisable monomers, which is added to the filler as a polymer dispersion or a polymer solution.

Description: METHOD FOR PRETREATMENT OF FILLER, MODIFIED FILLER WITH A HYDROPHOBIC POLYMER AND USE OF THE HYDROPHOBIC POLYMER The present invention relates to a method defined by the preambles of the independent claims presented below for pretreatment of a filler used in the making of paper, board or the like, to a modified filler and to its use. Fillers used in the making of paper and board are for instance calcium carbonate, such as precipitated calcium carbonate (PCC), kaolin, such as calcinated kaolin, talc, titanium dioxide, sodium silicate and aluminiumtrihydrate. Also mixtures of the above mentioned minerals can be used as fillers. An object of paper makers, particularly makers of fine paper, is ever more to increase the filler content of paper due to cost reasons. However, due to a highly in- creased filler content the paper loses in strength, stiffness and other mechanical characteristics. A high filler content also increases the linting of paper. As a high filler content for instance an amount can be considered, which calculated as dry matter comprises > 20 % of the amount of the fibre suspension. An addition of a binding agent can affect the above-mentioned characteristics. An addition of bind- ing agent can i.a. increase the strength of the finished paper. Among other materials starch has been conventionally used as a binding agent. Starch is a hydrophilic material, which added in large amounts assists water to penetrate into the paper web. Thus the use of starch has also negative effects, particularly on the wet strength of the paper. The use of starch can also have disadvantageous effects in the post-treatment of the paper, and for instance during printing it can cause too strong an absorption of the printing ink into the paper. Also other liquids, such as surface sizing agents and coatings may be absorbed in a non-desired manner into the paper. Other hydrophilic binding agents, such as hydrophilic synthetic polymers, may cause the same problems as starch. The object of the present invention is to provide an improved method for pretreatment of filler used in the making of paper, board or the like, a modified filler and its use. Then the object is to provide such a method and an additive for the pretreatment of a filler which enables also large additions of the filler without the great disadvantages caused by the absorption of water mentioned above. In order to attain the above-mentioned objects the method and the filler according to the invention are characterised in what is defined in the characterising parts of the independent claims presented below. A typical method according to the invention for pretreatment of filler used in the making of paper, board or the like comprises the addition of a hydrophobic polymer made of polymerisable monomers to the filler in order to create a hydrophobic film on the surface of the filler particles and/or between adjacent filler particles. The filler is pretreated with the hydrophobic polymer so that it makes it more difficult for water to penetrate into the filler layer. Thus, the pretreatment of the filler can improve the wet strength and reduce the linting of the paper, board or the like to be made. The addition of a hydrophobic polymer to the filler means in this description the combination of the polymer and the filler with each other. The combination can be made by mixing the polymer to the filler or by mixing the filler to the polymer. The combination can also be made so, that both materials are supplied simultaneously to the fibre suspension at the same dispensing point, so that the mixing occurs in the dispensing conduit immediately before reaching the fibre suspension. The mixing occurs at a high shear force. The advantages of the invention are manifested particularly when a hydrophobic polymer is added to the filler in papermaking using high amounts of filler, over 20 %, typically more than 25 % of the dry solids content of the paper. In the solu- tion according to the invention the hydrophobic polymer added to the filler is mainly a polymer which does not have to react covalently with the filler or with the cellulose fibre in order to create a barrier which restricts the penetration of water or increases retention. In the solution according to the invention the hydrophobic polymer forms a film-like barrier around the filler particles and between them. Pre- viously reactive sizes where the effect restricting the penetration of water is created only when the sizes react with the fibres have been used in the papermaking. These sizes are not film creating polymers, whereby they do not create a film on the filler surface, and thus they do not reduce paper