PROCESS FOR PREPARING SELF-LINING PIGMENT PARTICLES

专利摘要:
process for preparing self-bonding pigment particles, suspension of self-bonding pigment particles, use of a suspension of self-bonding pigment particles, and, paper product the present invention relates to a process for preparing self-bonding pigment particles from a suspension aqueous solution of a material containing calcium carbonate, in which an anionic binder and at least one cationic polymer are mixed with the suspension.
公开号:BR112014028076B1
申请号:R112014028076-2
申请日:2013-04-29
公开日:2021-03-23
发明作者:Patrick A. C. Gane；Joachim Schölkopf；Lars Andersson；Daniel Gantenbein；Maximilian Laufmann
申请人:Omya International Ag；
IPC主号:

专利说明:

[0001] [0001] The invention relates to a process for preparing suspensions of self-bonding pigment particles, to a suspension of self-bonding pigment particles, as well as to a paper product comprising self-bonding pigment particles and the use of the suspension of pigment particles. self-bonding pigment.
[0002] [0002] Mineral materials and binders are among the main constituents used in the manufacture of numerous products such as paints, paper and plastic materials. In them, mineral materials such as calcium carbonate and other particulate materials contribute to mechanical and optical properties, while the binder, usually based on latex and in the form of aqueous suspensions or dispersions, provides the necessary adhesion and cohesion for the respective constituents. of the final product to be produced.
[0003] [0003] In order to avoid the logistical difficulties of handling mineral and binder materials separately, and also to avoid the undesirable physical and chemical interactions developed in comparable mixtures of mineral and binder materials, the self-bonding pigment particles have been developed and are known in the industry. In this regard, self-bonding pigment particles having both the properties of the mineral material and the binder can be implemented directly in a variety of applications. This unique product, called self-bonding pigment particles, refers to the distinct solid particles, formed from mineral and binder material that are closely linked to each other. The internal cohesive forces are such that they provide self-bonding pigment particles with excellent mechanical stability.
[0004] [0004] The self-bonding pigment particles are prepared by a process implementing at least one step of grinding mineral materials in the presence of binder, where grinding refers to an operation leading to a reduction in particle size; the mineral materials in the self-bonding pigment particles have a smaller diameter than the initial mineral material used to produce the same. Such self-bonding pigment particles are described in several documents, including WO 2006/008657, WO 2006/128814, and WO 2008/139292.
[0005] [0005] In addition, the Applicant would like to mention the following applications on his behalf, which also refer to the processes for preparing self-bonding pigment particles: unpublished European patent applications with filing numbers 11 160900.4, 11 160926.9 , 11 179604.1, and 11 179572.0.
[0006] [0006] Self-bonding pigment particles containing polymer-based binders that are derived from natural or renewable resources are a particular point of interest for environmental reasons. However, such self-bonding pigment particles are often formed from negatively charged modified polysaccharides, which may be unfavorable for some fields of application. For example, due to their negative surface charge, such pigment particles are difficult to retain during papermaking processes. This leads to a high consumption of self-bonding pigment particles and additional retention aid during paper production in order to obtain the desired filler load on the paper.
[0007] [0007] Another problem with paper production processes is that the load levels on the paper are limited due to the loss of strength of the paper as the load levels increase. One reason for this is that the reduced number of fibers in the paper sheet reduces the number of fiber bonds in the sheet and the presence of the load reduces the contact area between the remaining fibers. As a result, the retention of high amounts of charge produces a weaker sheet that can break more easily on paper machines, sizing presses, coaters, winders, printing presses, printing machines, or copying machines.
[0008] [0008] However, high loading levels on paper are desirable since they could provide the possibility to reduce the amount of wood fibers in the paper. In addition, papers with a high load content will dry faster and, as a result, the papermaking machine can run faster. Consequently, the addition of high loading levels can reduce paper production costs and save natural resources.
[0009] [0009] US 5,611,890 refers to a soft, strong loaded tissue paper, comprising a particulate non-cellulosic filler, wherein said filler comprises from 5 to 50% by weight of said tissue paper. WO 03/087472 describes a filler treatment comprising the preparation of swollen latex-starch compositions, and the addition of said compositions to a filler suspension. The use of these treated loads during papermaking improves the retention of the load and produces loaded papers, where the addition of the load has only a minimal negative effect on the strength properties. A papermaking filler that has been treated on the surface with a cationic polymer is described in CA 2,037,525. The article “Improvement of paper properties using starch-modified precipitated calcium carbonate filler” by Zhao et al., TAPPI Journal 2005, vol. 4 (2), refers to the commercial precipitated calcium carbonate fillers that have been modified with crude corn and potato starches. These modified fillers were used as fillers for papermaking to improve strength in high filler papers.
[0010] [0010] In view of the above, improving the production process of self-bonding pigment particles remains of interest to those skilled in the art.
[0011] [0011] Consequently, it is an object of the present invention to provide a process for obtaining self-bonding pigment particles, which avoids the aforementioned disadvantages. In particular, it is desirable to provide a process for obtaining self-bonding pigment particles, which allows the supply of a filler material that shows good retention in papermaking processes, and avoids the use of large quantities of retention aids. . It is also desirable that the self-bonding pigment particles obtained can be incorporated into paper in large quantities and, thus, allow the production of high load content paper, without deteriorating the mechanical or optical properties of the paper. It should also be desirable to provide a process for making self-bonding pigment particles obtained having the ability to improve the mechanical properties of paper when used as filler in paper applications, especially when used in the production of high-load papers.
[0012] [0012] The above and other objectives are resolved by the matter as defined here in the independent claims.
[0013] a) prover uma suspensão compreendendo, pelo menos, um material contendo carbonato de cálcio, b) prover um aglutinante polimérico aniônico, em que referido aglutinante compreende pelo menos um polissacarídeo modificado, c) prover pelo menos um polímero catiônico, d) misturar a suspensão de etapa a) e o aglutinante de etapa b), e e) triturar a suspensão misturada de etapa d), em que o pelo menos um polímero catiônico de etapa c) (i) é misturado na etapa d) com a suspensão de etapa a) e o aglutinante de etapa b), e/ou (ii) é misturado com a suspensão obtida após a etapa e) de trituração, e a mistura obtida é desaglomerada. [0013] In accordance with an aspect of the present invention, a process is provided for the self-bonding pigment particles, the process comprising the following steps: a) provide a suspension comprising at least one material containing calcium carbonate, b) providing an anionic polymeric binder, wherein said binder comprises at least one modified polysaccharide, c) provide at least one cationic polymer, d) mixing the suspension of step a) and the binder of step b), and e) crush the mixed suspension of step d), wherein the at least one cationic polymer of step c) (i) is mixed in step d) with the suspension from step a) and the binder from step b), and / or (ii) it is mixed with the suspension obtained after step e) of grinding, and the mixture obtained is de-agglomerated.
[0014] [0014] According to another aspect of the present invention, a suspension of self-ligating pigment particles is provided, which can be obtained by the process of the present invention.
[0015] [0015] In accordance with yet another aspect of the present invention, the use of the suspension of self-ligating pigment particles invented in paper, plastics, paint, coatings, concrete and / or applications in agriculture is provided.
[0016] [0016] In accordance with yet another aspect of the present invention, a paper product is provided comprising self-bonding pigment particles, wherein the pigment particles comprise particles of material containing calcium carbonate which are at least partially coated with a polymeric binder anionic compound comprising at least one modified polysaccharide and at least one cationic polymer.
[0017] [0017] Advantageous embodiments of the present invention are defined in the corresponding subclaims.
[0018] [0018] According to an embodiment, in step d) of the inventive process, the suspension of step a) is, in a first step, mixed with the binder of step b), and then, in a second step, it is mixed with at least one cationic polymer from step c). According to another embodiment, in the first step a suspension of step a) is mixed with a first part of the binder from step b), the mixture obtained is crushed and then mixed with the remaining part of the binder from step b) . According to yet another embodiment, in step d) of the inventive process, the binder from step b) is, in a first step, mixed with the cationic polymer from step c), and then, in a second step, it is mixed with the suspension of step a). According to yet another embodiment, in step d), the suspension of step a) is mixed with the binder from step b) and the cationic polymer from step c) in one step.
[0019] [0019] According to one embodiment, the cationic polymer is added in an amount so that the charge density of the self-bonding pigment particles obtained is lower compared to the self-bonding pigment particles not containing the cationic polymer, preferably the cationic polymer is added in an amount such that the charge density of the self-bonding pigment particles obtained is between -100 and -5 µEq / g, preferably between -80 and -10 µEq / g, and more preferably between -70 and -15 µEq / g.
[0020] [0020] According to one embodiment, at least one material containing calcium carbonate is selected from calcium carbonate, minerals containing calcium carbonate, mixed calcium carbonate fillers, or mixtures thereof, preferably the at least one material containing calcium carbonate is calcium carbonate, and more preferably crushed calcium carbonate. According to another embodiment, the at least one material containing calcium carbonate is provided in the form of particles having a median particle diameter d50 value by weight of 0.1 to 100 µm, preferably 0.1 to 80 µm , more preferably from 0.5 to 50 µm, and most preferably from 5.0 to 25 µm. According to yet another embodiment, the at least one material containing calcium carbonate is provided in the form of particles having a specific surface area of 0.1 to 200 m2 / g, preferably 1 to 25 m2 / g, more preferably from 2 to 15 m2 / g, and most preferably from 3 to 12 m2 / g.
[0021] [0021] According to an embodiment, the suspension of step a) has a solid content of at least 1% by weight, preferably from 1 to 90% by weight, more preferably from 5 to 85% by weight, still more preferably from 20 to 75% by weight, and most preferably from 45 to 65% by weight, based on the total weight of the suspension.
[0022] [0022] According to one embodiment, the at least one modified polysaccharide is a carboxymethyl derivative and / or carboxymethyl hydroxypropyl derivative and / or carboxymethyl hydroxyethyl derivative of a polysaccharide, preferably a carboxymethylcellulose, an anionic starch, a guar anionic, or mixtures thereof. According to another embodiment, the at least one modified polysaccharide has a degree of substitution of hydroxyl groups in the range of 0.4 to 2.0, 0.5 to 1.8, 0.6 to 1.6, or 0.7 to 1.5.
[0023] [0023] According to an embodiment, the binder of step b) is a carboxymethylcellulose, preferably having an intrinsic viscosity in the range of 5 to 500 ml / g, preferably of 10 to 400 ml / g, and more preferably of 20 at 350 ml / g. According to another embodiment, the binder of step b) is in the form of a solution or dry material, preferably in the form of a solution having a binder concentration of 1 to 70% by weight, preferably 2 to 30% by weight. weight, more preferably 3 to 15% by weight, and most preferably 4 to 10% by weight, based on the total weight of the solution. According to yet another embodiment, the binder from step b) is added in an amount of 0.001 to 20% by weight, preferably from 0.005 to 15% by weight, more preferably from 0.01 to 10% by weight, and most preferably 0.05 to 5% by weight, based on the total weight of the dry calcium carbonate containing material.
[0024] [0024] According to one embodiment, the at least one cationic polymer of step c) is selected from the group comprising polyamines, polyethyleneimines, polyacrylamides, cationic epichlorohydrin resins, polydialldimethylammonium chloride, cationic starch, cationic guar, and mixtures of the same. According to another embodiment, the at least one cationic polymer of step c) is in the form of a solution or dry material, preferably in the form of an aqueous solution having a concentration of 1 to 70% by weight, preferably of 2 to 55% by weight, more preferably from 5 to 50% by weight, and most preferably from 30 to 50% by weight, based on the total weight of the solution. According to yet another embodiment, the at least one cationic polymer of step c) is added in an amount of 0.001 to 20% by weight, preferably from 0.005 to 15% by weight, more preferably from 0.01 to 10% by weight, and most preferably from 0.05 to 5% by weight or from 0.5 to 2.5% by weight, based on the total weight of the material containing dry calcium carbonate.
[0025] [0025] According to an embodiment, the grinding step e) is carried out at a temperature of 5 to 110 ° C, from 10 to 100 ° C, from 15 to 80 ° C, or from 20 ° C to 25 ° C. According to another embodiment, the grinding step e) is carried out batchwise or continuously, preferably continuously. According to yet another embodiment, the process further comprises a step of concentrating the suspension obtained from self-bonding pigment particles. The concentration step can be carried out using thermal and / or mechanical methods well known to the person skilled in the art.
[0026] [0026] According to one embodiment, the suspension of self-bonding pigment particles is used in wet end processes of a papermaking machine, on cigarette paper, plate and / or coating applications, or as a support for rotogravure and / or offset and / or inkjet printing and / or continuous inkjet printing and / or flexography and / or electrography and / or decoration surfaces. According to another embodiment, the suspension of self-bonding pigment particles is used to reduce the exposure to sunlight and UV of plant leaves.
[0027] [0027] According to one embodiment, the paper product has a higher flexural stiffness, compared to a paper product, in which the self-bonding pigment particles are replaced by the same amount of particles of material containing calcium carbonate, preferably the flexural stiffness is at least 5% greater, preferably at least 7% greater, and more preferably at least 10% greater compared to the flexural stiffness of a paper product, in which the self-bonding pigment particles are replaced by the same amount of particles of material containing calcium carbonate.
[0028] [0028] It should be understood that for the purpose of the present invention, the following terms have the following meaning.
[0029] [0029] The term "anionic polymeric binder", as used in the present invention, is a polymer that is capable of bonding to the surface of the particles of the material containing calcium carbonate and to itself, and / or to certain other materials upon drying. The bond includes ionic interactions and / or hydrogen-hydrogen bridge bonds between the groups on the surface of the particles of material containing calcium carbonate and the functional groups of the polymer. In addition, the term "anionic polymer" or "anionic polymeric binder", according to the meaning of the present invention, refers to a polymer having a negative net charge. This compound is typically modified with anionic groups. The term “anionic” does not exclude the presence of cationic groups as long as the sum of individual charges is negative.
[0030] A "material containing calcium carbonate", in the meaning of the present invention, can be a mineral material or a synthetic material having a calcium carbonate content of at least 50% by weight, preferably 75% by weight, more preferably 90% by weight, and most preferably 95% by weight, based on the total weight of the calcium carbonate containing material. The term "material containing dry calcium carbonate" is understood to refer to particles of material containing calcium carbonate having a total surface moisture content of less than 0.5% by weight, preferably less than 0.2% by weight and more preferably less than 0.1% by weight, based on the total weight of the particles.
