WO2012133088A1 - 印刷用塗工紙及びその製造方法 - Google Patents
印刷用塗工紙及びその製造方法 Download PDFInfo
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- WO2012133088A1 WO2012133088A1 PCT/JP2012/057287 JP2012057287W WO2012133088A1 WO 2012133088 A1 WO2012133088 A1 WO 2012133088A1 JP 2012057287 W JP2012057287 W JP 2012057287W WO 2012133088 A1 WO2012133088 A1 WO 2012133088A1
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- Prior art keywords
- coating
- paper
- base paper
- whiteness
- coating liquid
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Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H5/00—Special paper or cardboard not otherwise provided for
- D21H5/0005—Processes or apparatus specially adapted for applying liquids or other fluent materials to finished paper or board, e.g. impregnating, coating
- D21H5/0042—Processes or apparatus specially adapted for applying liquids or other fluent materials to finished paper or board, e.g. impregnating, coating by pouring or allowing to flow in a continuous stream onto the surface, the entire stream being carried away by the paper
- D21H5/0045—Falling curtain method
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H19/00—Coated paper; Coating material
- D21H19/66—Coatings characterised by a special visual effect, e.g. patterned, textured
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H19/00—Coated paper; Coating material
- D21H19/36—Coatings with pigments
- D21H19/38—Coatings with pigments characterised by the pigments
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H19/00—Coated paper; Coating material
- D21H19/36—Coatings with pigments
- D21H19/38—Coatings with pigments characterised by the pigments
- D21H19/385—Oxides, hydroxides or carbonates
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H19/00—Coated paper; Coating material
- D21H19/72—Coated paper characterised by the paper substrate
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
- D21H21/28—Colorants ; Pigments or opacifying agents
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
- D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
- D21H23/22—Addition to the formed paper
- D21H23/46—Pouring or allowing the fluid to flow in a continuous stream on to the surface, the entire stream being carried away by the paper
- D21H23/48—Curtain coaters
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H11/00—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
- D21H11/08—Mechanical or thermomechanical pulp
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H11/00—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
- D21H11/14—Secondary fibres
Definitions
- the present invention relates to a coated paper for printing and a method for producing the same.
- the present invention relates to a technique for efficiently producing a coated paper for matte printing that has both low opacity and high opacity and whiteness and little whiteness unevenness.
- the white unevenness is defined as a standard deviation of whiteness in a minute area. Even if the whiteness is high, if the white unevenness is inferior, the surface feel is poor, and the unevenness is further emphasized particularly in the halftone dot portion of the printed material, so that the value as the printed material is inferior.
- White unevenness is particularly noticeable when the difference between the whiteness of the base paper and the whiteness of the coating layer is large. For this reason, in order to reduce whiteness unevenness, the whiteness of the base paper has been increased to some extent and the difference between the whiteness of the base paper and the whiteness of the coating layer has been reduced. The opacity has fallen.
- An object of the present invention is to provide a technology for producing a coated paper for matte printing having a high opacity, a whiteness, and a good white unevenness while having a low basis weight with a good operability.
- the present inventors have applied a coating liquid on a base paper with low whiteness by a curtain coating method, thereby achieving high opacity while having a low basis weight.
- the present inventors have found that a coated paper for matte printing having whiteness and good whiteness unevenness can be obtained with good operability, and completed the present invention.
- the present invention includes the following inventions.
- a method for producing a coated paper for matte printing having a basis weight of 60 to 90 g / m 2 , a whiteness of 75% or more, and an opacity of 95% or more, comprising waste paper pulp and / or mechanical pulp comprising curtain coating a coating liquid containing calcium carbonate on a base paper having a whiteness of 45 to 70%, which is made from raw pulp containing 50% or more in total.
- the method according to (1), wherein the coating amount per side is 12 to 30 g / m 2 .
- the average particle size (D50) is 0.3 to 0.8 ⁇ m, and the particle size (D75) at 75 cumulative mass% and the particle size at 25 cumulative mass% of the particle size distribution curve by the sedimentation method.
- the method according to (1) or (2), wherein spindle-shaped light calcium carbonate having a ratio (D75 / D25) of (D25) of 1.5 or more and less than 3.5 is used.
- a coating speed of the curtain coating is 800 m / min or more.
- the coating solution includes a viscosity improver that is a W / O emulsion in which an aqueous solution of a polycarboxylic acid copolymer having a weight average molecular weight of 4 million to 50 million is dispersed in an organic solvent.