linting. Further, when they react with the fibre they prevent the creating of bonds between the fibres, and thus they have a negative effect on the paper strength properties. The polymer added to the filler is typically a polymer which is created by solution or emulsion polymerisation with polymerisable monomers, and which has a molecular weight > 5000, typically > 10,000. In special cases the polymer can also contain a minor portion of smaller polymer molecules. The polymer is added to the filler as a polymer dispersion or a polymer solution, which is polymerised using as a stabilising agent polysaccharide, such as starch, mannan and/or CMC. In addition it is possible to use as the stabilising agent a syn- thetic polymer, such as polyaminoamide or another polyaminopolymer, and/or a suitable dispersing agent, and/or anionic and/or cationic polymerisable monomers. According to a preferred embodiment of the invention the polymer can be added to the filler as a polymer dispersion which is formed by copolymerising a monomer mixture of a polysaccharide dissolved in water, the monomer mixture containing at least one vinylic monomer. The temperature at which the polymer made by co- polymerisation generates a film is about -50 to 200 °C, typically 0 to 100 °C, most typically 0 to 70 °C. Regarding the prevention of linting a temperature of 10 to 50 °C is preferred. In this case a dense film is formed on the surface of the filler particles. However, the selected temperature depends on the temperature conditions in the paper machine. The polysaccharide used to prepare the polymer, for instance starch, is chemically modified by cationic and or anionic groups, whereby the substitution level (OS) regarding the cationic and/or anionic substituents is typically 0.1 to 2, most typically 0.1 to 1. According to another preferred embodiment of the invention the polymer can be added to the filler as a stable product which is formed by mixing starch in granule form into a synthetic polymer, such as styrene maleic anhydrate (SMA), styrene maleic imide (SMI) or the like, and by letting the starch react with the polymer under the influence of heat. According to an advantageous embodiment of the invention the polymer can be added to the filler as a polymer dispersion which comprises the following components, whose amounts are presented as dry solids content, a) 5 to 50 %, advantageously 5 to 40 % starch having a substitution level (DS) regarding cationic and/or anionic substituents of about 0.01 to 1, typically 0.04 to 1.0, and an intrinsic viscosity of > 1.0 dl/g in the cationised and/or anionised state, typically 1.5 to 15 dl/g; b) 50 to 95 %, advantageously 60 to 95 % of a monomer mixture containing at least one vinylic monomer, and c) water. The most typically used monomers in the preparation are for instance styrene, 1,3- butadiene, butylacrylate, metyl methacrylate, ethyl acrylate, 2-ethyl hexyl acrylate, acrylonitrile, acrylamide, methacrylamide and vinyl acetate. Also cationic and/or anionic monomers can be used in the preparation, such as acrylic acid, methacrylic acid and chloride of trimethyl ammonium propylmethacrylamide. The temperature at which the polymer which is formed by a monomer mixture will generate a film is typically 10 to 50 °C, advantageously 20 to 50 °C. The monomer mixture used in the preparation of the polymer dispersion can comprise e.g. about 40 to 70 % acrylates and about 30 to 60 % styrene, whereby the monomer mixture can comprise of, for instance, the following components: a) acrylonitrile, 0 to 19 %, typically 5 to 19 %, most typically about 19 %; b) acrylates, 10 to 60 %, typically 20 to 50 %, most typically about 30 %, and c) styrene, 10 to 60 %, typically 20 to 40 %, most typically about 30 %. As an answer to the problems regarding wet strength and linting in papermaking the solution according to the invention thus proposes the use of an additive containing a hydrophobic polymer for pretreatment of the filler. In this case the additive is typically a hydrophobic polymer made of polymerisable monomers, which is added to the filler as a polymer dispersion or as a polymer solution in order to create a hydrophobic film on the surface of the filler particles and thus to improve the characteristics of the paper or the like to be manufactured, such as to increase wet strength and to reduce linting. The polymer is made of a monomer mixture containing at least one vinylic monomer. According to a preferred embodiment of the invention the polymer is made of a monomer mixture containing at least acrylates and styrene. The monomer mixture comprises e.g. A) acrylonitrile or methacrylonitrile or a mixture of them; b) acrylates; and c) styrene or other copolymerable monomers unsubstituted by ethylene. The invention