[0031] [0031] The term "cationic polymer", in the meaning of the present invention, refers to a polymer having a positive net charge. This compound is typically modified with cationic groups. The term "cationic" does not exclude the presence of anionic groups since the sum of individual charges is positive.
[0032] [0032] Throughout this document, the “degree of substitution” is specified with respect to the total number of groups substituted or modified per unit of unmodified monomer of the original polysaccharide.
[0033] [0033] The term "free polymer", in the meaning of the present invention, refers to the amount of polymer in the suspension, which is not bound in the particles of material containing calcium carbonate.
[0034] [0034] "Crushed calcium carbonate" (GCC), in the meaning of the present invention, is a calcium carbonate obtained from natural sources, such as limestone, marble, calcite or plaster, and processed through a wet treatment and / or dry as crushing, sifting and / or fractioning, for example, by a cyclone or classifier. The term "crushed dry calcium carbonate" is understood to refer to crushed calcium carbonate having a total surface moisture content of less than 0.5% by weight.
[0035] [0035] The term "intrinsic viscosity", as used in the context of the present invention, is a measure of the ability of a polymer in solution to improve the viscosity of the solution, being specified in ml / g.
[0036] [0036] "Modified calcium carbonate" (MCC), in the meaning of the present invention, can distinguish a natural crushed or precipitated calcium carbonate with a modification of internal structure or a surface reaction product.
[0037] [0037] The "modified polysaccharides", in the meaning of the present invention, are polysaccharides, in which at least part of the hydroxyl groups are carboxylated. In addition, the modified polysaccharides may contain other modifications such as aldehyde groups.
[0038] [0038] Throughout this document, the "particle size" of a calcium carbonate product is described by its particle size distribution. The dx value represents the relative diameter, for which x% by weight of the particles have smaller diameters than dx. This means that the value of d20 is the particle size in which 20% by weight of all particles are smaller, and the value of d75 is the particle size in which 75% by weight of all particles are smaller. The d50 value is thus the median particle size by weight, that is, 50% by weight of all grains are larger or smaller than this particle size. For the purpose of the present invention, the particle size is specified as the median particle size by weight d50, unless otherwise indicated. To determine the d50 value of the median particle size by weight, for particles having a d50 value between 0.2 and 5 µm, a Sedigraph 5100 or 5120 device from Micromeritics, USA can be used.
[0039] [0039] The "precipitated calcium carbonate" (PCC), in the meaning of the present invention, is a synthesized material, generally obtained by precipitation following a reaction of carbon dioxide and calcium hydroxide (hydrated lime) in an aqueous environment or by precipitation of a calcium and carbonate source in water. In addition, the precipitated calcium carbonate can also be the product of introducing calcium and carbonate salts, calcium chloride and sodium carbonate, for example, in an aqueous environment.
[0040] [0040] A "specific surface area (SSA)" of a mineral pigment, in the meaning of the present invention, is defined as the surface area of the mineral pigment divided by the mass of the mineral pigment. As used here, the specific surface area is measured by adsorption using the BET isotherm (ISO 9277: 2010), being specified in m2 / g.
[0041] [0041] A "suspension" or "slurry", in the meaning of the present invention, comprises insoluble solids and water, and optionally other additives and generally contains large amounts of solids and thus is more viscous and may have a higher density than the liquid from which it is formed.
[0042] [0042] For the purposes of the present invention, the term "viscosity" with reference to coating formulations, refers to Brookfiled viscosity. Brookfiled viscosity can be measured by a Brookfield viscometer at 23 ° C at 100 rpm, being specified in mPa ∙ s.
[0043] [0043] Where the term "comprising" is used in the present description and claims, it does not exclude other elements. For the purposes of the present invention, the term "consisting of" is considered to be a preferred embodiment of the term "comprising of". If a group is subsequently defined as comprising at least a number of embodiments, this should also be understood as describing a group, which preferably consists only of these embodiments.
[0044] [0044] Where a definite or indefinite article is used when referring to a singular noun, for example, "um", "uma" or "o", it includes the plural reference of this name, unless it is specifically described.
[0045] [0045] The terms such as "obtainable" or "definable" and "obtained" or "defined" are used interchangeably. This, for example, means that, unless the context clearly dictates otherwise, the term “obtained” does not mean that, for example, an embodiment must be obtained by, for example, the sequence of steps following the term “Obtained”, although this limited understanding is always included by the terms “obtained” or “defined” as a preferred embodiment.
[0046] [0046] The inventive process for preparing the self-bonding pigment particles comprises the steps of (a) providing a suspension comprising at least one material containing calcium carbonate, (b) providing an anionic polymeric binder, wherein said binder comprises at least minus a modified polysaccharide, (c) providing at least one cationic polymer, (d) mixing the step suspension (a) and the step binder (b), and (e) grinding the mixed step suspension (d), in that the at least one cationic polymer from step c) (i) is mixed in step d) with the suspension from step a) and the binder from step b), and / or (ii) is mixed with the suspension obtained after step e) crushing, and the mixture obtained is de-agglomerated.
[0047] [0047] In the following the details and preferred embodiments of the inventive process will be specified in greater detail. It should be understood that these technical details and embodiments also apply to the inventive suspension of self-bonding pigment particles and their use. Step a): The suspension of at least one material containing calcium carbonate
[0048] [0048] In step a) of the process of the present invention, an aqueous suspension of at least one material containing calcium carbonate is provided. The aqueous suspension of the material containing calcium carbonate can be obtained by mixing the particles of material containing calcium carbonate with water.
[0049] [0049] The material containing calcium carbonate can be selected from calcium carbonate, minerals containing calcium carbonate, mixed carbonate-based fillers, or mixtures thereof. Calcium carbonate can be selected from crushed calcium carbonate, precipitated calcium carbonate, modified calcium carbonate or mixtures thereof.
[0050] [0050] According to a preferred embodiment of the present invention, the material containing calcium carbonate is crushed calcium carbonate.
[0051] [0051] Crushed (or natural) calcium carbonate (GCC) is understood to be a naturally occurring form of calcium carbonate, mined from sedimentary rocks such as limestone or plaster, or from metamorphic marble rocks. Calcium carbonate is known to exist as three types of crystal polymorphs: calcite, aragonite and valerite. Calcite, the most common crystal polymorph, is considered to be the most stable crystal form of calcium carbonate. Less common is aragonite, which has an orthorhombic crystal structure of grouped or discrete needles. Valerite is the rarest polymorph of calcium carbonate and is generally unstable. Crushed calcium carbonate is almost exclusively from the calcitic polymorph, which is said to be trigonal-rhombohedral and represents the most stable of the calcium carbonate polymorphs. The term "source" of calcium carbonate in the meaning of the present application refers to the naturally occurring mineral material from which calcium carbonate is obtained. The source of calcium carbonate can comprise other naturally occurring components, such as magnesium carbonate, aluminosilicate, etc.
[0052] [0052] According to an embodiment of the present invention, GCC is obtained by dry grinding. According to another embodiment of the present invention, GCC is obtained by wet grinding and subsequent drying.
[0053] [0053] In general, the grinding step can be carried out with any conventional grinding device, for example, under conditions such that the comminution predominantly results from impacts with a secondary body, that is, in one or more of: a mill ball mill, a bar mill, a vibrating mill, a roller crusher, a centrifugal impact mill, a vertical bead mill, a friction mill, a pin mill, a hammer mill, a sprayer, a shredder, a decompressor, a knife cutter, or other type of equipment known to the person skilled in the art. In the event that the mineral powder containing calcium carbonate comprises a mineral material containing wet crushed calcium carbonate, the grinding step can be carried out under conditions such that autogenous and / or horizontal ball grinding and / or other such grinding takes place. processes known to the conversant. The mineral material containing wet-ground crushed calcium carbonate thus obtained can be washed and the water removed by well-known processes, for example, by flocculation, filtration or forced evaporation before drying. The subsequent drying step can be carried out in a single step such as spray drying, or in at least two steps. It is also common for such mineral material to undergo a beneficiation step (such as a flotation, bleaching or magnetic separation step) to remove impurities.
[0054] [0054] According to an embodiment of the present invention the source of crushed calcium carbonate (GCC) is selected from marble, plaster, calcite, dolomite, limestone, or mixtures thereof. Preferably, the source of crushed calcium carbonate is selected from marble.
[0055] [0055] According to one embodiment, the suspension of step a) of process comprises a crushed calcium carbonate. According to another embodiment of the present invention, the suspension of process step a) comprises a mixture of two or more crushed calcium carbonates selected from different sources of crushed calcium carbonate. For example, the suspension of at least one crushed calcium carbonate may comprise a GCC selected from dolomite and a GCC selected from marble.
[0056] [0056] According to an embodiment of the present invention, the process step a) suspension consists of at least one crushed calcium carbonate. The process step a) suspension may consist of a crushed calcium carbonate, or it may consist of two or more crushed calcium carbonates selected from different sources of crushed calcium carbonate.
[0057] [0057] "Precipitated calcium carbonate" (PCC), in the meaning of the present invention, is a synthesized material, generally obtained by precipitation following the reaction of carbon dioxide and lime in an aqueous environment or by precipitation from an ion source of calcium and carbonate in water or by precipitation of calcium and carbonate ions, for example, CaCl2 and Na2CO3, out of solution. Precipitated calcium carbonate exists in three primary crystalline forms: calcite, aragonite and valerite, and there are many different polymorphs (crystal habits) for each of these crystalline forms. Calcite has a trigonal structure, with typical crystal habits such as scalenohedral (S-PCC), rhombohedral (R-PCC), hexagonal, pinacoidal, colloidal (C-PCC), cubic, and prismatic (P-PCC). Aragonite is an orthorhombic structure with crystal habits typical of twin hexagonal prismatic crystals, as well as a diverse variety of thin elongated prismatic shapes, curved blade shapes, acute pyramids, cisterned crystals, branched tree and coral or larvae shapes .
[0058] [0058] According to one embodiment, the precipitated calcium carbonate is crushed before being used in the process of the present invention.
[0059] [0059] According to one embodiment, the suspension of step a) of process comprises a precipitated calcium carbonate, preferably scalenehedral precipitated calcium carbonate (S-PCC). According to another embodiment of the present invention, the suspension of process step a) comprises a mixture of two or more precipitated calcium carbonates selected from different sources of precipitated calcium carbonate. For example, the suspension of at least one precipitated calcium carbonate may comprise a PCC selected from S-PCC and a PCC selected from R-PCC. According to another embodiment of the present invention, the suspension of process step a) consists of at least one precipitated calcium carbonate. The suspension from step a) can consist of one type of PCC, or it can consist of a mixture of two or more types of PCC.
[0060] [0060] A modified calcium carbonate can distinguish a naturally ground or precipitated calcium carbonate with a surface and / or internal structure modification, for example, calcium carbonate can be treated or coated with a hydrophobizing surface treatment agent such as , for example, an aliphatic carboxylic acid or a siloxane. According to a preferred embodiment of the present invention, the modified calcium carbonate is a surface-reacted calcium carbonate.
[0061] [0061] According to an embodiment of the present invention, the calcium carbonate-containing material comprises a modified calcium carbonate. According to another embodiment of the present invention, the calcium carbonate-containing material comprises a mixture of two or more modified calcium carbonates having different surface and / or internal structure modifications. According to an embodiment of the present invention, the calcium carbonate-containing material consists of a modified calcium carbonate. According to another embodiment of the present invention, the calcium carbonate-containing material consists of a mixture of two or more modified calcium carbonates having different surface and / or internal structure modifications.
[0062] [0062] According to another embodiment, the material containing calcium carbonate is a mixture of crushed calcium carbonate and / or precipitated calcium carbonate and / or modified calcium carbonate.
[0063] [0063] According to an embodiment of the present invention, the minerals containing calcium carbonate comprise dolomite.
[0064] [0064] According to a preferred embodiment, mixed carbonate-based fillers are selected from calcium associated with magnesium and analogues or derivatives, various materials, such as clay or talc or analogues or derivatives, and mixtures of these charges, such as, for example, talc - calcium carbonate, or mixtures of calcium carbonate-kaolin, or mixtures of natural calcium carbonate with aluminum hydroxide, mica or with synthetic or natural fibers or mineral structures such as calcium talc-carbonate or talc- titanium dioxide or titanium calcium dioxide carbonate structures.
[0065] [0065] According to another embodiment of the present invention, the aqueous suspension comprising at least one material containing calcium carbonate comprises another mineral such as talc, kaolin, TiO2, bentonite, or mixtures thereof.
[0066] [0066] According to one embodiment, at least one material containing calcium carbonate is provided in the form of particles. The particles of material containing calcium carbonate can have a median particle diameter d50 value by weight of 0.1 to 100 µm, preferably from 0.1 to 80 µm, more preferably from 0.5 to 50 µm, and the most preferably from 5.0 to 25 µm.
[0067] [0067] According to an embodiment of the present invention, particles of material containing calcium carbonate have a specific surface area of 0.1 to 200 m2 / g, preferably 1 to 25 m2 / g, more preferably of 2 to 15 m2 / g, and most preferably 3 to 12 m2 / g, measured using nitrogen and the BET method, according to ISO 9277: 2010.
[0068] [0068] The at least one material containing calcium carbonate is suspended in water and thus forms an aqueous suspension or slurry of the material containing calcium carbonate. The obtained suspension can be crushed under conditions such that autogenous crushing takes place and / or by horizontal ball milling, and / or other processes known to the skilled person.
[0069] [0069] According to an embodiment of the present invention, the suspension provided in process step a) has a solids content of at least 1% by weight, preferably from 1 to 90% by weight, more preferably from 5 to 85% by weight, even more preferably from 20 to 75% by weight, and most preferably from 45 to 65% by weight, based on the total weight of the suspension. The suspension of process step a) can be provided in a non-dispersed or dispersed manner, i.e., the suspension includes a dispersant. According to a preferred embodiment, the suspension of step a) is undispersed, that is, it does not contain a dispersant.
[0070] [0070] According to an exemplary embodiment, at least one material containing calcium carbonate is supplied in the form of a wet filter cake, preferably having a solid content of 65 to 85% by weight, based on weight total suspension. Step b): The anionic polymeric binder
[0071] [0071] In step b) of the process according to the present invention, an anionic polymeric binder is provided, wherein said binder comprises at least one modified polysaccharide.
[0072] [0072] "Modified polysaccharides", in the meaning of the present invention, are polysaccharides, in which at least part of the hydroxyl groups are carboxylated. In addition, the modified polysaccharides may contain other modifications such as aldehyde groups.
