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    • 专利摘要:
    METHOD AND CONTROL SYSTEM OF AN IGNITION SYSTEM. The present invention is related to a method for monitoring an ignition system, in which the ignition system comprises a charge coil (Ll) for charging the ignition system, a primary coil (L4) and a secondary coil (L5) , said primary and secondary coils L4, L5) being arranged to generate a voltage for spark generation, and a control unit (Ml), characterized by the fact that it comprises the steps of: (a) providing a separate coil (L3), adjacent to at least one of the load coils (Ll), primary coil (L4) and secondary coil (L5); (b) use the control unit (Ml) to monitor a magnetic flux in the separate coil (L3); and (c) using the information related to said magnetic flux as an access to control at least one property of an ignition system operation. The invention also relates to a control system for an ignition system.
    公开号:BR112012010339B1
    申请号:R112012010339-3
    申请日:2010-11-03
    公开日:2020-11-03
    发明作者:Juppo Ari；Stenbacka Ulf
    申请人:Kemira Oyj；
    IPC主号:
    专利说明:

    Field of the Invention
    [001] The present invention relates to a process for the production of paper and cardboard, in which a cationic polymer is used as a retention system and a nanocellulose substance as a microparticle. Background of the Invention
    [002] Currently, the use of microparticles in the paper production retention system, particularly in the production of fine paper, is quite common, whose objective is to further improve the efficiency of the production process. The advantages of introducing microparticles include improved retention, more efficient dehydration, and better training. The most effective microparticles in use are microparticles based on colloidal silica of various types, solid or in the form of sol, and expandable natural materials, such as bentonite, which belongs to the smectite clays group. Instead, or in addition, a microparticulate compound can be used as an auxiliary retention agent in the retention system polymers, which can be anionic, cationic or nonionic and which are characterized by a high molecular weight. The problem involving these compounds, typically, is excessive flocculation, which deteriorates the optical properties of paper.
    [003] Bentonite was used as an auxiliary retention agent in the production of paper, together with a cationic polymer, as described in U.S. Patent No. 4,753,710. In the process according to that patent, a cationic polymer, preferably polyethyleneimine, a polyamine and epichlorohydrin product, a polymer of diallyl dimethylammonium chloride or a polymer of acrylic monomers, were added to a cellulosic aqueous suspension before the last one. shear stage, and bentonite was added after that shear stage. Retention improvement, dehydration, drying and tissue formation properties were thus obtained. In the microparticle system according to this process, bentonite, available under the trade name HYDROCOL, is used.
    [004] The use of silicate microparticles together with a cationic polymer in a retention system is described in U.S. Patent No. 5,194,120. The prevalent cation in amorphous synthetic metal silicate was magnesium (Mg) and the polymer was preferably a derivative of ternary or quaternary amine from polyacrylamide, its weight ratio being between 0.03: 1 and 30: 1. By the present method, the retention, dehydration and formation properties have been improved through the use of smaller amounts of auxiliary retention agents than before and, thus, the costs were correspondingly lower.
    [005] Patent document WO 01/40577 discloses a method of producing paper or cardboard, in which auxiliary retention agents are added to the raw material stream. Improved retention and more effective dehydration are achieved by adding a cationic polymer solution to the stream of raw material and a mixture of suspension-shaped microparticles, composed of an expandable clay from the smectite group, for example, bentonite , and a colloidal synthetic metal silicate, in which the prevalent cation is magnesium.
    [006] The most commonly used microparticles are inorganic materials, especially several minerals. These minerals increase the ash content of the paper produced.
    [007] US Patent No. 4,483,743 discloses a process for the manufacture of microfibrillated cellulose (MFC), by passing a liquid suspension of cellulose through a high pressure homogenizer, having a small diameter hole, in which the suspension is subjected to a pressure drop of at least 3,000 psig (20,670 kPa) and a high shear action, followed by a high impact deceleration speed, with the passage of said suspension through the orifice, until the cellulose suspension becomes substantially stable. The produced MFC has a water retention value above 280%. MFC can be used with paper products and non-woven sheets to improve its strength. The MFC produced by this type of process typically has a width of about 25-100 nm, while the length is much greater.