is illustrated with the aid of the enclosed examples of embodiments. Example 1 Paper (80 g/m 2 ) was prepared in a sheet mould where the fibres were oriented with the aid of flow. In the preparation a cellulose mixture of birch and pine was used in proportion 70/30 beaten to about 35 °SR. The temperature of the fibre suspension was 45 °C. In addition precipitated calcium carbonate (PCC) was used as filler, at a level of 25 % of the total pulp composition. To the fibre suspension 1 % pulp starch with a cationic degree DS of 0.035 was also added. As retention agents, which were dispensed after the filler addition, 0.05 % Percol 162 and 0.15 % Hydrocol O were used. The results are shown in Table 1 below. Table 1 - In test points 1 and 2 alkylketene dimer dispersion (AKD) was mixed to the filler material before adding it to the fibre suspension. - In test point 3 the AKD was added to the fibre suspension, and the filler without AKD addition was added. - In test points 4 to 9 the AKD was added to the fibre suspension in a similar manner as in point 3, using the standard amount 0.25 %, and the other chemicals were admixed to the filler material before adding to the fibre suspension. The chemical dosage was calculated to correspond to a certain percentage of active chemical of the paper's dry solids content. - In test points 4 and 5 starch was used, which had been used to stabilise the AKD dispersion, in order to illustrate the effect of starch in the test points 1 to 3. - In test points 6 and 7 ammonium salt of styrene maleic acid was added to the filler material, whereby the salt had been treated at an active material ratio 1:1 with the same starch which was used in the test points 4 and 5. - In test points 8 and 9 styrene acrylate acrylonitrile copolymer, the preparation of which is disclosed in more detail in the patent application PCT/FIl 00/00084, example 4. The strength of the wet paper was determined from humid paper (dry solids content 45 %) before drying. In the example 1 it can be seen that AKD improves the hydrophobicity of the paper, but impairs the paper's strength characteristics. The strength of the dry paper is obtained with the starch used in dispersing the AKD. However, the starch reduces the wet strength of the paper. Both SMA and styrene acrylate substantially improve the strength properties of wet paper and have an improving effect also on the dry strength and on the hydrophobicity of the paper. Example 2 Paper (80 g/m 2 ) was made in a test paper machine having a web width of 70 cm and the speed 80 m/min. In the making a cellulose mixture of birch and pine in propor- tions 70/30 beaten to about 28 °SR was used. In addition precipitated calcium carbonate (PCC) was used as filler, at a level of 25 % of the total pulp composition. To the fibre suspension 0.9 % pulp starch with a cationic degree DS of 0.045 and 0.2 % of AKD dispersion was also added, the dosage determined according to the AKD concentration. As retention agents, which were dispensed after the filler addi- tion, we used 0.03 % Percol 162 and 0.15 % Hydrocol O. In this example the styrene acrylate acrylonitrile copolymer mentioned in example 1 was used as a variable, which was either dispensed to the fibre suspension before the filler, or mixed to the filler. The dispensed amount was in both test points the same, 0.6 % of the paper's dry solids content. The tensile strength of wet paper was determined from paper which had been immersed in water so long that a paper's dry solids content of 45 % was obtained. The results are presented in Table 2 below. Table 2 In the table it can clearly be seen that the addition of the hydrophobic polymer pro- vides a better wet strength value and linting value, when the addition is made to the filler instead of to the fibre suspension. In the table it can be seen that the paper linting is much lower when the hydrophobic polymer is dispersed to the fibre suspension after it has been admixed to the filler, compared to a situation where the polymer would have been dispersed directly to the fibre suspension. The dispersion to the filler also had an impact on the paper's strength and hydrophobicity. The method according to this invention, where the filler is pretreated or modified by a hydrophobic material which creates a film, increases the hydrophobicity of the paper or the like, and at the same time it improves the strength characteristics of both dry and wet paper. Further as advantages of the solution according to the invention can be mentioned, that the method is able to reduce the paper linting. The invention is not intended to be limited to the exemplary embodiments presented above, but the intention is to be able to implement the invention widely within the scope defined by the enclosed claims.