[0073] [0073] The polysaccharides modified according to the present invention can comprise the following structure:
[0074] [0074] Polysaccharides are the structures of polymeric carbohydrates, formed by repetition units (at least 10) joined together by glycosidic bonds. Depending on the spatial arrangement of glycosidic bonds, it is possible to distinguish between glycosidic bonds α and β. These structures can be linear, but they can also contain varying degrees of branching. Polysaccharides can also contain slight modifications of the repeat unit. Exemplary polysaccharides are starch, cellulose, or glycogen, but also structural polysaccharides, such as cellulose and chitin.
[0075] [0075] The modified polysaccharide can have a degree of substitution of hydroxyl groups in the range of 0.4 to 2.0, 0.5 to 1.8, 0.6 to 1.6, or 0.7 to 1.5 .
[0076] According to an embodiment of the present invention, the at least one modified polysaccharide is a carboxymethyl derivative and / or carboxymethyl hydroxypropyl derivative and / or carboxymethyl hydroxyethyl derivative of a polysaccharide. For example, the modified polysaccharide can be a carboxymethylcellulose (CMC), an anionic starch, an anionic guar, or mixtures thereof.
[0077] [0077] According to a preferred embodiment of the present invention, the at least one modified polysaccharide is carboxymethylcellulose (CMC).
[0078] [0078] Carboxymethylcellulose (CMC) can be prepared from cellulose by reaction with monochloroacetic acid in the presence of caustic soda to form the sodium salt of carboxymethylcellulose. Each D-glucose repeat unit contains three hydroxyl groups capable of etherification, to give a maximum charge density of three carboxylic groups per unit of monomer (that is, a degree of substitution of three). The molecular weight and intrinsic viscosity of the binder materials based on carboxymethylcellulose can be adjusted by treatment with hydrogen peroxide (H2O2). Reference is made to DE 1 543 116 A1 describing a method for the preparation of low viscosity, water-soluble CMC by oxidative degradation with H2O2 (hydrogen peroxide) and to DE 44 11 681 A1 describing the dependence on polysaccharide ether degradation in the amount of oxidizing agent, temperature and duration of treatment.
[0079] [0079] According to an embodiment of the present invention, carboxymethylcellulose has an intrinsic viscosity in the range of 5 to 500 ml / g, preferably 10 to 400 ml / g, and more preferably 20 to 350 ml / g.
[0080] [0080] According to another preferred embodiment of the present invention, the at least one modified polysaccharide is an anionic starch.
[0081] [0081] Anionic starch is preferably chemically modified with anionic groups selected from the group comprising carboxyl groups, carboxymethyl groups, carboxymethyl hydroxypropyl groups, carboxymethyl hydroxyethyl groups, phosphate groups, sulfonate groups and mixtures thereof. Anionic starch can be chosen from chemically modified starches originating from starches selected from the group comprising wheat starch, corn starch, rice starch, potato starch, tapioca starch, maranta starch, sorghum starch and mixtures of themselves. In a preferred embodiment, the anionic starch is selected from amylopectin enriched, that is to say the chemically modified starch is preferably selected from the group consisting of rice starch, potato starch, and mixtures thereof. Anionic starch can also be obtained from genetically modified sources comprising starches enriched with amylopectin. Methods for preparing such anionic starches are known to the person skilled in the art. The molecular weight of anionic starch can be in the range of 1000 to 1000000 g / mol and is generally about 220000 g / mol. The molecular weight of anionic starch can be adjusted by treatment with hydrogen peroxide (H2O2).
[0082] [0082] According to another preferred embodiment of the present invention, the at least one modified polysaccharide is an anionic guar.
[0083] [0083] Guar comprises a natural heteropolysaccharide (guarano) consisting of galactose units and mannose units generally in a 1: 2 ratio, the endosperm component of guar seeds. In general, guar comprises a linear chain of 1,4-linked β-D-mannopyranosyl units with 1,6-linked α-D-galactopyranosyl units. Guar seeds containing about 14 to 1% by weight of bark, 35 to 42% by weight of endosperm and 43 to 4% by weight of embryo, are usually dry milled and sieved to separate the endosperm that is the industrial guar from business. A guar derivative can be obtained, for example, by modifying the heteropolysaccharide through the use of enzymes, acids, oxidation medium, temperature, radiation, etc. Methods for preparing such guar derivatives are known to the person skilled in the art. For example, a modification can be obtained by using a commercially available α-D-galactosidase enzyme that is usable to remove α-D-galactopyranosyl units. By controlling the extent of time that guarano is exposed to the enzyme α-Dgalactosidase, the extent of removal of α-Dgalactopyranosyl units can be controlled from the linear chain of mannose units. Additionally or alternatively, a guar modification can be obtained by etherifying guar with propylene oxide or ethylene oxide resulting in a hydroxypropyl guar or hydroxyethyl guar.
[0084] [0084] According to an embodiment of the present invention, the anionic guar is a carboxymethyl guar (CMG) and / or carboxymethyl hydroxypropyl guar (CMHPG) and / or carboxymethyl hydroxyethyl guar (CMHEG). For example, carboxymethyl guar is obtained by reacting a guar with monochloroacetic acid in the presence of caustic soda.
[0085] [0085] A modified polysaccharide solution can be concentrated, for example, by ultrafiltration or thermal drying. The dry modified polysaccharide is preferably produced by thermal drying, more preferably by spray drying and has a solids content of more than 90, preferably 95 to 99.9% by weight, based on the total weight of the modified polysaccharide.
[0086] [0086] According to an embodiment of the present invention, the process anionic polymeric binder of step a) comprises a modified polysaccharide. According to another embodiment of the present invention, the anionic binder of step a) process comprises two or more modified polysaccharides. According to a preferred embodiment of the present invention, the process anionic polymeric binder of step a) consists of at least one modified polysaccharide. The process-a) process anionic polymeric binder may consist of a modified polysaccharide type, or it may consist of a mixture of two or more modified polysaccharide types.
[0087] [0087] According to an embodiment of the present invention, the anionic polymeric binder employed in the process according to the present invention has a pH of 4.5 to 12, preferably 7 to 11, and more preferably 8.0 to 10.5.
[0088] [0088] The anionic polymeric binder can be supplied as a solution or dry material. According to a preferred embodiment, the anionic polymeric binder is in the form of an aqueous solution.
[0089] [0089] According to an embodiment of the present invention, the anionic polymeric binder is in the form of an aqueous solution having a binder concentration of 1 to 70% by weight, preferably 2 to 30% by weight, more preferably of 3 to 15% by weight, and most preferably 4 to 10% by weight, based on the total weight of the binder solution.
[0090] [0090] According to an embodiment of the present invention, the binder from step b) is added in an amount of 0.001 to 20% by weight, preferably from 0.005 to 15% by weight, more preferably from 0.01 to 10 % by weight, and most preferably 0.05 to 5% by weight, based on the total weight of the dry calcium carbonate containing material.
[0091] [0091] According to a preferred embodiment of the present invention, the anionic binder of step b) is at least one carboxymethylcellulose added in an amount of 0.05 to 5% by weight, preferably 0.5 to 2.5 % by weight, based on the total weight of the material containing dry calcium carbonate. Step c)
[0092] [0092] In step c) of the process according to the present invention, at least one cationic polymer is provided.
[0093] [0093] The inventors of the present application surprisingly found that the addition of at least one cationic polymer can lead to better retention of the self-bonding pigment particles during the papermaking processes. Without being bound by any theory, it is believed that the anionic charge of the anionic polymer binder is at least partially neutralized by the cationic polymer.
[0094] [0094] The inventors also found that the addition of at least one cationic polymer can reduce the amount of free polymer in the suspension of self-bonding pigment particles obtained. Without being limited to any theory, it is believed that the cationic polymer can improve the adhesion or adsorption of the anionic binder and / or at least one cationic polymer on the crushed calcium carbonate particles. This discovery was very surprising since it is known that the dispersion of crushed calcium carbonate with cationic starch can result in the suspension of pigment particles containing high amounts of free polymer.
[0095] [0095] In addition, the inventors surprisingly found that the self-bonding properties of the pigment particles are also improved. As a result, paper products comprising the inventive self-bonding particles as a filler material exhibit improved strength, and also allow for the production of papers with a high filler content. Another advantage is that the physical and optical properties of paper comprising the inventive self-bonding pigment particles as filler material are not impaired to any substantial degree.
[0096] [0096] According to an embodiment of the present invention, the at least one cationic polymer is selected from the group comprising polyamines, polyethyleneimines, polyacrylamides, cationic epichlorohydrin resins, polydialldimethylammonium chloride, cationic starch, cationic guar, or mixtures thereof. .
[0097] [0097] According to another embodiment of the present invention, the at least one cationic polymer is a polyamine, preferably a polyethyleneimine (PEI) being selected from the group comprising branched polyethyleneimines, linear polyethyleneimines and mixtures thereof. Preferably, the function ratio of primary, secondary and tertiary amines in the inventive branched polyethyleneimines is in the range of 1: 0.86: 0.42 to 1: 1.20: 0.76, before a possible modification of the branched polyethyleneimines.
[0098] [0098] According to a preferred embodiment of the present invention, at least one polyethyleneimine is selected from the group of modified and unmodified polyethyleneimines. Examples for suitable polyethyleneimines are ethylenimine homopolymers (aziridine) or their superior counterparts and also the graft polymers of polyamidoamines or polyvinylamines with ethyleneimine or their superior counterparts. Polyethyleneimines can be cross-linked or non-cross-linked, quaternized and / or modified by reaction with alkylene oxides, dialkyl or alkylene carbonates or C1-C8-carboxylic acids. Polyethyleneimines can be modified by reaction with alkylene oxides such as ethylene oxide, propylene oxide or butylene oxide, dialkyl carbonates such as dimethyl carbonate and diethyl carbonate, alkylene carbonates such as ethylene carbonate or propylene carbonate, or acids C1- C8-carboxylics. Modified PEIs can include alkoxylated polyethyleneimines such as propoxylated polyethyleneimines (PPEIs) and ethoxylated polyethyleneimines (EPEIs). Other preferred modified polyethyleneimines can be obtained by reacting unmodified PEIs with one or more C1-C28-fatty acids, preferably with one or more C6-C18-fatty acids and especially preferred with C10-C14-fatty acids, such as, for example , coconut fatty acid.
[0099] [0099] Polyethyleneimine can have an average molecular weight Mw in the range of 1000 g / mol and 1000000 g / mol. In another preferred embodiment of the present invention, polyethyleneimine is selected from the group of linear polyethyleneimines having a weight average molecular weight Mw of 100 to 700 g / mol, and preferably 146 to 232 g / mol, and is preferably selected from among triethylenetetramine, pentaethylene hexamine and tetraethylenepentamine. According to another preferred embodiment, polyethyleneimine is selected from the group of branched polyethyleneimines having a weight average molecular weight Mw of 500 to 8000 g / mol and preferably 800 to 1200 g / mol.
[0100] [00100] According to an embodiment of the present invention, the at least one cationic polymer is a cationic starch.
[0101] [00101] Cationic starch is preferably chemically modified with cationic groups selected from the group comprising amino groups, imonium groups, ammonium groups, sulfonium groups, phosphonium groups, and mixtures thereof. Cationic starch can be chosen from chemically modified starches originating from any virtual natural sources giving reasonable amounts of starch. For example, cationic starch can be chosen from chemically modified starches originating from starches selected from the group comprising wheat starch, corn starch, rice starch, potato starch, tapioca starch, maranta starch, sorghum starch and mixtures thereof. In a preferred embodiment, the cationic starch is selected from those enriched with amylopectin, i.e., the chemically modified starch is preferably selected from the group consisting of rice starch, potato starch, and mixtures thereof. Cationic starch can also be obtained from genetically modified sources comprising starches enriched with amylopectin. Methods for preparing such cationic starches are known to the person skilled in the art. The molecular weight of the cationic starch can be in the range of 1000 to 1000000 g / mol and is generally about 220000 g / mol. The molecular weight of cationic starch can be adjusted by treatment with hydrogen peroxide (H2O2).
[0102] [00102] According to another embodiment of the present invention, the at least one cationic polymer is a cationic guar.
[0103] [00103] Guar comprises a natural heteropolysaccharide (guarano) consisting of galactose units and mannose units generally in the ratio of 1: 2 and is the endosperm component of guar seeds. In general, guar comprises a linear chain of 1,4-linked β-D-mannopyranosyl units with 1,6-linked α-D-galactopyranosyl units. Guar seeds containing about 14 to 1% by weight of bark, 35 to 42% by weight of endosperm and 43 to 4% by weight of embryo, are generally dry milled and sieved to separate the endosperm that is the industrial guar from business. A guar derivative can be obtained, for example, by modifying the heteropolysaccharide through the use of enzymes, acids, oxidation medium, temperature, radiation, etc. Methods for preparing such guar derivatives are known to the person skilled in the art. For example, a modification can be achieved by using a commercially available α-D-galactosidase enzyme, which is usable to remove α-D-galactopyranosyl units. By controlling the length of time that guarano is exposed to the enzyme α-D-galactosidase, the extent of removal of α-D-galactopyrosyl units from the linear chain of mannose units can be controlled. A cationic guar can be obtained by reacting guar with derivatives of quaternary ammonium salts.
[0104] [00104] According to yet another embodiment of the present invention, the at least one cationic polymer is polydialyldimethylammonium chloride (polyDADMAC).
[0105] [00105] PoliDADMAC (polydialyldimethylammonium chloride) is a linear homopolymer of diallyldimethylammonium chloride (DADMAC) having the following structure:
[0106] [00106] The linear homopolymer formed from a monomer that has a quaternary ammonium and two unsaturated functionalities -CH = CH2 is polymerized by polymerization by free radicals from DADMAC. In the quaternary ammonium groups of polyDADMAC structure they are in rings that are included in the dorsal structure of the polymer chain. This composition means that polyDADMAC macromolecules tend to be quite rigid, having a longer persistence length than, for example, polyamines. For this reason, poliDADMAC is expected to have a more extended conformation in solution. The polyDADMAC can have a weight average molecular weight Mw in the range of 10000 to 1000000 g / mol and preferably in the range of 100000 to 500000 g / mol.
[0107] [00107] Other examples of cationic polymer that are suitable for the process of the present invention are polyacrylamides, or cationic epichlorohydrin resins.
[0108] [00108] According to an exemplary embodiment, polyacrylamides include monomers of dialkylaminoethyl (meth) acrylates, dialkylaminoethyl (meth) acrylamides, dialkylaminomethyl (meth) acrylamides, and (dialkylamino-1,3) acrylamides -propyl, preferably copolymerized with nonionic monomers, preferably arylamide.
[0109] [00109] According to another embodiment, the cationic epichlorohydrin resins are copolymers comprising as the monomer one or more dicarboxylic acids and one or more monomers among the group of diamines, triamines, dialcanolamines or trialcanolamines and epichlorohydrin.
[0110] [00110] Preferably C2-C10 saturated or unsaturated, branched or unbranched dicarboxylic acids, preferably C3-C9 dicarboxylic acids, C4-C8 dicarboxylic acids, C5-C7 dicarboxylic acids, in particular, adipic acid are used as the dicarboxylic acid monomers . Especially suitable as the second monomer of the binder polymer are the substituted and unsubstituted linear and branched diamines and triamines, in particular N- (2-aminoethyl) -1,2-ethanediamine. Preferably dialcanolamines and trialcanolamines are used include, for example, diethanolamine, N-alkyl-dialcanolamines such as N-methyl and N-ethyldiethanolamine and triethanolamine. For monitoring and control of molecular weight and / or chain length, one or more monovalent amines such as monoalkanolamines can be used during polycondensation. Monoethanol is preferably used. The resulting intermediate product is further reacted with epichlorohydrin.