    [008] U.S. Patent No. 4,952,278 discloses a paper structure having high opacity and improved tensile strength, obtained by incorporating expanded cellulose fibers and an opacifying mineral pigment, such as titanium dioxide. The expanded cellulosic fiber can be microfibrillated cellulose, as described in the patent mentioned above. The expanded cellulosic fibers are added in an amount of 1% to 25%, preferably 5% to 10%, based on the dry weight of the paper structure that has been rendered opaque.
    [009] Patent document WO 2007/091942 Al discloses an improved method for manufacturing microfibrillated cellulose. The disclosed method is said to solve the problems related to clogging that occurs in high pressure homogenizers, and to high energy consumption. According to this document, microfibrillated cellulose is manufactured by refining a pulp containing hemicelluloses, preferably a sulfite pulp, and treating the pulp with a decomposition enzyme, followed by homogenization of the pulp. The enzyme is a cellulase, preferably an endoglucanase type cellulase, more preferably, it is a single component endoglucanase. The pulp can be refined before or after the enzyme treatment, or else, before and after this treatment. The microfibrillated cellulose obtained can be used in food products, cosmetics, pharmaceuticals, paper products, composite materials, coatings or in rheology modifiers (for example, drilling muds).
    [0010] Another type of microfibrillated cellulose is described by Wãgberg Lars et al. , Langmuir, 2008, Vol. 24, 2008, pages 784-795. This microfibrillated cellulose was prepared by homogenization under high pressure of carboxymethylated cellulose fibers. The fibers consisted of softwood dissolving pulp fibers. The MFC produced, typically, had a width of about 5-14 nm and a length that can be greater than 1 pm.
    [0011] Other methods of chemical pretreatment are also known, such as a pretreatment by oxidation of pulp fibers, described by Saito et al., In the publication Biomacromolecules, Vol. 8, No. 8, 2007, pages 2485-2491. The pulp fibers are oxidized through a system mediated by the radical 2,2,6,6-tetramethylpiperidine-1-oxyl (TEMPO), followed by mechanical treatment. This pretreatment by oxidation converts the primary hydroxyl groups of celluloses into carboxylate groups. The nanofibers produced typically have a width of about 3-4 nm and a length of some pm.
    [0012] One of the purposes of the present invention is to provide an organic substance that can act as a microparticle, which results in an improvement in retention, compared to mineral microparticles, and that is made of a renewable material. Summary of the Invention
    [0013] According to the present invention, it has been discovered that nanocellulose can be used as a substance that can act as a microparticle in a retention system, together with a water-soluble cationic polymer, to improve total retention and retention loading material during the production of paper or cardboard. In addition, it was discovered that in addition to improving retention, nanocellulose also improves the drainage of raw materials for papermaking, in the paper or cardboard production process.
    [0014] According to the observations of the present inventors, when nanocellulose is used together with cationic polyacrylamide, it acts as an effective microparticulate substance in the retention system. In comparison, a retention system comprising cationic polyacrylamide and bentonite as an inorganic microparticle is not as effective. Detailed Description of the Invention
    [0015] Thus, according to a first aspect of the present invention, a process for the production of paper or cardboard is provided, comprising: adding a retention system to a stream of raw material that is admitted into the input box of a machine of paper; - direct the stream of raw material to a screen system; - dehydrate the raw material stream in the screen system to form a paper tissue; and - drying the paper tissue; where the retention system comprises a cationic polymer soluble in water and nanocellulose acting as a microparticle, where the nanocellulose is added as an active substance in an amount of less than 1%, based on the weight of dry solids of the raw material.
    [0016] Nanocellulose is preferably added as an active substance in an amount between 0.02 and 0.8%, preferably between 0.05 and 0.7%, more preferably between 0.1 and 0.5%, with based on the weight of dry solids of the raw material.