Claims: Claims 1. A method for pretreatment of filler, such as calcium carbonate, kaolin, talc, titanium dioxide, sodium silicate and aluminiumtrihydrate or their mixture, used in the making of paper, board or the like, the pretreatment being conducted before the filler is supplied to the fibre suspension, characterised in that - the pretreatment comprises the addition of a hydrophobic polymer made of polymerisable monomers to the filler in order to create a hydrophobic film on the surface of the filler particles and or between adjacent filler particles, and that - the polymer added to the filler is added as a polymer dispersion or a polymer solu- tion, which is polymerised using polysaccharide, such as starch, mannan and/or CMC as a stabilising agent, in order to improve the characteristics of the paper, board or the like to be made, such as to increase the wet strength and/or reduce the linting. 2. A method according to claim 1, characterised in that the polymer added to the filler is a polymer, which is made by solution polymerisation or emulsion polymerisation of polymerisable monomers. 3. A method according to claim 1, characterised in that the polymer added to the filler is- mainly an inert polymer, which does not react covalently with the filler or with the cellulose fibre. 4. A method according to claim 1, characterised in that the polymer added to the filler has a molecular weight, which is mainly over 5,000, typically over 10,000. 5. A method according to claim 1, characterised in that the polymer added to the filler is added as a polymer dispersion or a polymer solution, which is polymerised using further as a stabilising agent, - a synthetic polymer, such as polyaminoamide or other polyaminopolymer, and/or some other suitable dispersing agent, and/or - anionic and/or cationic polymerisable monomers. 6. A method according to claim 1, characterised in that the polymer is added to the filler as a stable product which is formed by mixing starch in granule form into a synthetic polymer, such as styrene maleic anhydrate (SMA), styrene maleic imide (SMI) or the like, and by letting the starch react with the polymer under the influence of heat. 7. A method according to claim 1, characterised in that the polymer to be added to the filler is added as a polymer dispersion which is formed by copolymerising a monomer mixture of a polysaccharide dissolved in water, the monomer mixture containing at least one vinylic monomer. 8. A method according to claim 7, characterised in that the polysaccharide is chemically modified by cationic and/or anionic groups, whereby the substitution level (DS) regarding the cationic and/or anionic substituents is typically 0.1 to 2, most typically 0.1 to 1. 9. A method according to claim 7, characterised in that the temperature at which the polymer made by copolymerisation creates a film is about -50 to 200 °C, typically 0 to 100 °C, more typically 0 to 70 °C, most typically 0 to 50 °C. 10. A method according to claim 1, characterised in that the polymer to be added to the filler is added as a polymer dispersion which is comprised of the following components, whose amounts are presented as dry solids content, a) 5 to 50 %, advantageously 5 to 40 % starch having a substitution level (DS) regarding cationic and/or anionic substituents of about 0.01 to 1, typically 0.04 to 1.0, and an intrinsic viscosity of > 1.0 dl/g in a cationised and/or anionised state, typi- cally l .5 to l5 dl g; b) 50 to 95 %, advantageously 60 to 95 % of a monomer mixture containing at least one vinylic monomer, and c) water. 11. A method according to claim 10, characterised in that the film generating temperature of the polymer which is formed by said monomer mixture is typically 10 to 50 °C, advantageously 20 to 50 °C. 12. A method according to claim 10, characterised in that the monomer mixture comprises 40 to 70 % acrylates and 30 to 60 % styrene. 13. A method according to claim 10, characterised in that the monomer mixture comprises a) acrylonitrile, 0 to 19 %, typically 5 to 19 %, most typically about 19 %; b) acrylates, 10 to 60 %, typically 20 to 50 %, most typically about 30 %, and c) styrene, 10 to 60 %, typically 20 to 40 %, most typically about 30 %. 