[0111] [00111] According to a preferred embodiment of the present invention, the cationic epichlorohydrin resin is an adipic acid copolymer with N- (2-aminoethyl) -1,2-ethanediamine and epichlorohydrin.
[0112] [00112] According to an embodiment of the present invention, the at least one cationic polymer is a mixture of two or more of the aforementioned polymers. According to another embodiment of the present invention, the at least one cationic polymer consists of one of the aforementioned polymers.
[0113] [00113] According to a preferred embodiment, the at least one cationic polymer is polyDADMAC. According to another preferred embodiment, the at least one cationic polymer is a cationic starch.
[0114] [00114] The at least one cationic polymer can be provided in an aqueous form, for example, in the form of a water-based solution, or in the form of an organic solution, for example, in an organic solvent selected from the group comprising methanol, ethanol, acetone, and mixtures thereof. However, the at least one cationic polymer can also be provided in the form of an emulsion or dispersion of water and / or organic solvents, or in the form of a mixture of a solution and / or an emulsion and / or a dispersion of water and / or organic solvents.
[0115] [00115] If at least one cationic polymer is provided in the form of a solution, the solution is preferably prepared, wherein the at least one cationic polymer is added to a solvent, preferably water, having a temperature of at least 50 ° C , preferably between 50 ° C and 100 ° C, more preferably between 60 ° C and 98 ° C and most preferably between 70 ° C and 96 ° C. For example, the solution is prepared in which at least one cationic polymer is added to the water having a temperature between 80 ° C and 96 ° C, such as between 90 ° C and 96 ° C.
[0116] [00116] Alternatively, the starch solution is prepared in which at least one cationic polymer is added to a solvent, preferably water, having a temperature below 50 ° C, preferably between 5 ° C and 50 ° C, more preferably between 10 ° C and 40 ° C and most preferably 15 ° C and 30 ° C.
[0117] [00117] In a preferred embodiment, the cationic polymer solution is prepared in which at least one cationic polymer is added in water at about room temperature, that is, at a temperature of 20 ° C ± 2 ° C.
[0118] [00118] According to an alternative embodiment, the at least one cationic polymer is provided in the dry form, for example, in the form of a dry powder.
[0119] [00119] In case the at least one cationic polymer is provided in the form of a dispersion, the particle size of the cationic polymer can have a d50 value of 10 to 500 nm, preferably 20 to 100, and more preferably 25 at 80 nm.
[0120] [00120] The at least one cationic polymer of step c) can be provided in the form of a solution or dry material, preferably in the form of an aqueous solution having a concentration of 1 to 70% by weight, preferably from 2 to 55% by weight. weight, more preferably 5 to 50% by weight, and most preferably 30 to 50% by weight, based on the total weight of the solution.
[0121] [00121] According to an embodiment of the present invention, the cationic polymer is added in an amount so that the charge density of the self-bonding pigment particles obtained is less compared to the self-bonding pigment particles not containing the cationic polymer. For example, the cationic polymer can be added in an amount such that the charge density of the self-bonding pigment particles obtained is between -100 and -5 µEq / g, preferably between -80 and -10 µEq / g, and more preferably between -70 and -15 µEq / g.
[0122] [00122] According to an embodiment of the present invention, the at least one cationic polymer of step c) is added in an amount of 0.001 to 20% by weight, preferably from 0.005 to 15% by weight, more preferably from 0 .01 to 10% by weight, and most preferably 0.05 to 5% by weight or 0.5 to 2.5% by weight, based on the total weight of the material containing dry calcium carbonate.
[0123] [00123] According to a preferred embodiment of the present invention, the at least one cationic polymer of step c) is polyDADMAC, preferably added in an amount of 0.05 to 5% by weight, more preferably from 0.5 to 2.5% by weight, based on the total weight of the material containing dry calcium carbonate.
[0124] [00124] According to another preferred embodiment of the present invention, the at least one cationic polymer of step c) is a cationic starch, preferably added in an amount of 0.05 to 5% by weight, more preferably 0, 5 to 2.5% by weight, based on the total weight of the material containing dry calcium carbonate.
[0125] [00125] According to a preferred embodiment of the present invention, the anionic binder of step b) is at least one carboxymethylcellulose, and the at least one cationic polymer of step c) is polyDADMAC, in which the binder is added in a amount of 0.5 to 2.5% by weight, preferably 1.0 to 2.0% by weight, and the cationic polymer is added in an amount of 0.5 to 2.5% by weight, preferably 0, 8 to 2.0% by weight, based on the total weight of the material containing dry calcium carbonate.
[0126] [00126] According to an exemplary embodiment, the anionic binder of step b) is a carboxymethylcellulose, and the at least one cationic polymer of step c) is polyDADMAC, in which the binder is added in an amount of about 2 , 0% by weight, and the cationic polymer is added in an amount of 0.8 to 2.0% by weight, based on the total weight of the material containing dry calcium carbonate.
[0127] [00127] According to another exemplary embodiment, the material containing calcium carbonate is calcium carbonate, preferably crushed calcium carbonate, the anionic binder of step b) is a carboxymethylcellulose, and at least one cationic polymer of step c ) is polyDADMAC, in which the binder is added in an amount of about 2.0% by weight, and the cationic polymer is added in an amount of 0.8 to 2.0% by weight, based on the total weight of the material containing dry calcium carbonate.
[0128] [00128] According to a preferred embodiment of the present invention, the anionic binder of step b) is at least one carboxymethylcellulose, and the at least one cationic polymer of step c) is a cationic starch, in which the binder is added in an amount of 0.5 to 2.5% by weight, preferably 1.0 to 2.0% by weight, and at least one cationic polymer is added in an amount of 0.5 to 2.5% by weight , preferably from 0.7 to 2.0% by weight, based on the total weight of the material containing dry calcium carbonate.
[0129] [00129] According to an exemplary embodiment, the anionic binder of step b) is a carboxymethylcellulose, and the at least one cationic polymer of step c) is a cationic starch, in which the binder is added in an amount of about 0.5% by weight, and the cationic polymer is added in an amount of about 1.5% by weight, based on the total weight of the material containing dry calcium carbonate.
[0130] [00130] According to another exemplary embodiment, the material containing calcium carbonate is calcium carbonate, preferably crushed calcium carbonate, the anionic binder of step b) is a carboxymethylcellulose, and at least one cationic polymer of step c ) is a cationic starch, in which the binder is added in an amount of about 0.5% by weight, and the cationic polymer is added in an amount of about 1.5% by weight, based on the total weight of the material containing dry calcium carbonate. Step d): Mixing
[0131] [00131] In step d) of the process of the present invention, the suspension of step a) and the binder of step b) are mixed.
[0132] [00132] According to an embodiment of the present invention, the at least one cationic polymer from step c) is mixed in step d) with the suspension from step a) and the binder from step b).
[0133] [00133] According to an embodiment of the present invention, the suspension of step a) is, in a first step, mixed with the binder of step b), and then, in a second step, it is mixed with at least cationic polymer from step c).
[0134] [00134] According to another embodiment of the present invention, the suspension of step a) is, in a first step, mixed with the binder of step b), and then, in a second step, it is mixed with at least a cationic polymer from step c), in which, in the first step, a suspension of step a) is mixed with a first part of the binder from step b), the mixture obtained is ground and then mixed with the remaining part of the binder of step b).
[0135] [00135] According to another embodiment of the present invention, the binder of step b) is, in a first step, mixed with the cationic polymer of step c), and then, in a second step, it is mixed with the suspension step a).
[0136] [00136] According to yet another embodiment of the present invention, the suspension of step a) is mixed with the binder of step b) and the cationic polymer of step c) in one step.
[0137] [00137] According to an exemplary embodiment of the present invention, in a first step, the suspension of step a) is mixed with the binder of step b), wherein said binder is provided in the form of a solution, and then , in a second step, the at least one cationic polymer from step c) is added to a suspension in the form of a dry powder.
[0138] [00138] According to another exemplary embodiment of the present invention, in a first step, the at least one cationic polymer from step c) is mixed with the binder from step b) to form a pre-mixed solution, wherein the cationic polymer and the binder are provided in the form of a solution, and then, in a second step, the premixed solution is mixed with the suspension from step a).
[0139] [00139] The mixing step d) can be carried out under mixing and / or homogenization conditions. The person skilled in the art will adapt these mixing and / or homogenization conditions, such as mixing speed and temperature according to his process equipment. For example, mixing and homogenization can take place by means of a plow mixer. Plow mixers operate on the principle of a mechanically produced fluidized bed. The plow blades rotate close to the inner wall of a horizontal cylindrical drum and transport the components of the mixture out of the product bed and into the open mixing space. The mechanically produced fluidized bed ensures an intense mixture of even large batches in a very short time. Cutters and / or dispersers are used to disperse lumps in a dry operation. The equipment that can be used in the inventive process is available, for example, from Gebrüder Lödige Maschinenbau GmbH, Germany, or from Silverson, USA In addition, a tubular mixing apparatus can be used, for example, from Ystral GmbH, Ballrechten-Dottingen , Germany. Another piece of equipment that can be used in the inventive process is a MEGATRON® Inline homogenizer from Kinematika AG, Switzerland.
[0140] [00140] According to an embodiment of the present invention, process step d) is carried out using a fluidized bed mixer or plowed type mixer.
[0141] [00141] Process step d) can be carried out at room temperature, that is, at a temperature of 20 ° C ± 2 ° C, or at other temperatures. According to one embodiment, process step d) is carried out at a temperature of 5 to 140 ° C, preferably 10 to 110 ° C, and most preferably 20 to 105 ° C. Heat can be introduced by internal shear or by an external source or a combination thereof.
[0142] [00142] According to an exemplary embodiment of the invention, the suspension from step a) and / or the anionic polymeric binder from step b) is preheated beforehand and these components are mixed in the process step d). For example, the suspension of step a) and / or the anionic polymeric binder of step b) can be preheated to a temperature of 30 to 100 ° C, 40 to 90 ° C, or preferably 50 to 80 ° C . According to another exemplary embodiment of the invention, the suspension of step a) and / or the anionic polymeric binder of step b) and / or at least one cationic polymer of step c) is preheated beforehand and these components are mixed in process step d). For example, the suspension of step a) and / or the anionic polymeric binder of step b) and / or at least one cationic polymer of step c) can be preheated to a temperature of 30 to 100 ° C, 40 at 90 ° C, or preferably from 50 to 80 ° C.
[0143] [00143] According to an embodiment of the present invention, process step d) is carried out for at least 1 s, preferably for at least 1 min, for example, for at least 15 min, 30 min, 1 hour, 2 hours, 4 hours, 6 hours, 8 hours, or 10 hours.
[0144] [00144] To ensure better dispersion, a dispersant can also be added to any of the components used in the inventive process, for example, in the form of an aqueous solution and / or a powder of a dispersant. A suitable dispersant is preferably selected from the group comprising homopolymers or copolymers of polycarboxylic acid salts based on, for example, acrylic acid, methacrylic acid, maleic acid, fumaric acid or itaconic acid and acrylamide or mixtures thereof. Acrylic acid homopolymers or copolymers are especially preferred. The weight average molecular weight Mw of such products is preferably in the range of 2000 to 15000 g / mol, with a weight average molecular weight Mw of 3000 to 7000 g / mol or 3500 to 6000 g / mol being especially preferred. According to an exemplary embodiment, the dispersant is sodium polyacrylate having a weight average molecular weight Mw from 2000 to 15000 g / mol, preferably from 3000 to 7000 g / mol, and most preferably from 3500 to 6000 g / mol .
[0145] [00145] According to a preferred embodiment, no dispersant is added in process step d).
[0146] [00146] The mixing step can be carried out at a high solid content, that is, at a solid content of 50 to 80% by weight, based on the total weight of the suspension. However, the mixing step can be carried out at a solid content of more than 80% by weight, based on the total weight of the suspension, for example, using a plow mixer.
[0147] [00147] The solids content of the suspension can be adjusted by methods known to the person skilled in the art. To adjust the solids content of an aqueous mineral material comprising suspension, the suspension can be partially or completely dehydrated by filtration, centrifugation or thermal separation process. For example, suspensions can be partially or completely dehydrated by a filtration process such as nanofiltration or a thermal separation process, such as an evaporation process. Or, alternatively, water can be added to the solid mineral material (for example, resulting from filtration) until the desired solids content is obtained. Additionally or alternatively, the suspension of self-bonding pigment particles or another pigment particle suspension having an appropriate lower content of solid particles can be added to the particulate material of the mixed suspension until the desired solid content is obtained. Suspensions of additionally added self-bonding pigment particles or other suspensions of pigment particles can be dispersed or non-dispersed.
[0148] [00148] According to an embodiment of the present invention, the solids content of the mixed suspension of step d) is adjusted so that it is from 10 to 80% by weight, more preferably from 20 to 70% by weight, the more preferably 40 to 65% by weight, based on the total weight of the suspension.
[0149] [00149] According to a preferred embodiment of the present invention, the solid content of the mixed suspension of step d) is adjusted to a high solid content so that it is 50 to 80% by weight, more preferably 60 to 79% by weight, most preferably 65 to 78% by weight, based on the total weight of the suspension. Step e)
[0150] [00150] In step e) of the process according to the present invention, the mixed suspension of step d) is crushed.
[0151] [00151] According to one embodiment, the aqueous environment of the suspension to be ground has a pH of 7 to 12, preferably 8 to 11, and more preferably 8.5 to 10.5.
[0152] [00152] The grinding process can be carried out by all techniques and grinders well known to those skilled in the art by wet grinding. The grinding step can be carried out with any conventional grinding device, for example, under conditions such that the comminution predominantly results from impacts with a secondary body, that is, in one or more of: a ball mill, a bars, a vibrating mill, a centrifugal impact mill, a vertical bead mill, a friction mill, or other such equipment known to the person skilled in the art. The grinding step e) can be carried out batchwise or continuously, preferably continuously.
[0153] [00153] According to an embodiment of the present invention, the grinding step e) is carried out at a temperature of 5 to 110 ° C, 10 to 100 ° C, 15 to 80 ° C, or 20 ° C to 25 ° C. For example, the grinding step e) is carried out at a temperature of at least 50 ° C, preferably between 50 ° C and 100 ° C, more preferably between 60 ° C and 90 ° C and most preferably between 60 ° C and 70 ° C. Or, alternatively, the grinding step e) is carried out at a temperature below 50 ° C, preferably between 10 ° C and 50 ° C, more preferably between 20 ° C and 40 ° C and most preferably between 20 ° C and 30 ° C. For example, the grinding step e) is carried out at room temperature, that is, at a temperature of 20 ° C ± 2 ° C.
[0154] [00154] In a preferred embodiment of the present invention, the grinding step e) is carried out until the fraction of self-ligating pigment particles having a particle size of less than 1 µm is greater than 10% by weight, preferably greater than 20% by weight, more preferably greater than 30% by weight, and most preferably greater than 50% by weight, based on the total weight of the pigment particles, as measured with a Mastersizer 2000.