    [0017] The nanocellulose can be added in the form of an aqueous suspension or gel, comprising at most 5%, preferably from 0.1 to 4%, more preferably, from 0.3 to 3% by weight of solids.
    [0018] The term nanocellulose as used in the present description includes microfibrillated / microfibrillary cellulose and nanofibrillated / nanofibrillary cellulose of the types described, for example, in the aforementioned publications. The basic idea that underlies the implementation of nanocellulose was to simply slide the cell wall and release the microfibrils, which constitute the main building block of wood fibers. Nanocelluloses are types of materials in the form of gel, even in very low concentrations. The width and length of the nanocellulose fibers vary, depending on the specific manufacturing process. A typical width of nanocellulose is about 3 to about 100 nm, preferably about 10 to about 30 nm, and a typical length is about 100 nm to about 2 pm, preferably about 100 to 100m.
    [0019] Nanocellulose can be produced from cellulose pulp or cellulose pulp previously hydrolyzed, including sulfite pulp and Kraft pulp, through multiple shear, as described in US Patent No. 4,483,743, or through enzymatic hydrolysis combined with shear, as described in the patent document WO 2007/091942, or through pretreatment or chemical modification of the cellulose pulp, with subsequent submission to mechanical shear, as described by Wágberg Lars et al. , Langmuir, 2008, Vol. 24, pages 784-795, and by Saito et al., Biomacromolecules, Vol. 8, No. 8, 2007, pages 2485-2491.
    [0020] As explained above, there are several types of nanocellulose, depending on the manufacturing process. A preferred nanocellulose is of a type produced from cellulose pulp, through enzymatic treatment, followed by homogenization in a high pressure homogenizer. The enzyme in the enzyme treatment preferably comprises a cellulase, such as endoglucanase. The high pressure homogenizer preferably comprises "z" shaped chambers and the pulp is passed several times, preferably at least three times through the chambers.
    [0021] Another preferred nanocellulose is the type that is produced from cellulose pulp, through chemical pretreatment, followed by homogenization in a high pressure fluidization / homogenizer device. Several chemical modifications are known in the art. A preferred chemical pretreatment comprises the carboxymethylation of cellulose fibers. The pulp can be sulfite pulp or Kraft pulp. Also, dissolving pulps, such as sulfite dissolving pulps having a low hemicellulose content, can be used. The high pressure homogenizer preferably comprises "z" shaped chambers and the pulp is passed through the chambers at least once.
    [0022] Suitable pulps that can be used for the production of nanocellulose include all types of wood-based chemical pulps, such as sulfite, sulfate and soda pulps, targeted, semi-targeted, and non-targeted. Also, dissolving pulps having a low content, typically below 5% hemicellulose, can be used.
    [0023] The components of the retention system can be added simultaneously or sequentially.
    [0024] According to a preferred embodiment, the components of the retention system are added sequentially.
    [0025] Preferably, the sequential addition comprises the addition of water-soluble cationic polymer, which will provide the formation of flakes, followed by the submission of the raw material to shear forces so that the flakes are broken, and then, the addition of nanocellulose. The time between the addition of the water-soluble cationic polymer and the nanocellulose, preferably, is at most 60 seconds, more preferably, between 0.5 and 20 seconds.
    [0026] The cationic polymer used in the invention can be advantageously produced by copolymerizing acrylamide with a cationic monomer, or methacrylamide with a cationic monomer. The molecular weight of the cationic polymer is preferably 500,000, and it is added as an active substance to the raw material, preferably in an amount of at least 0.02%, more preferably, 0.03-0.05%, with based on the weight of dry solids of the raw material.