14. A method according to claim 1, characterised in that a hydrophobic polymer is added to the filler in the making of paper, which uses large amounts of filler, the amounts being > 20 %, typically > 25 %, of the dry solids content of the paper. 15. A modified filler to be used in the making of paper, board or the like, characterised in that the modified filler comprises - a filler known as such, e.g. calcium carbonate, kaolin, talc, titanium dioxide, sodium silicate and aluminiumtrihydrate, and - a hydrophobic polymer made of polymerisable monomers, which is added to the filler as a polymer dispersion or a polymer solution, which is polymerised using polysaccharide, such as starch, mannan and/or CMC as the stabilising agent, in order to create a hydrophobic film on the surface of the filler particles and/or between adjacent filler particles. 16. A modified filler according to claim 15, characterised in that the polymer is an inert polymer having a molecular weight, which is over 5,000, preferably > 10,000. 17. A modified filler according to claim 15, characterised in that the polymer is formed from a monomer mixture containing at least one vinylic monomer. 18. A modified filler according to claim 15, characterised in that the polymer is formed from a monomer mixture containing a) acrylonitrile or methacrylonitrile or a mixture thereof, b) acrylates, c) styrene or other copolymerisable monomers unsubstitued by ethylene. 19. A modified filler according to claim 15, characterised in that the polymer is formed from a monomer mixture containing a) 0 to 19 %, preferably 5 to 19 %, most preferably about 19 % of acrylonitrile; b) 10 to 60 %, preferably 20 to 50 %, most preferably about 30 % acrylates, and c) 10 to 60 %, preferably 20 to 40 %, most preferably about 30 % styrene, 20. A modified filler according to claim 15, characterised in that the polymer dispersion is comprised of the following components, whose amounts are presented as dry solids content, a) 5 to 50 %, advantageously 5 to 40 % starch having a substitution level (DS) regarding cationic and/or anionic substituents of about 0.01 to 1, typically 0.04 to 1.0, and an intrinsic viscosity of > 1.0 dl/g in a cationised and/or anionised state, typi- cally l.5 to l5 dl/g; b) 50 to 95 %, advantageously 60 to 95 % of a monomer mixture containing at least one vinylic monomer, and c) water. 21. The use of a hydrophobic polymer made of polymerisable monomers for modifying a filler, such as calcium carbonate, kaolin, talc, titanium dioxide, sodium silicate and aluminiumtrihydrate or their mixture, used in the making of paper, board or the like, characterised in that the polymer is added to the filler as a polymer dispersion or a polymer solution, which is polymerised using polysaccharide, such as starch, mannan and/or CMC as a stabilising agent, before the filler is supplied to the fibre suspension. 22. The use according to claim 21, characterised in that the polymer is formed from a monomer mixture containing at least one vinylic monomer. 23. The use according to claim 21, characterised in that the polymer is added as a polymer dispersion formed from the following components, whose amounts are pre- sented as dry solids content, a) 5 to 50 %, advantageously 5 to 40 % starch having a substitution level (DS) regarding cationic and or anionic substituents of about 0.01 to 1, typically 0.04 to 1.0, and an intrinsic viscosity of > 1.0 dl/g in a cationised and/or anionised state, typically 1.5 to 15 dl/g; b) 50 to 95 %, advantageously 60 to 95 % of a monomer mixture containing at least one vinylic monomer, and c) water. 24. The use according to claim 23, characterised in that the monomer mixture comprises 40 to 70 % acrylates and 30 to 60 % styrene.

Inventors: MALMSTROEM OLOF, NIINIKOSKI MARI, NURMINEN MARKKU, SUNDBERG KENNETH, ZETTER CLAES, MALMSTROEM, OLOF, NIINIKOSKI, MARI, NURMINEN, MARKKU, SUNDBERG, KENNETH, ZETTER, CLAES
Applicants: MALMSTROEM OLOF, NIINIKOSKI MARI, NURMINEN MARKKU, RAISIO CHEM LTD, SUNDBERG KENNETH, ZETTER CLAES, MALMSTROEM, OLOF, NIINIKOSKI, MARI, NURMINEN, MARKKU, RAISIO CHEMICALS LTD, SUNDBERG, KENNETH, ZETTER, CLAES
Application year: 2001
Main classification: D21H17
IPC codes: C09C1, C09C3, D21H17, D21H21