[0155] [00155] Additionally or alternatively, the grinding step e) is carried out until the fraction of self-ligating pigment particles having a particle size of less than 2 µm is greater than 20% by weight, preferably greater than 40% in weight, more preferably greater than 60% by weight, and most preferably greater than 80% by weight, based on the total weight of the pigment particles, as measured with a Mastersizer 2000.
[0156] [00156] Additionally or alternatively, the self-ligating pigment particles obtained by the process of the present invention can have a d50 value of median particle diameter by weight, measured according to the sedimentation method, in the range of 0.1 µm to 10 µm , preferably from 0.5 µm to 8 µm and most preferably from 0.8 µm to 6 µm, for example, from 1.0 µm to 5.5 µm. Additionally or alternatively, the self-bonding pigment particles obtained in step e) may have a d98 of less than 25 µm, preferably less than 20, more preferably less than 15 µm, and most preferably less than 10 µm .
[0157] [00157] According to an embodiment of the present invention, the at least one cationic polymer from step c) is mixed with the suspension obtained in the grinding step e) and the obtained mixture is de-agglomerated.
[0158] [00158] The mixing can be carried out in the same way as described under step d) above.
[0159] [00159] To de-agglomerate the obtained mixture, an in-line homogenizer can be used, for example, Megatron® homogenizer from Kinematika AG, Switzerland. Other optional process steps
[0160] [00160] According to an optional embodiment of the present invention, the process further comprises a step of concentrating the suspension of self-bonding pigment particles obtained by the process of the present invention.
[0161] [00161] The solids content of the suspension of self-ligating pigment particles obtained can be adjusted by concentration of methods known to the person skilled in the art. The concentration of the corresponding pigment material suspension can be obtained by means of a thermal process, for example, in an evaporator, or by means of a mechanical process, for example, in a filter press such as nanofiltration, and / or centrifuge.
[0162] [00162] The solids content of the suspension of self-ligating pigment particles obtained by the process of the present invention can be concentrated so that it is from 10 to 80% by weight, more preferably from 20 to 70% by weight, most preferably from 40 to 60% by weight, based on the total weight of the suspension. According to a preferred embodiment, the solid content of the suspension of self-bonding pigment particles obtained is concentrated to an average solid content such that it is 50 to 60% by weight. Or alternatively, the solid content of the self-bonding pigment particle suspension obtained can be concentrated to a high solid content such that it is 50 to 80% by weight, more preferably 60 to 79% by weight, most preferably of 65 to 78% by weight, based on the total weight of the suspension.
[0163] [00163] According to an optional embodiment of the present invention, the step of concentrating the suspension of self-ligating particles obtained by the process of the present invention is carried out so that a dry product is obtained. The term "dry product" is understood to refer to pigment particles having a total surface moisture content of less than 0.5% by weight, preferably less than 0.2% by weight and more preferably less than 0.1% by weight, based on the total weight of the pigment particles.
[0164] [00164] If the inventive process still comprises the optional step of concentrating the suspension of self-bonding pigment particles obtained so that a dry product or a suspension having a solids content of at least 65% by weight is obtained, more preferably at least 80% by weight and most preferably at least 90% by weight, based on the total weight of the suspension of self-bonding pigment particles, the dry product or suspension can be further diluted. If the dry product or suspension is further diluted, the solids content in the obtained suspension is adjusted so that it is at least 1% by weight, preferably from 1% by weight to 80% by weight, more preferably 5% by weight at 60% by weight, even more preferably from 10% by weight to 50% by weight, and most preferably from 15% by weight to 45% by weight, based on the total weight of the suspension of self-bonding pigment particles.
[0165] [00165] In a preferred embodiment of the present invention, the process of the present invention can directly lead to the suspension of high solids of self-ligating pigment particles, i.e., to a suspension having a solid content of 50 to 80% by weight , based on the total weight of the suspension of self-bonding pigment particles, which means that an additional concentration step is not implemented in the process of the present invention.
[0166] [00166] To ensure a better dispersion, a dispersant can also be added to any of the components used in the inventive process, for example, in the form of an aqueous solution and / or a powder of a dispersant. A suitable dispersant is preferably selected from the group comprising homopolymers or copolymers of polycarboxylic acid salts based on, for example, acrylic acid, methacrylic acid, maleic acid, fumaric acid or itaconic acid and acrylamide or mixtures thereof. Acrylic acid homopolymers or copolymers are especially preferred. The weight average molecular weight Mw of such products is preferably in the range of 2000 to 15000 g / mol, with a weight average molecular weight Mw of 3000 to 7000 g / mol or 3500 to 6000 g / mol being especially preferred. According to an exemplary embodiment, the dispersant is sodium polyacrylate having a weight average molecular weight Mw from 2000 to 15000 g / mol, preferably from 3000 to 7000 g / mol, and most preferably from 3500 to 6000 g / mol .
[0167] [00167] According to a preferred embodiment, no dispersant is added to any of the process steps, preferably no dispersant is added to the process step e). The suspension of self-bonding pigment particles
[0168] [00168] According to another aspect, the present invention relates to a suspension of self-ligating pigment particles that is obtainable by the process according to the present invention.
[0169] The inventive self-bonding pigment particle suspension preferably has a low amount of free polymer in the water phase of the suspension. The total polymer content in the water phase can be determined after drying at 120 ° C by measuring the loss in ignition values (LOI) at 570 ° C. To determine the free polymer content, the suspension is diluted and centrifuged. The filter cake is dried at 120 ° C and the ignition value loss at 570 ° C measured. The difference between the two LOI values is referred to as delta LOI (dLOI). A method for determining ignition loss, and dLOI, is described in the example section.
[0170] [00170] According to an embodiment of the present invention, the amount of free polymer in the water phase of the inventive self-bonding pigment particle suspension is below 70% by weight, preferably below 50% by weight, more preferably below 30% by weight, and most preferably below 25% by weight, based on the total amount of polymer added to the suspension of the calcium carbonate containing material.
[0171] [00171] According to another embodiment of the present invention, the charge density of the inventive self-ligating pigment particles is between -100 and -5 µEq / g, preferably between -90 and -20 µEq / g, more preferably between - 80 and -40 µEq / g, and most preferably between - 75 and -60 µEq / g.
[0172] [00172] The inventive self-bonding pigment particles can have a specific surface area of 0.1 to 200 m2 / g, preferably from 1 to 25 m2 / g, more preferably from 2 to 15 m2 / g, and most preferably from 3 to 12 m2 / g, measure using nitrogen and the BET method according to ISO 9277: 2010.
[0173] [00173] According to another aspect of the present invention, the suspension of self-bonding pigment particles obtainable by the inventive process is used in paper, plastics, paint, coatings, concrete and / or applications in agriculture, for example, as filler.
[0174] [00174] According to an exemplary embodiment of the present invention, the suspension of self-ligating particles obtainable by the inventive process is used on paper, for example, in the wet end process of a paper-making machine, preferably on cigarette paper, plate and / or coating applications, or preferably as a support for gravure and / or offset and / or inkjet printing and / or continuous inkjet printing and / or flexography and / or electrography and / or decoration surfaces.
[0175] [00175] Another application is in the coating of tree leaves and / or plant leaves to reduce exposure to sunlight and UV from the leaf surface.
[0176] [00176] In accordance with another aspect of the present invention, a paper product is provided comprising the inventive self-bonding pigment particles, wherein the pigment particles comprise particles of material containing calcium carbonate that are at least partially coated with a binder of calcium carbonate. anionic polymer comprising at least one modified polysaccharide and at least one cationic polymer.
[0177] [00177] According to one embodiment, the paper product comprising the inventive self-bonding pigment particles has a greater flexural stiffness, compared to a paper product, in which the inventive self-bonding pigment particles are replaced by the same amount of particles of material containing calcium carbonate. According to an embodiment of the present invention, the flexural stiffness is at least 5% greater, preferably at least 7% greater, and more preferably at least 10% greater compared to the flexural stiffness of a paper product, in that the inventive self-bonding pigment particles are replaced by the same amount of particles of material containing calcium carbonate.
[0178] [00178] According to an exemplary embodiment the paper comprising the inventive self-bonding pigment particles as the loading material has a flexural stiffness of at least 0.25 mNm, preferably at least 0.30 mNm at a fill load of 20% by weight.
[0179] [00179] It should be understood that the advantageous embodiments described above with respect to the inventive method for producing self-bonding pigment particles can also be used to prepare or define the inventive suspension and its use. In other words, the preferred embodiments described above and any combinations of these embodiments can also be applied to an inventive suspension and its use.
[0180] [00180] The scope and interest of the invention will be better understood based on the following figures and examples which are intended to illustrate certain embodiments of the invention and are not limiting. Description of figures:
[0181] [00181] Figure 1 shows the relative retention values obtained for paper suspensions comprising the pigment particles of Examples 1, 3, and 11 as fillers, in which the pulp was diluted in tap water.
[0182] [00182] Figure 2 shows the relative retention values obtained for paper suspensions comprising the pigment particles of Examples 1, 3, and 11 as fillers, where the pulp was diluted in clear filtrate.
[0183] [00183] Figure 3 shows the breaking length of uncoated, wood-free paper containing Hydrocarb® HO ME - 67% and the pigment particles of Example 4 as fillers in different amounts.
[0184] [00184] Figure 4 shows the tensile index of uncoated wood-free paper containing Hydrocarb® HO ME - 67% and the pigment particles of Example 4 as fillers in different amounts.
[0185] [00185] Figure 5 shows the traction energy absorption of uncoated, wood-free paper containing Hydrocarb ® HO ME - 67% and the pigment particles of Example 4 as fillers in different amounts.
[0186] [00186] Figure 6 shows the growth job of tearing uncoated wood-free paper containing Hydrocarb® HO ME - 67% and the pigment particles of Example 4 as fillers in different amounts.
[0187] [00187] Figure 7 shows the internal connection (z direction) of uncoated wood-free paper containing Hydrocarb® HO ME - 67% and the pigment particles of Example 4 as fillers in different amounts.
[0188] [00188] Figure 8 shows the flexural stiffness of uncoated, wood-free paper containing Hydrocarb® HO ME - 67% and the pigment particles of Example 4 as fillers in different amounts.
[0189] [00189] Figure 9 shows the elasticity modulus of uncoated, wood-free paper containing Hydrocarb® HO ME - 67% and the pigment particles of Example 4 as fillers in different amounts.
[0190] [00190] Figure 10 shows the amount of retention aid required for paper suspensions containing Hydrocarb® HO ME - 67%, Hydrocarb® HO ME - 67% and a cationic polymer, the pigment particles of Example 1, the particles of Example 3 pigment as fillers.
[0191] [00191] Figure 11 shows the tensile index of supercalendered paper containing Hydrocarb® HO ME - 67%, Hydrocarb® HO ME - 67% and a cationic polymer, the pigment particles of Example 1, the pigment particles of Example 3 as loads.
[0192] [00192] Figure 12 shows the traction energy absorption of supercalendered paper containing Hydrocarb® HO ME - 67%, Hydrocarb® HO ME - 67% and a cationic polymer, the pigment particles of Example 1, the pigment particles of Example 3 as charges.
[0193] [00193] Figure 13 shows the internal bonding of supercalendered paper containing Hydrocarb® HO ME - 67%, Hydrocarb® HO ME - 67% and a cationic polymer, the pigment particles of Example 1, the pigment particles of Example 3 as loads.
[0194] [00194] Figure 14 shows the amount of free polymer in aqueous suspensions of self-ligating calcium carbonate particles versus the amount of the cationic polymer added.
[0195] [00195] Figure 15 shows the turbidity values obtained for paper suspensions containing Hydrocarb® HO ME - 67% or as pigment particles from Examples 15 to 20 as fillers.
[0196] [00196] Figure 16 shows the turbidity values obtained for paper suspensions containing Hydrocarb® HO ME - 67% or as pigment particles from Examples 21 to 25 as fillers.
[0197] [00197] Figure 17 shows the breaking length of uncoated, wood-free paper containing Hydrocarb® HO ME - 67% with and without cationic polymer, the pigment particles of Example 27 with and without cationic polymer, and the particles of pigment of Example 28 as fillers in different amounts.
[0198] [00198] Figure 18 shows the tensile index of uncoated, wood-free paper containing Hydrocarb® HO ME - 67% with and without cationic polymer, the pigment particles of Example 27 with and without cationic polymer, and the particles of pigment of Example 28 as fillers in different amounts.
[0199] [00199] Figure 19 shows the traction energy absorption of uncoated, wood-free paper containing Hydrocarb ® HO ME - 67% with and without cationic polymer, the pigment particles of Example 27 with and without cationic polymer, and the pigment particles of Example 28 as fillers in different amounts.
[0200] [00200] Figure 20 shows the flexural stiffness of uncoated, wood-free paper containing Hydrocarb® HO ME - 67% with and without cationic polymer, the pigment particles of Example 27 with and without cationic polymer, and the particles of pigment of Example 28 as fillers in different amounts.
[0201] [00201] Figure 21 shows the internal connection (z direction) of uncoated wood-free paper containing Hydrocarb® HO ME - 67% with and without cationic polymer, the pigment particles of Example 27 with and without cationic polymer, and the pigment particles of Example 28 as fillers in different amounts. EXAMPLES 1. Measurement methods
[0202] [00202] In the following, materials and measurement methods implemented in the examples are described. Brookfiled viscosity
[0203] [00203] The Brookfiled viscosity of the suspension of self-ligating pigment particles was measured after one hour of production and after one minute of stirring at room temperature at 100 rpm using a Brookfield viscometer of the RVT type equipped with an appropriate spindle. Particle size
[0204] [00204] The particle distribution of the crushed calcium carbonate particles was measured using a Sedigraph 5120 from Micromeritics, USA. The particle size distribution of the inventive self-ligating pigment particles was measured using a Mastersizer 2000 from Malvern Instruments Ltd, England. The method and instruments are known to the person skilled in the art and are commonly used to determine the grain size of fillers and pigments. The measurement was carried out in an aqueous solution comprising 0.1% by weight of Na4P2O7. The samples were dispersed using a high speed and supersonic stirrer. Solids content of an aqueous suspension
[0205] [00205] The solids content of the suspension (also known as “dry weight”) was determined using an HR73 Moisture Analyzer from Mettler-Toledo, Switzerland, with the following settings: temperature of 120 ° C, automatic shut-off 3, drying standard, 5 to 20 g of suspension. Intrinsic viscosity
[0206] [00206] The intrinsic viscosity was determined by a Schott AVS 370 system. The samples were dissolved in a 0.2 M NaCl solution, and subsequently, the pH was adjusted to 10 with NaOH. Measurements were performed at 25 ° C with a capillary type 0a and corrected using the Hagenbach correction. Polyelectrolyte (PET) titration
[0207] [00207] The polyelectrolyte content in the aqueous suspension was determined using a Mettler DL 55 Memotitrator device, equipped with a Phototrode DP 660, marketed by Mettler-Toledo, Switzerland. Measurements of the polyelectrolyte content were performed by weighing a sample of the calcium carbonate suspension in a titration vessel and diluting the sample with deionized water to a volume of approximately 40 ml. Subsequently, 10 ml of 0.01 M cationic N (N, N-dimethyl-3,5-dimethylene-piperidinium chloride) (PDDPC; obtained from ACROS Organics, Belgium) were slowly added under stirring to the titration vessel in 5 min and then the contents of the vessel were stirred for another 20 min. Then, the suspension was filtered through a 0.2 μm mixed ester membrane filter (Ø 47 mm) and washed with 5 ml of deionized water. The filtrate thus obtained was diluted with 5 ml of pH 7 phosphate buffer (Riedel-de Haën, Germany) and then 0.01 M of a potassium polyvinyl sulfate solution (KPVS; obtained from SERVA Feinbiochemica, Heidelberg) the excess of cationic reagent was added slowly to the filtrate. The end point of titration was detected by a Phototrode DP660, which was adjusted to 1200 to 1400 mV in deionized water, before such measurement. The load calculation was performed according to the following assessment:
[0208] [00208] For the measurement of ignition loss, the samples of the suspensions of self-bonding pigment material were dried in a microwave at approximately 200 W for about 75 min, so that the samples had a maximum humidity of about 0.5% by weight, based on the total weight of the particulate material. Subsequently, the dried samples were de-agglomerated using an ultra-centrifugal RETSCH mill (type ZM) with 200 µm of filter and rotor having 24 teeth. 3 to 4 g of the sample obtained were weighed in a porcelain crucible and heated in a muffle furnace at about 570 ° C until constant mass. After cooling in a desiccator, the porcelain crucible was weighed with the residue obtained. The values given here are the average of two measurements of samples independently prepared.
[0209] [00209] Ignition loss is an absolute measurement shown as a percentage and calculated according to the following formula:
[0210] [00210] An aliquot of the suspension was diluted with deionized water to a concentration of 10% by weight, based on the total weight of the suspension. The suspension was stirred for 5 minutes. The suspension was centrifuged with a laboratory centrifuge at 2600 g for 15 minutes. The upper water phase was poured and the sedimented cake was dried in a microwave at approximately 200 W for about 75 min, so that the samples have a maximum moisture content of about 0.5% by weight, with based on the total weight of the particulate material. Subsequently, the dried samples were de-agglomerated using an ultra-centrifugal RETSCH mill (type ZM) with 200 µm of filter and rotor having 24 teeth. 3 to 4 g of the samples obtained were weighed in a porcelain crucible and heated in a muffle furnace at about 570 ° C until constant mass. After cooling in a desiccator, the porcelain crucible was weighed with the residue obtained. The values given here are the average of two measurements of samples independently prepared.
[0211] [00211] Ignition loss is an absolute measurement shown as a percentage and calculated according to the following formula:
[0212] [00212] The amount of free polymer can be calculated according to the following formula:
[0213] [00213] It was found that the LOI of the original GCC was 0.6% and this is taken into account by subtracting this 0.6%. Whiteness measurement (R457) and yellowing index
[0214] [00214] Whiteness and yellowing index were determined according to the TAPPI T452 / ISO 247 standard. The brightness was determined according to DIN 54 502 / TAPPI 75. Turbidity
[0215] [00215] Turbidity was measured with the Hach Lange 2100AN IS laboratory turbidity meter and calibration was performed using StabCal turbidity standards (formazine standards) of <0.1, 20, 200, 1000, 4000, and 7500 NTU (units nephelometric turbidity). Chemical oxygen demand
[0216] [00216] The chemical oxygen demand (COD) was measured according to the Lange method (ISO 15705), as described in the document issued by HACH LANGE LTD, entitled "DOC042.52.20023.Nov08". Approximately 2 ml of the liquid phase was added to a small Lange CSB LCK 014 vat, covering a range between 1000 and 10000 mg / l and heated in the nearest small vat for two hours at 148 ° C in a dry thermostat. This suspension was then analyzed according to the Lange method. 2. Examples 1 to 12 Example 1 - GCC with CMC (comparative example)
[0217] [00217] A chemical-free calcium carbonate from Norway, Molde, having a fineness corresponding to a d50 value of 0.8 µm and a d98 value of 5.0 µm, was used as crushed calcium carbonate (GCC ). The specific surface (BET) of the crushed calcium carbonate was 7.5 m2 / g and a loading density was -24.8 µEq / g. The GCC was provided in the form of a filter cake having a solids content of 70.0% by weight.
[0218] [00218] The anionic polymeric binder was a carboxymethyl cellulose (CMC) having a molecular weight of 90000 g / mol (No. 419273, commercially available from Sigma Aldrich, Germany). The intrinsic viscosity of CMC was 327 ml / g, and the degree of substitution (degree of carboxylation) was 0.7. CMC was used in the form of an aqueous solution containing 6% by weight of CMC, based on the total amount of the solution.
[0219] [00219] A slurry with a solid content of 50.0% by weight, based on the total amount of the slurry, was prepared from the GCC filter cake by adding 2.0% by weight of CMC, with based on the total weight of the crushed dry calcium carbonate.
[0220] [00220] The slurry obtained has a Brookfiled viscosity of 237 mPas. The particle size distribution of the pigment particles, measured on a Sedigraph 5120, has a fraction of 88% by weight less than 2 µm, and 61% by weight less than 1 µm.
[0221] [00221] The slurry obtained was dry-ground at room temperature. Wet grinding of the slurry was carried out in a vertical friction mill (Dynomill®, Bachofen, Switzerland) having a volume of 600 cm3 at a speed of 2500 rpm and a flow rate of 500 cm3 / min. A 480 cm3 crushing chamber was filled (80%) with crushing beads having a diameter of 0.6 - 1.0 mm (melt beads consisting of 68% baddeleyite and 32% amorphous silicate). The slurry was passed through the mill four times.
[0222] [00222] The product obtained was analyzed with respect to particle size, specific surface (BET), brightness, electrochemical charge (PET), and LOI. Tables 2 and 3 summarize the properties of the obtained slurry and the pigment particles contained therein. Examples 2 to 8 - GCC with CMC and polyDADMAC (inventive examples)
[0223] [00223] A chemical-free calcium carbonate from Norway, Molde, having a fineness corresponding to a d50 value of 0.8 µm and a d98 value of 5.0 µm was used as crushed calcium carbonate (GCC) . The specific surface (BET) of the crushed calcium carbonate was 7.5 m2 / g and a loading density was -24.8 µEq / g. The GCC was provided in the form of a filter cake having a solids content of 70.0% by weight.
[0224] [00224] The anionic polymeric binder was a carboxymethylcellulose (CMC) having a molecular weight of 90,000 g / mol (No. 419273, commercially available from Sigma Aldrich, Germany). The intrinsic viscosity of CMC was 327 ml / g, and the degree of substitution (degree of carboxylation) was 0.7. CMC was used in the form of an aqueous solution containing 6% by weight of CMC, based on the total amount of the solution.
[0225] [00225] As a cationic polymer, PoliDADMAC (Catiofast BP®, liquid, commercially available from BASF, Germany) was used in the form of a solution containing 50% by weight of PoliDADMAC, based on the total weight of the solution.
[0226] [00226] In a first step, a slurry with a solid content of 50.0% by weight, based on the total amount of the slurry, was prepared from the GCC filter cake by adding 2.0% in weight of the CMC, based on the total amount of the slurry. In a second step, polyDADMAC was added in different amounts, that is, in amounts of 0.50% by weight (Example 2), 1.00% by weight (Examples 3 and 5), 1.25% by weight (Example 6), 1.50% by weight (Example 7), 1.75% by weight (Example 8), and 2.00% by weight (Example 4), based on the total weight of the crushed dry calcium carbonate (see also table 1).
[0227] [00227] Subsequently, the slurry obtained was wet-milled at room temperature. Wet grinding of slurry was carried out in a vertical friction mill (Dynomill®, Bachofen, Switzerland) having a volume of 600 cm3 at a speed of 2500 rpm and a flow rate of 500 cm3 / min. 480 cm3 (80%) of the crushing chamber was filled with crushing beads having a diameter of 0.6 - 1.0 mm (melt beads consisting of 68% baddeleyite and 32% amorphous silicate). The slurry was passed through the mill four times.
[0228] [00228] The products obtained were analyzed with respect to particle size, specific surface (BET), brightness, electrochemical charge (PET), and LOI. Tables 2 and 3 summarize the properties of the obtained slurries and the inventive self-bonding pigment particles contained therein. Examples 9 to 11 - GCC with CMC and cationic starch (inventive examples)
[0229] [00229] A chemical-free calcium carbonate from Norway, Molde, having a fineness corresponding to a d50 value of 0.8 µm and a d98 value of 5.0 µm was used as crushed calcium carbonate (GCC) . The specific surface (BET) of the crushed calcium carbonate was 7.5 m2 / g and a loading density was -24.8 µEq / g. The GCC was provided in the form of a filter cake having a solids content of 70.0% by weight.
[0230] [00230] The anionic polymeric binder was a carboxymethylcellulose (CMC) having a molecular weight of 90000 g / mol (No. 419273, commercially available from Sigma Aldrich, Germany). The intrinsic viscosity of CMC was 327 ml / g, and the degree of substitution (degree of carboxylation) was 0.7. CMC was used as a dry powder.
[0231] [00231] As a cationic polymer, the cationic starch Cargill C * Bond (No. HR05947, commercially available from Cargill Deutschland GmbH, Germany) was used as a dry powder.
[0232] [00232] Pre-mixed solutions of starch and CMC were prepared with different amounts and ratios of cationic starch and CMC, that is, 1.5% by weight of CMC and 0.5% by weight of starch (Example 9), 1.0% by weight of CMC and 1.0% by weight of starch (Example 10), and 0.5% by weight of CMC and 1.5% by weight of starch (Example 11), based on the total weight of crushed dry calcium carbonate (see also table 1). These pre-mixed solutions were produced by dissolving the cationic starch in water and heating the solution to 100 ° C. The starch solution was cooled to room temperature, and the CMC powder was added. The solution was stirred at room temperature for 30 to 60 min until the CMC was dissolved.
[0233] [00233] A slurry with a solid content of 50.0% by weight, based on the total amount of slurry, was prepared from the GCC filter cake by adding a premixed solution of starch and CMC.
[0234] [00234] Subsequently, the slurry obtained was wet-milled at room temperature. Wet grinding of slurry was carried out in a vertical friction mill (Dynomill®, Bachofen, Switzerland) having a volume of 600 cm3 at a speed of 2500 rpm and a flow rate of 500 cm3 / min. 480 cm3 (80%) crushing chamber was filled with crushing beads having a diameter of 0.6 - 1.0 mm (melted melt beads consisting of 68% baddeleyite and 32% amorphous silicate). The slurry was passed through the mill four times.
[0235] [00235] The products obtained were analyzed with respect to particle size, specific surface (BET), brightness, electrochemical charge (PET), and LOI. Tables 2 and 3 summarize the properties of the obtained slurries and the pigment particles containing them. Example 12 - Plaster with CMC and polyDADMAC (inventive example)
[0236] [00236] A plaster of France, Omey, having a fraction of particles finer than 2 µm of 43% by weight, and a fraction of particles finer than 1 µm of 18% by weight was used as crushed calcium carbonate (GCC). GCC was provided as a dry powder.
[0237] [00237] The anionic polymeric binder was a carboxy methylcellulose (CMC), commercially available under the trade name Finnfix 10 from CP Kelko, USA. The intrinsic viscosity of the CMC was 135 ml / g. CMC was used in the form of an aqueous solution containing 3% by weight of CMC, based on the total amount of the solution.
[0238] [00238] As a cationic polymer, PoliDADMAC (Catiofast BP®, liquid, commercially available from BASF, Germany) was used in the form of a solution containing 50% by weight of PoliDADMAC, based on the total weight of the solution.
[0239] [00239] In a first step, in the above CMC solution consisting of 2020 g of water and 64 g of Finnfix 10, 3000 g of plaster were added and the resulting mixture was stirred for 10 minutes. In a second step, poliDADMAC was added in an amount of 1.80% by weight, based on the total weight of the crushed dry calcium carbonate (see also table 1).
[0240] [00240] Subsequently, the slurry obtained was wet-milled at room temperature. Wet grinding of slurry was carried out in a vertical friction mill (Dynomill®, Bachofen, Switzerland) having a volume of 600 cm3 at a speed of 2500 rpm and a flow rate of 500 cm3 / min. 480 cm3 (80%) crushing chamber was filled with crushing beads having a diameter of 0.6 - 1.0 mm (melted melt beads consisting of 68% baddeleyite and 32% amorphous silicate). The slurry was passed through the mill four times.
[0241] [00241] The products obtained were analyzed with respect to particle size, specific surface (BET), brightness, electrochemical charge (PET), and LOI. Tables 2 and 3 summarize the properties of the obtained slurries and the inventive self-bonding pigment particles contained therein.
[0242] [00242] From the measured details, it can be understood that the charge density of the self-bonding pigment particles comprising the cationic polyDADMAC polymer is linearly reduced with an addition of the cationic polymer. A similar trend is observed for self-bonding pigment particles comprising Cargill C * Bond as a cationic polymer.
[0243] [00243] Furthermore, the results show that with the increase in the amount of cationic polymer, the amount of total polymer that is absorbed on the surface of the self-bonding pigment particles increases and the amount of free polymer in the aqueous phase decreases, respectively (see Table 3, last two lines).
[0244] [00244] The measured R457 brightness values for the self-bonding pigment particles produced hardly differ from each other (see Table 3), which means that the presence of the cationic polymer on the self-bonding surface does not have an impact on the optical properties of the pigment particles . 3. Example 13 - Retention studies
[0245] [00245] The self-bonding pigment particles of Comparative Example 1 and inventive examples 3 and 11 were tested as paper fillers in a dynamic retention study using DFS 03 (BTG Mütek GmbH).
[0246] [00246] Thermomechanical pulp (TMP) fibers were used for the retention study. The paste was either diluted in tap water which was treated with 0.057 g / l of a polyacrylic acid homopolymer having a molecular weight of 3500 g / mol and a polydispersity D = 2.5, or with clear filtrate, ie , the water that was used in the paper mill for the dilution of the pulp. 6.00 g / l of fibers were mixed with 6.00 g / l of filter to obtain a paste consistency of the paste / filler mixture of 12.0 g / l as the top box of a papermaking machine. The load was added within 1 min of shaking time for 10 s of shaking at 800 rpm, 10 s of shaking at 1200 rpm, 5 s of shaking at 1000 rpm, and 5 s of shaking at 800 rpm, where after 20 s, Percol PBR 30 special powder (commercially available from BASF, Germany) in the form of 0.2% solution was added as a retention aid. After another 30 s, the valve was opened. The tests were performed with different concentrations of retention aid, that is, with 250 g / t, 500 g / t, 750 g / t, 1000 g / t, 1500 g / t, 2000 g / t, and 3000 g / t. The relative retention as determined by measuring the NTU turbidity of the clear filtrate and the sample filtrates over time:
[0247] [00247] The results of the retention studies are shown in Figure 1 and 2, in which Figure 1 shows the results for the paste that was diluted in tap water and Figure 2 shows the results for the paste that was diluted in clear filtrate . The retention values obtained for the inventive self-bonding pigment particles of Example 3 and 11 are very good and significantly better than those of the comparative charge of Example 1. 4. Example 14 - Test of mechanical strength properties of uncoated wood-free paper containing the inventive pigment particles as filler
[0248] [00248] Eucalyptus pulp (Jarilyptus) refined at 30 ° SR was used as a pulp. The self-bonding pigment particles of Example 4 were tested as paper fillers. In addition, Hydrocarb ® HO ME - 67% was tested as a comparative example. The pigment particle suspension was diluted with water to a concentration of 10% by weight, based on the total amount of the slurry, and de-agglomerated with a high speed agitator (Kinematica, Switzerland).
[0249] [00249] 60 g of paste (dry) was diluted in 10 dm3 of tap water, and then the pigment particle suspension to be tested was added in an amount in order to obtain the desired overall filler content based on in the final paper weight. The obtained suspension was stirred for 30 min. Subsequently 0.06% (based on dry weight) of a polyacrylamide (Polymin 1530, commercially available from BASF, Germany) was added as a retention aid and 78 g / m2 sheets were formed using the Rapid test sheet former -Köthen. Each leaf was dried using the Rapid-Köthen dryer.
[0250] [00250] The load content on the test sheets was determined by burning a quarter of a dry test sheet in a muffle furnace heated to 570 ° C. After the firing was complete, the residue was transferred in a desiccator and left to cool. When the ambient temperature was reached, the weight of the residue was measured and the mass was related to the initially measured weight of a quarter of the dry test sheet. The charge content in the examples is between 18 and 30%.
[0251] [00251] The mechanical resistance properties of the test sheets were distinguished after drying the test sheets by the breaking length according to ISO 1924-2, the traction index according to ISO 1924-2, the absorption of traction energy according to ISO 1924-2, the breakthrough growth work according to ISO 53115, the internal connection (z direction) according to SCAN-P80: 98 / TAPPI T541, flexural stiffness according to ISO 53123-1, and the modulus of elasticity according to ISO 53123-1.