    [0027] The cationic polymer used in the invention can be any copolymer of acrylamide and / or methacrylamide, prepared using at least one of the comonomers of a cationically charged monomer or a cationically chargeable monomer. Such monomers include methacryloyl-oxyethyltrimethyl ammonium chloride, acryloyl-oxyethyltrimethyl ammonium chloride, 3- (methacrylamido) propyltrimethyl ammonium chloride, 3- (acrylamido) propyltrimethyl ammonium chloride, dimethylethylmethyl ammonium chloride, acrylate, methyl ammonium chloride, acrylate dimethylaminopropylacrylamide, dimethylaminopropylmethacrylamide, or a similar monomer. The polymer may also contain monomers other than acrylamide, methacrylamide or some cationic or cationable monomer.
    [0028] The cationic polymer can also be a polymer that has been treated after becoming cationic, for example, a polymer prepared from polyacrylamide or polymethacrylamide, using Hofmann or Mannich reactions.
    [0029] The cationic polymer can be prepared by conventional methods of polymerization by radical initiation, and as a product it can be presented as a dry powder or an emulsion of a polymer solution in an organic medium.
    [0030] Before dosing, preferably a polymer solution is prepared at a concentration of 0.05-0.5%, preferably 0.1-0.3%, the solution of which can be further diluted before the in order to ensure an optimal mixture.
    [0031] The method according to the invention was observed to be robust with respect to several types of tests, types of pulps and fillers. The raw material and its initial pulp may, for example, comprise a conventional chemical pulp (cellulose), chemomechanical pulp or mechanical pulp, or other conventional raw materials used in the manufacture of paper, such as, for example, recycled fiber. The filler material, which can be, for example, ground or precipitated calcium carbonate, kaolin, calcined kaolin, talc, titanium dioxide, plaster or a synthetic inorganic or organic filler, however, preferably, is calcium carbonate, being incorporated into the pulp by a conventional method, before adding the cationic polymer. In addition, additives commonly used in paper production can be introduced into the raw material. The process according to the invention can be used in any conventional paper or cardboard manufacturing device.
    [0032] In a second aspect, the present invention refers to the use of nanocellulose as a material that acts as a microparticle, to improve the retention of papermaking raw materials, during the production of paper or cardboard, in which the nanocellulose is used as an active substance in an amount of less than 1%, based on the weight of dry solids in the papermaking raw material. At the same time, the drainage of the papermaking raw material in the production of paper or cardboard will also be improved.
    [0033] Nanocellulose is preferably used as an active substance in an amount between 0.02 and 0.8%, preferably between 0.05 and 0.7%, more preferably between 0.1 and 0.5%, based on in the weight of dry solids of the raw material.
    [0034] Nanocellulose is preferably used in conjunction with an auxiliary retention agent, which comprises a water-soluble cationic polymer, as defined above.
    [0035] It is preferred to use the nanocellulose sequentially with the cationic polymer, preferably, and in such a way, that the nanocellulose is added after the cationic polymer. However, it is also possible to use nanocellulose and the cationic polymer simultaneously.
    [0036] By using the nanocellulose microparticle according to the present invention, an amazingly satisfactory retention was obtained. When the nanocellulose microparticulate organic substance of the present invention is used as an auxiliary retention agent, the ash retention (filler material) can be 5 to 15 percentage units higher, compared to bentonite at the same dosage levels. . Satisfactory loading material retention is especially important, as the loading material forms the main part of the raw material fraction that is difficult to retain in the screen unit.
    [0037] With the process of the present invention, retention can be improved compared to previous known processes and, at the same time, if desired, the amount of the required auxiliary retention agent can be reduced and, in addition, the total load of ash can be decreased compared to previous known processes using minerals.
    [0038] The invention and its preferred embodiments are described below with the help of several examples; however, the purpose of the examples is not to limit the scope of the invention. In the present description, percentage values refer to the percentage by weight, unless otherwise specified. Examples Example 1
    [0039] Retention tests were performed using a Dynamic Drain Jar (DDJ) device. The raw material used was collected from a fine paper production machine. The raw material sample was taken from the machine box. The filler material was added to the raw material and the filler material content in the raw material was 45% of the dry solids content of the raw material. The filler material used was precipitated calcium carbonate. To perform the tests, the raw material was diluted with white liquor to a consistency of 8.0 g / L. Then, starch was added to the raw material, before the retention test started. The following stepwise procedure was used in the tests: 1. At time 0 s, with the mixing speed of 1500 rpm, the raw material sample was poured into a reaction vessel; 2. After 15 s, the polymer was dosed in the raw material; 3. With the time of 30 s, the microparticle or substance with microparticle function was dosed in the raw material; 4. After 45 s, a filtered sample was taken.
    Tabela 2 - % de Retenção de Cinzas na Primeira Passagem Medido com Drenagem Dinâmica em Aparelho Jar (DDJ) Dosagem de PAM (1) - 300 g/ton Dosagem de PAM (2) – 600 g/ton Dosagem de Bentonita (1) – 500 g/ton Dosagem de Bentonita (2) – 1500 g/ton Dosagem de Bentonita (3) – 3000 g/ton Dosagem de Nanocelulose (1) – 500 g/ton Dosagem de Nanocelulose (2) – 1500 g/ton Dosagem de Nanocelulose (3) – 3000 g/ton.[0040] The screen used was a DDJ screen of 200 mesh, model 125P. The polymer was a cationic polyacrylamide (PAM) from Kemira, which is a copolymer of acrylamide and acryloyloxyethyltrimethyl ammonium chloride, with a charge of approximately 1 meq / g and a molecular weight of approximately 7 mg / mol. The bentonite microparticle used was Altonit SF, from Kemira. The other component with microparticle function was a nanocellulose produced by homogenization under high pressure of carboxymethylated cellulose fibers in a homogenizer. The nanocellulose was diluted from 2% to 0.5%, in the same homogenizer. Dosages are indicated as the amount of material dosed as an active substance by weight of dry solids of the raw material, the unit being g / ton. The results of the retention are shown in Tables 1 and 2. Table 1 -% Retention in the First Passage Measured with Dynamic Drainage in Jar Apparatus (DDJ) Table 2 -% of Ash Retention in the First Passage Measured with Dynamic Drainage in Jar Apparatus (DDJ) Dosage of PAM (1) - 300 g / ton Dosage of PAM (2) - 600 g / ton Dosage of Bentonite (1) - 500 g / ton Dosage of Bentonite (2) - 1500 g / ton Dosage of Bentonite (3) - 3000 g / ton Nanocellulose dosage (1) - 500 g / ton Nanocellulose dosage (2) - 1500 g / ton Nanocellulose dosage (3) - 3000 g / ton.
    [0041] In all dosages of the depolycrylamide polymer (PAM), it can be seen that the nanocellulose microparticle type material works better than bentonite, with the use of the same dosages.
    [0042] This example clearly shows that the retention results with the use of nanocellulose acting as microparticles are substantially better than with the use of bentonite. Example 2
    [0043] Drainage tests were performed using a Dynamic Filtration System (DFS-03). The raw material used was collected from a fine paper production machine. The raw material sample was taken from the machine box. The filler material was added to the raw material and the filler material content in the raw material was 45% of the dry solids content of the raw material. The loading material used was precipitated calcium carbonate. To perform the tests, the raw material was diluted with white liquor to a consistency of 8.0 g / L. Then, starch was added to the raw material, before the start of the drainage test. The following step-by-step procedure was used in the tests: 1. At time 0 s, with a mixing speed of 800 rpm, the raw material sample was poured into a reaction vessel; 2. After 15 s, the polymer was dosed in the raw material; 3. With the time of 30 s, the microparticle or substance with microparticle function was dosed in the raw material; 4. After 45 s, dehydration was started and measured for 60 seconds.