[0252] [00252] Figures 3 to 9 show the mechanical properties of the test sheets tested. The data show that the use of the self-bonding pigment particles of the present invention allows to increase the filling load by about 22% and to about 28%, that is, by about 6%, without affecting the mechanical strength of the paper. In the case of an internal connection (Figure 7), the effect is even more pronounced at a higher load content would be possible. A special highlight is the positive effect of the inventive self-bonding pigment particles on the flexural stiffness (Figure 8) and the modulus of elasticity (Figure 9) of the paper. In particular, good flexural rigidity is an important property in types of wood-free uncoated papers such as copy paper. 5. Example 15 - Test of mechanical strength properties of supercalendered paper (SC) containing the inventive pigment particles as a filler
[0253] [00253] Thermomechanical paste (TMP) 85% and Kraft pine paste (15%) refined at 27 ° SR (Schopper-Riegler) were used for the study with test sheet. The mixture of the thermomechanical paste and the pine kraft paste has 80 ° SR. The self-bonding pigment particles of Example 3 were tested as paper fillers. In addition, the particles of Example 1, Hydrocarb® HO ME - 67%, and Hydrocarb® HO ME - 67%, where 0.8% by weight of cationic starch (Cargill C * Bond, No. HR05947, commercially available from Cargill Deutschland GmbH, Germany) were added to the fiber suspension, based on the total weight of the dry fibers, were tested as a comparative example. The pigment particle suspensions were diluted with water to a concentration of 10% by weight, based on the total amount of the suspension, and de-agglomerated with a high speed agitator (Kinematica, Switzerland).
[0254] [00254] 60 g (dry) of paste mixture were diluted in 10 dm3 of tap water. In a comparative example, 0.8% by weight of cationic starch (Cargill C * Bond, No. HR05947, commercially available from Cargill Deutschland GmbH, Germany), based on the total weight of dry fibers, was added to the fiber suspension and the suspension was stirred for 15 min. Then the pigment particle suspension was added in an amount in order to obtain the desired overall filler content, based on the final paper weight. The suspension was stirred for 30 minutes, and subsequently the special Percol PBR 30 auxiliary retention powder (commercially available from BASF, Germany) was added in amounts given in table 4 below, and 52 g / m2 sheets were formed using the Rapid-Köthen test sheets. Each leaf was dried using the Rapid-Köthen dryer. The sheets were calendered with a Voith calender at 0.95 - 1.05 PPS of roughness.
[0255] [00255] The load content in the test sheets was determined by burning a quarter of the test sheet calendered in a muffle furnace, heated to 570 ° C. After the firing was complete, the residue was transferred in a desiccator and allowed to cool. When the ambient temperature was reached, the weight of the residue was measured and the mass was related to the initially measured weight of the quarter leaf for dry testing. The charge content in the examples was 37 or 42%.
[0256] [00256] The reduced anionic charge of the inventive self-ligating pigment particles reduced the demand for the retention polymer in obtaining the test sheet (see Figure 10). The mechanical properties of the test sheets tested are shown in Figure 11 to 13. All test sheets with the inventive self-bonding pigment particles showed increased sheet traction and improved internal bonding, compared with Hydrocarb® HO ME - 67%, and Hydrocarb ® HO ME - 67% with the addition of 0.8% by weight of cationic starch, based on the total weight of dry fibers. In particular, the use of the pigment particles of Example 3 as a filler leads to an increase in the tensile index and internal bond of about 20%, compared to the Hydrocarb® HO ME filler - 67% (see Figures 11 and 13). 6. Examples 16 to 21
[0257] [00257] A chemical-free calcium carbonate from Norway, Molde, having a fineness corresponding to a d50 value of 0.8 µm and a d98 value of 5.0 µm was used as crushed calcium carbonate (GCC) . The specific surface (BET) of the crushed calcium carbonate was 7.5 m2 / g and a loading density was -24.8 µEq / g. The GCC was provided in the form of a filter cake having a solids content of 70.0% by weight.
[0258] [00258] Different types of carboxymethylcellulose (CMC) having different molecular weights were used as anionic polymeric binder (Finnfix 2 (lower molecular weight), Finnfix 5, Finnfix 10, Finnfix 30, Finnfix 150, and Finnfix 300 (higher molecular weight), commercially available from CP Kelko, USA). The intrinsic viscosity of CMC was 90 to 300 ml / g, and the degree of substitution (degree of carboxylation) was 0.7. CMC was used in the form of an aqueous solution containing 3-6% by weight of CMC, based on the total amount of the solution.
[0259] [00259] As a cationic polymer PoliDADMAC (Catiofast BP®, liquid, commercially available from BASF, Germany) was used in the form of a solution containing 50% by weight of PoliDADMAC, based on the total weight of the solution.
[0260] [00260] In a first step, a slurry with a solid content of 50.0% by weight, based on the total amount of the slurry, was prepared from the GCC filter cake by adding water and 2.0 % by weight of the different CMC types, based on the total amount of dry GCC, ie Finnfix 2 (Example 16), Finnfix 5 (Example 17), Finnfix 10 (Example 18), Finnfix 30 (Example 19), Finnfix 150 (Example 20), and Finnfix 300 (Example 21) (see also table 5 below). In a second step, poliDADMAC was added in an amount of 0.8% by weight, based on the total amount of dry GCC.
[0261] [00261] Subsequently, the slurry obtained was wet-milled at room temperature. Wet grinding of slurry was carried out in a vertical friction mill (Dynomill®, Bachofen, Switzerland) having a volume of 600 cm3 at a speed of 2500 rpm and a flow rate of 500 cm3 / min. 480 cm3 (80%) crushing chamber was filled with crushing beads having a diameter of 0.6 - 1.0 mm (melt beads consisting of 68% baddeleyite and 32% amorphous silicate). If necessary, the solid content was adjusted during crushing to avoid blocking the mill. The grinding was carried out to more than 73 to 77% of the particles having a particle size of less than 1 µm as determined by Sedigraph 5120.
[0262] [00262] The products obtained were analyzed with respect to particle size, specific surface (BET), brightness, electrochemical charge (PET), and LOI. Tables 6 and 7 summarize the properties of the obtained slurries and the pigment particles containing them.
[0263] [00263] From the measured details, it can be understood that the charge density of the self-ligating pigment particles is between -70 and - 80 µEq / g and varies only slightly depending on the molecular weight of the CMC employed. The free polymer in the solution was found to be below 30% for each of Examples 16 to 21. 7. Examples 22 to 26
[0264] [00264] A chemical-free calcium carbonate from Norway, Molde, having a fineness corresponding to a d50 value of 0.8 µm and a d98 value of 5.0 µm was used as crushed calcium carbonate (GCC) . The specific surface (BET) of the crushed calcium carbonate was 7.5 m2 / g and a loading density was -24.8 µEq / g. The GCC was provided in the form of a filter cake having a solids content of 70.0% by weight.
[0265] [00265] The anionic polymeric binder was a carboxymethyl cellulose (CMC) having an intrinsic viscosity of the CMC was 135 ml / g, and the degree of substitution (degree of carboxylation) was 0.7. CMC was used in the form of an aqueous solution containing 6% by weight of CMC, based on the total amount of the solution.
[0266] [00266] As a cationic polymer, PoliDADMAC (Catiofast BP®, liquid, commercially available from BASF, Germany) was used in the form of a solution containing 50% by weight of PoliDADMAC, based on the total weight of the solution.
[0267] [00267] In a first step, a slurry with a solid content of 50.0% by weight, based on the total amount of the slurry, was prepared from the GCC filter cake by adding water and 2.0 % by weight of CMC, based on the total amount of dry GCC. In a second step, polyDADMAC was added in different amounts, that is, in amounts of 0.4% by weight (Example 23), 0.6% by weight (Example 24), 1.0% by weight (Example 25) , and 1.2% by weight (Example 26), based on the total amount of dry GCC. In Example 21, no polyDADMAC was added.
[0268] [00268] Subsequently, the slurry obtained was wet-milled at room temperature. Wet grinding of slurry was carried out in a vertical friction mill (Dynomill®, Bachofen, Switzerland) having a volume of 600 cm3 at a speed of 2500 rpm and a flow rate of 500 cm3 / min. 480 cm3 (80%) crushing chamber was filled with crushing beads having a diameter of 0.6 - 1.0 mm (melted beads consisting of 68% baddeleyite and 32% amorphous silicate). If necessary, the solid content was adjusted during crushing to avoid blocking the mill. The grinding was carried out to more than 73 to 77% of the particles having a particle size of less than 1 µm as determined by Sedigraph 5120.
[0269] [00269] The products obtained were analyzed with respect to particle size, specific surface (BET), brightness, electrochemical charge (PET), and LOI. Tables 9 and 10 summarize the properties of the obtained slurries and the pigment particles containing them.
[0270] [00270] From the measured details, it can be understood that the charge density of the self-bonding pigment particles is linearly reduced with the increase in the amount of cationic polymer. As shown in Figure 14 the amount of free polymer in the solution is also reduced with an increase in the amount of cationic polymer and reaches a level around 15 to 20% of free polymer to an amount of cationic polymer of more than 0.6 % by weight, based on the amount of dry GCC. 8. Example 27 - Retention studies
[0271] [00271] The self-bonding pigment particles of Examples 16 to 26 were tested as paper fillers in a dynamic retention study. In addition, Hydrocarb® HO ME - 67% has been tested as a comparative example.
[0272] [00272] The fibers used for the retention study comprise 85% thermomechanical paste (TMP) and 15% pine kraft paste. The paste was either diluted in tap water which was treated with 0.057 g / l of a sodium polyacrylic acid homopolymer having a molecular weight of 3500 g / mol and a polydispersity D = 2.5, or with clear filtrate, ie , the water that was used in the paper mill for the dilution of the pulp. 5.5 g / l of fibers were mixed with 5.5 g / l of load to obtain a paste consistency of the paste / load mixture of 11.0 g / l as in the top box of the papermaking machine. The load was added within 1 min of shaking time for 10 s of shaking at 800 rpm, 10 s of shaking at 1200 rpm, 5 s of shaking at 1000 rpm, and 5 s of shaking at 800 rpm, where after 20 s, Percol PBR 30 special powder (commercially available from BASF, Germany) in the form of 0.2% solution was added as a retention aid. After an additional 30 s, the valve was opened. The tests were performed without retention aid and different concentrations of retention aid, that is, with 250 g / t, 500 g / t, 750 g / t, 1000 g / t, and 1500 g / t.
[0273] [00273] The relative retention was determined by measuring the NTU turbidity of the clear filtrate and the sample filtrates over time:
[0274] [00274] The results of the retention studies are shown in Figures 15 and 16. The retention values obtained for the self-bonding pigment particles of Example 15 to 25 were, in most cases, below those of the comparative load Hydrocarb® HO ME - 67%, but were still acceptable. It can be found, from Figure 15, that the retention values of the self-ligating particles of Examples 16 to 21 differ depending on the molecular weight of the CMC; the lower the molecular weight of CMC, the better the retention. Figure 16 shows that the retention values of the self-bonding particles of Examples 22 to 26 are increased with the increased amount of cationic polymer. 9. Examples 28 and 29 Example 28 - GCC with CMC (comparative example)
[0275] [00275] A chemical-free calcium carbonate from Norway, Molde, having a fineness corresponding to a d50 value of 0.8 µm and a d98 value of 5.0 µm was used as crushed calcium carbonate (GCC) . The specific surface (BET) of the crushed calcium carbonate was 7.5 m2 / g and a loading density was -24.8 µEq / g. The GCC was provided in the form of a filter cake having a solids content of 83.0% by weight.
[0276] [00276] The anionic polymeric binder was a carboxymethyl cellulose (CMC) having an intrinsic viscosity of the CMC was 135 ml / g, and the degree of substitution (degree of carboxylation) was 0.7. CMC was used in the form of an aqueous solution containing 6% by weight of CMC, based on the total amount of the solution.
[0277] [00277] A pre-mixed solution of CMC was prepared by dissolving 31 g of CMC in 1.4 kg of water under vigorous stirring. After 30 min of stirring, the pre-mixed CMC solution was added to 4.8 kg of the Hydrocarb® HO-ME filter cake. The mixture was dispersed with a dissolver - shaker at 2000 - 4000 rpm.
[0278] [00278] Subsequently, the slurry obtained was crushed wet, at room temperature. Wet grinding of slurry was carried out in a vertical friction mill (Dynomill®, Bachofen, Switzerland) having a volume of 600 cm3 at a speed of 2500 rpm and a flow rate of 500 cm3 / min. 480 cm3 (80%) crushing chamber was filled with crushing beads having a diameter of 0.6 - 1.0 mm (melted melt beads consisting of 68% baddeleyite and 32% amorphous silicate). The grinding was carried out to more than 60% of the particles having a particle size of less than 1 µm as determined by Sedigraph 5120. Example 29 - GCC with CMC and cationic starch (inventive example)
[0279] [00279] As a cationic polymer, a cationic starch (Cargill C * Bond, No. HR05947, commercially available from Cargill Deutschland GmbH, Germany) was used as a dry powder.
[0280] [00280] A premixed solution of cationic starch was prepared by dissolving 16 g of the cationic starch in 2.25 kg of water and heating the obtained suspension to 95 ° C for one hour. Subsequently, the cationic starch solution was mixed with the particles obtained in Example 28.
[0281] [00281] The obtained suspension was de-agglomerated by passing the slurry three times through a homogenizer (Megatron, Kinematica, Switzerland) at room temperature. 10. Example 30 - Test of mechanical strength properties of uncoated wood-free paper containing the inventive pigment particles as filler
[0282] [00282] Eucalyptus pulp (Jarilyptus) refined at 30 ° SR was used as a pulp. The slurry of the self-bonding pigment particles obtained in inventive example 29 was tested as a paper filler. In addition, a Hydrocarb® HO ME - 67% slurry having a solid content of 6% by weight, based on the total amount of the slurry, was tested as a comparative example, as well as the particle slurry obtained in the comparative example 28. In addition, Hydrocarb® HO ME - 67% and Example 28 slurry with cationic starch were prepared, in which the amount of starch was 1.5% by weight, based on the total amount of dry GCC .
[0283] [00283] 60 g of paste (dry) was diluted in 10 dm3 of tap water, and then the pigment particle suspension to be tested was added in an amount in order to obtain the desired overall filler content based on in the final paper weight. The obtained suspension was stirred for 30 min. Subsequently 0.06% (based on dry weight) of a polyacrylamide (Polymin 1530, commercially available from BASF, Germany) was added as a retention aid and 78 g / m2 sheets were formed using the Rapid test sheet former -Köthen. Each leaf was dried using the Rapid-Köthen dryer.
[0284] [00284] The load content in the test sheets, as determined by burning a quarter of a dry test sheet in a muffle furnace heated to 570 ° C. After the firing was complete, the residue was transferred in a desiccator and allowed to cool. When the ambient temperature was reached, the weight of the residue was measured and the mass was related to the initially measured weight of the dry quarter of the test sheet. The charge content in the examples is between 18 and 31%.
[0285] [00285] The mechanical resistance properties of the test sheets were distinguished after drying the test sheets by breaking length according to ISO 1924-2, the traction index according to ISO 1924-2, the absorption of traction energy according to ISO 1924-2, the tear growth work according to ISO 53115, the internal connection (z direction) according to SCAN-P80: 98 / TAPPI T541, flexural stiffness according to ISO 53123-1, and the modulus of elasticity according to ISO 53123-1.
[0286] [00286] Figures 17 to 21 show the mechanical properties of the test sheets tested. Test sheets without cationic starch, that is, test sheets containing Hydrocarb® HO ME - 67% or the particles of Example 28 as filler show the lowest mechanical strength properties. The addition of cationic starch to the paper suspension can slightly improve mechanical strength. However, the inventive use of self-ligating particles as a filler greatly improves the mechanical strength properties of test sheets tested at fill levels around 20%. The data also show that the use of the self-bonding pigment particles of the present invention allows to increase the fill load by about 22% and to about 27 to 28%, that is, by about 5 to 6%, without affecting the resistance mechanics of paper. A special highlight is the positive effect of the inventive self-bonding pigment particles on the flexural stiffness (Figure 20) of the paper. In particular, good flexural stiffness is an important property in types of uncoated paper without wood, such as copy paper.