    Dosagem do Polímero - 600 g/ton Dosagem Bentonita (1) - 500 g/ton Dosagem Bentonita (2) - 1500 g/ton Dosagem Bentonita (3) - 3000 g/ton Dosagem Nanocelulose (1) - 500 g/ton Dosagem Nanocelulose (2) - 1500 g/ton Dosagem Nanocelulose (3) - 3000 g/ton[0044] The screen used was a 60 mesh DFS screen. The polymer was a cationic polyacrylamide (PAM) from Kemira, which is a copolymer of acrylamide and acryloyloxyethyltrimethyl ammonium chloride, with a charge of approximately 1 meq / g and a molecular weight approximately 7 mg / mol. The bentonite microparticle used was Altonit SF, from Kemira. The other component with a microparticle function was the same nanocellulose as in Example 1. Dosages are indicated as the amount of material dosed as an active substance by weight of dry solids of the raw material, the unit being g / ton. The drainage results are shown in Table 3. Table 3 Dehydration time (in seconds) for a 700 mL filtrate, Measured with DFS-03. Polymer dosage - 600 g / ton Bentonite dosage (1) - 500 g / ton Bentonite dosage (2) - 1500 g / ton Bentonite dosage (3) - 3000 g / ton Nanocellulose dosage (1) - 500 g / ton Nanocellulose dosage (2) - 1500 g / ton Dosage Nanocellulose (3) - 3000 g / ton
    [0045] It can be seen that nanocellulose acting as a microparticulate material provides faster dehydration than bentonite.
    [0046] This example clearly shows that the results of dehydration with the use of nanocellulose acting as microparticles are substantially better than with the use of bentonite. Example 3
    [0047] Retention was also measured using a Retention Process Analyzer (RPA) device. RPA is similar to DDJ, but it also measures the stability of flakes in the filtrate with turbidity measurements. The raw material used was collected from a fine paper production machine. The raw material sample was taken from the machine box. The filler material was added to the raw material and the filler material content in the raw material was 45% of the dry solids content of the raw material. The loading material used was precipitated calcium carbonate. To perform the tests, the raw material was diluted with white liquor to a consistency of 8.0 g / L. Then, starch was added to the raw material, before the start of the drainage test. The following stepwise procedure was used in the tests: 1. The raw material sample was poured into a reaction vessel, with a mixing speed of 1000 rpm, and the filtrate was passed through a screen, with subsequent measurement of turbidity. After that, the filtrate was added back to the reaction vessel (circulation); 2. After 50 s, the polymer was dosed in the raw material; 3. With the time of 65 s, the microparticle or substance with the function of microparticle was dosed in the raw material; 4. The stability of the flakes was measured up to 120 seconds.
    Teste 0 0,96 0, 96 0, 96 0,96 0,96 0, 96 Dosagem do Polimero - 600 g/ton Dosagem Bentonita (1) - 500 g/ton Dosagem Bentonita (2) - 1500 g/ton Dosagem Bentonita (3) - 3000 g/ton Dosagem Nanocelulose (1) - 500 g/ton Dosagem Nanocelulose (2) - 1500 g/ton Dosagem Nanocelulose (3) - 3000 g/ton.[0048] The screen used was a DDJ screen of 200 mesh, model 125P. The polymer was a cationic polyacrylamide (PAM) from Kemira, which is a copolymer of acrylamide and acryloyloxyethyltrimethyl ammonium chloride, with a charge of approximately 1 meq / g and a molecular weight of approximately 7 mg / mol. The bentonite microparticle used was Altonit SF, from Kemira. The other microparticulate component was the same nanocellulose as in Example 1. Dosages are indicated as the amount of material dosed as an active substance by weight of dry solids of the raw material, the unit being g / ton. The retention results are shown in Table 4, shown below. Table 4 - 1 of the Relative Retention Value Measured by RPA Test 0 0.96 0, 96 0, 96 0.96 0.96 0, 96 Polymer dosage - 600 g / ton Bentonite dosage (1) - 500 g / ton Bentonite dosage (2) - 1500 g / ton Bentonite dosage (3) - 3000 g / ton Nanocellulose dosage (1) - 500 g / ton Nanocellulose dosage (2) - 1500 g / ton Nanocellulose dosage (3) - 3000 g / ton.
    [0049] It can be seen that nanocellulose acting as a microparticulate material provides a relative retention value as satisfactory as bentonite. dehydration faster than bentonite. This means that some types of flakes are formed with both nanocellulose and bentonite.
    权利要求:
    Claims (9)
    [0001]
    1. Process for the production of paper or cardboard, comprising: - adding a retention system to a stream of raw material that is admitted into the inbox of a paper machine; - direct the stream of raw material to a screen system; dehydrate the stream of raw material in the screen system to form a paper tissue; and - drying the paper tissue; characterized by the fact that the retention system comprises a water-soluble cationic polymer, which comprises an acrylamide or methacrylamide copolymer and a cationic monomer, the molecular weight of the cationic polymer being at least 500,000, and - nanocellulose acting as a microparticle, where the nanocellulose is added as an active substance in an amount of less than 1%, based on the weight of dry solids of the raw material, in which the components of the retention system are added sequentially, and in which the sequential addition comprises adding the cationic polymer soluble in water to form flakes, followed by submission of the raw material to shear forces to break the flakes and then add the nanocellulose.
    [0002]
    2. Process according to claim 1, characterized by the fact that the nanocellulose is added as an active substance in an amount between 0.02 and 0.8%, preferably between 0.05 and 0.7%, more preferably , between 0.1 and 0.5%, based on the weight of dry solids of the raw material.
    [0003]
    Process according to claim 1 or 2, characterized in that the nanocellulose is added in the form of an aqueous suspension or gel, comprising a maximum of 5%, preferably from 0.1 to 4%, more preferably, 0.3 to 3% by weight of solids.
    [0004]
    4. Process according to any one of the preceding claims, characterized by the fact that nanocellulose is produced from cellulose pulp, through enzymatic treatment followed by homogenization in a high pressure homogenizer, in which the enzyme in the enzymatic treatment comprises preferably, a cellulase, such as endoglucanase.
    [0005]
    5. Process according to any one of claims 1 to 3, characterized by the fact that nanocellulose is produced from cellulose pulp, through chemical pretreatment followed by homogenization in a high pressure fluidization device, and in which the Chemical pretreatment preferably comprises fiber carboxymethylation.
    [0006]
    6. Process according to claim 1, characterized by the fact that the time between the addition of the water-soluble cationic polymer and the nanocellulose is at most 60 seconds, preferably between 0.5 and 20 seconds.
    [0007]
    7. Process according to any one of the preceding claims, characterized by the fact that the cationic polymer is added as an active substance in an amount of at least 0.02%, preferably between 0.03 and 0.05%, with based on the weight of dry solids of the raw material.
    [0008]
    8. Process according to any one of the preceding claims, characterized by the fact that the raw material contains chemical pulp, chemomechanical pulp, mechanical pulp or recycled fiber, or various combinations thereof.
    [0009]
    Process according to any one of the preceding claims, characterized in that the raw material further comprises a filler, such as ground or precipitated calcium carbonate, kaolin, calcined kaolin, talc, titanium dioxide, plaster or an inorganic or organic synthetic filler, and additives commonly used in paper production.
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    引用文献:
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    法律状态:
    2018-04-10| B06F| Objections, documents and/or translations needed after an examination request according art. 34 industrial property law|
    2019-02-12| B06T| Formal requirements before examination|
    2019-12-10| B07A| Technical examination (opinion): publication of technical examination (opinion)|
    2020-04-07| B09A| Decision: intention to grant|
    2020-11-03| B16A| Patent or certificate of addition of invention granted|Free format text: PRAZO DE VALIDADE: 10 (DEZ) ANOS CONTADOS A PARTIR DE 03/11/2020, OBSERVADAS AS CONDICOES LEGAIS. |
    优先权:
    申请号 | 申请日 | 专利标题
    US25790509P| true| 2009-11-04|2009-11-04|
    EP09174967.1|2009-11-04|
    EP09174967.1A|EP2319984B1|2009-11-04|2009-11-04|Process for production of paper|
    US61/257,905|2009-11-04|
    PCT/FI2010/050887|WO2011055017A1|2009-11-04|2010-11-03|Process for production of paper|
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