权利要求:
Claims (20)
[0001]
Process for preparing self-bonding pigment particles, characterized by the fact that it comprises the following steps: a) provide a suspension comprising at least one material containing calcium carbonate, b) providing an anionic polymeric binder, wherein said binder comprises at least one modified polysaccharide, c) providing at least one cationic polymer, in which at least one cationic polymer from step c) is selected from the group comprising polyamines, polyethyleneimines, polyacrylamides, cationic epichlorohydrin resins, polydialldimethylammonium chloride, cationic starch, cationic guar, and mixtures of the same. d) mixing the suspension of step a) and the binder of step b), and e) crush the mixed suspension of step d), wherein the at least one cationic polymer of step c) (i) is mixed in step d) with the suspension from step a) and the binder from step b), and / or (ii) is mixed with the suspension obtained after step e) of grinding, and the mixture obtained is de-agglomerated, wherein the binder from step b) is added in an amount of 0.001 to 20% by weight, based on the total weight of the material containing dry calcium carbonate, the at least one cationic polymer from step c) is added in an amount of 0.001 to 20% by weight, based on the total weight of the material containing dry calcium carbonate, and the grinding step e) is carried out until the fraction of self-bonding pigment particles having a particle size of less than 2 µm is greater than 20% by weight, based on the total weight of the pigment particles, as measured with a Mastersizer 2000.
[0002]
Process according to claim 1, characterized by the fact that, in step d), the suspension of step a) is, in a first step, mixed with the binder from step b), and then, in a second step, it is mixed with at least one cationic polymer from step c).
[0003]
Process according to claim 2, characterized in that, in the first step, a suspension of step a) is mixed with a first part of the binder from step b), the mixture obtained is crushed and then mixed with the part remaining binder from step b).
[0004]
Process according to claim 1, characterized by the fact that, in step d), the binder from step b) is, in a first step, mixed with the cationic polymer from step c), and then, in a second step, is mixed with the suspension of step a).
[0005]
Process according to claim 1, characterized in that, in step d), the suspension of step a) is mixed with the binder from step b) and the cationic polymer from step c) in one step.
[0006]
Process according to any one of the preceding claims, characterized in that the cationic polymer is added in an amount so that the charge density of the self-bonding pigment particles obtained is lower compared to the self-bonding pigment particles not containing the cationic polymer , preferably the cationic polymer is added in an amount so that the charge density of the self-bonding pigment particles obtained is between -100 and - 5 µEq / g, preferably between -80 and -10 µEq / g, and more preferably between - 70 and -15 µEq / g.
[0007]
Process according to any one of the preceding claims, characterized in that the at least one material containing calcium carbonate is selected from calcium carbonate, minerals containing calcium carbonate, mixed calcium carbonate fillers, or mixtures thereof. , preferably the at least one calcium carbonate-containing material is calcium carbonate and, more preferably, crushed calcium carbonate.
[0008]
Process according to any one of the preceding claims, characterized in that the at least one material containing step a) calcium carbonate is provided in the form of particles having a median particle diameter d50 value by weight of 0.1 to 100 µm, preferably from 0.1 to 80 µm, more preferably from 0.5 to 50 µm, and most preferably from 5.0 to 25 µm.
[0009]
Process according to any one of the preceding claims, characterized in that the at least one material containing calcium carbonate is provided in the form of particles having a specific surface area of 0.1 to 200 m2 / g, preferably 1 to 25 m2 / g, more preferably from 2 to 15 m2 / g, and most preferably from 3 to 12 m2 / g.
[0010]
Process according to any one of the preceding claims, characterized in that the suspension of step a) has a solid content of at least 1% by weight, preferably from 1 to 90% by weight, more preferably from 5 to 85% by weight, even more preferably from 20 to 75% by weight, and most preferably from 45 to 65% by weight, based on the total weight of the suspension.
[0011]
Process according to any one of the preceding claims, characterized in that the at least one modified polysaccharide is a carboxymethyl derivative and / or carboxymethyl hydroxypropyl derivative and / or a carboxymethyl hydroxyethyl derivative of a polysaccharide, preferably a carboxymethylcellulose, a starch anionic, an anionic guar, or mixtures thereof.
[0012]
Process according to claim 11, characterized by the fact that at least one modified polysaccharide has a degree of substitution of hydroxyl groups in the range of 0.4 to 2.0, 0.5 to 1.8, 0.6 to 1.6, or 0.7 to 1.5.
[0013]
Process according to any one of the preceding claims, characterized in that the binder of step b) is a carboxymethylcellulose, preferably having an intrinsic viscosity in the range of 5 to 500 ml / g, preferably 10 to 400 ml / g, and more preferably from 20 to 350 ml / g.
[0014]
Process according to any one of the preceding claims, characterized in that the binder of step b) is in the form of a solution or dry material, preferably in the form of a solution having a binder concentration of 1 to 70% by weight, preferably from 2 to 30% by weight, more preferably from 3 to 15% by weight, and most preferably from 4 to 10% by weight, based on the total weight of the solution.
[0015]
Process according to any of the preceding claims, characterized in that the binder from step b) is added in an amount of 0.005 to 15% by weight, more preferably from 0.01 to 10% by weight, and most preferably from 0.05 to 5% by weight, based on the total weight of the material containing dry calcium carbonate.
[0016]
Process according to any one of the preceding claims, characterized in that the at least one cationic polymer of step c) is in the form of a solution or dry material, preferably in the form of an aqueous solution having a concentration of 1 to 70% by weight, preferably from 2 to 55% by weight, more preferably from 5 to 50% by weight, and most preferably from 30 to 50% by weight, based on the total weight of the solution.
[0017]
Process according to any one of the preceding claims, characterized in that the at least one cationic polymer of step c) is added in an amount of 0.005 to 15% by weight, more preferably from 0.01 to 10% by weight, and most preferably 0.05 to 5% by weight or forms 0.5 to 2.5% by weight, based on the total weight of the dry calcium carbonate containing material.
[0018]
Process according to any of the preceding claims, characterized by the fact that the grinding step e) is carried out at a temperature of 5 to 110 ° C, 10 to 100 ° C, 15 to 80 ° C, or 20 ° C to 25 ° C.
[0019]
Process according to any one of the preceding claims, characterized in that the grinding step e) is carried out in a batch or continuous, preferably continuous.
[0020]
Process according to any of the preceding claims, characterized in that the process further comprises a step of concentrating the suspension obtained from self-bonding pigment particles.

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引用文献:

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公开号 | 申请日 | 公开日 | 申请人 | 专利标题

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法律状态:
2018-03-06| B06F| Objections, documents and/or translations needed after an examination request according [chapter 6.6 patent gazette]|

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2018-03-13| B06F| Objections, documents and/or translations needed after an examination request according [chapter 6.6 patent gazette]|

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2018-03-20| B06I| Publication of requirement cancelled [chapter 6.9 patent gazette]|Free format text: ANULADA A PUBLICACAO CODIGO 6.6.1 NA RPI NO 2462 DE 13/03/2018 POR TER SIDO INDEVIDA. |

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2021-03-02| B09A| Decision: intention to grant [chapter 9.1 patent gazette]|

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2021-03-23| B16A| Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 29/04/2013, OBSERVADAS AS CONDICOES LEGAIS. |

优先权:

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申请号 | 申请日 | 专利标题

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EP12167683.7A|EP2662419B1|2012-05-11|2012-05-11|Charge controlled PHCH|

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EP12167683.7|2012-05-11|

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US201261648639P| true| 2012-05-18|2012-05-18|

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US61/648,639|2012-05-18|

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PCT/EP2013/058937|WO2013167420A1|2012-05-11|2013-04-29|Charge controlled phch|

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