- a viscosity improver that is a W / O emulsion in which an aqueous solution of a polycarboxylic acid copolymer having a weight average molecular weight of 4 million to 50 million is dispersed in an organic solvent.
- a matte printing coated paper that has both low opacity and high opacity and whiteness, which are usually difficult to achieve, and has little whiteness unevenness, is a base paper with low whiteness. Can be obtained with good operability.
- the printing coated paper of the present invention is a curtain coating of a pigment coating solution containing calcium carbonate as a white pigment on a base paper having a low whiteness and containing a large amount of waste paper pulp and / or mechanical pulp. According to the present invention, whiteness and opacity can be improved at the same time, and a matte printing coated paper with low white weight and little white unevenness can be efficiently produced.
- Base Paper In the present invention, a base paper having a whiteness of 45 to 70% is used, which is made from raw pulp containing a total of 50% or more of waste paper pulp and / or mechanical pulp. Since the base paper reflects the whiteness of the pulp that is normally used, for example, the whiteness of the pulp used may be set to 45% to 70%.
- the base paper used in the present invention uses waste paper pulp and / or mechanical pulp in total of 50% or more as raw material pulp.
- the opacity of the obtained coated paper for printing can be greatly improved. The reason for this is not clear, but because waste paper pulp has low whiteness, light absorption is high, and mechanical pulp has low density when made into paper. It is estimated that the opacity of the coated paper increases.
- Used paper pulp may or may not be deinked, and deinked pulp includes high-quality paper, medium-quality paper, low-grade paper, newspaper, flyers, magazines, etc. It is possible to use deinked pulp and the like.
- base paper made from mechanical pulp and waste paper pulp has a coating solution that is too water-absorbing, so that the coating solution can easily penetrate into the paper layer, resulting in poor coverage of the coating solution and reduced whiteness.
- white unevenness is likely to occur due to water absorption unevenness.
- the curtain coating method to be described later it has surprisingly succeeded in suppressing white unevenness while using a large amount of mechanical pulp and the like.
- the smoothness of the base paper generally decreases.
- the present invention even if a base paper with low smoothness containing a large amount of mechanical pulp or waste paper pulp is used. Generation of white unevenness is suppressed.
- the reason why a coated paper for printing with little white unevenness can be obtained while using a large amount of mechanical pulp or the like is speculated as follows, although details are unknown. That is, in the most commonly used blade-type coating method, the coating liquid is pushed into the base paper by the blade, so if the base paper has low smoothness and water absorption is uneven, Can not be covered by, and tends to appear as white unevenness. On the other hand, in the curtain coating method used in the present invention, since the coating layer previously formed in the form of the curtain film is placed on the base paper, the contact between the curtain film and the base paper is gentle and soft compared to the blade system. It is estimated that the dispersion of the base paper can be covered by the soft coating layer.
- the coating liquid since the coating liquid is not pushed into the base paper during coating, the pigment contained in the coating liquid stays on the surface of the base paper, improving the concealment of the base paper and increasing the bulkiness with many voids. It is presumed that the light scattering property becomes high because a simple coating layer is obtained.
- a base paper with low whiteness is used.
- the whiteness of the base paper is as low as 45 to 70%, preferably 55 to 70%. If the whiteness is lower than 45%, even if the white unevenness is good, sufficient whiteness cannot be obtained after coating. On the other hand, if the whiteness is higher than 70%, the light absorption is inferior so Sufficient opacity cannot be obtained.
- the basis weight of the base paper used in the present invention to obtain a coated printing paper of low basis weight, preferably in the range of 30 ⁇ 66g / m 2, more preferably in the range of 33 ⁇ 50g / m 2, 35 A range of ⁇ 45 g / m 2 is more preferred.
- the basis weight is lower than 30 g / m 2 , the paper strength is reduced and paper breakage is likely to occur during operation, and the production efficiency is lowered.
- the basis weight is higher than 66 g / m 2 , the coating amount must be reduced in order to obtain a low basis weight coated paper, and as a result, whiteness, opacity, and white unevenness are compatible at a high level. It becomes difficult to do.
- the density of the base paper used in the present invention is preferably 0.40 ⁇ 0.70g / cm 3, more preferably 0.40 ⁇ 0.60g / cm 3, is 0.45 ⁇ 0.55g / cm 3 Further preferred. If the density of the base paper is higher than 0.7 g / cm 3, it is not preferable because there are few voids and sufficient light scattering properties cannot be obtained in the base paper layer and sufficient opacity cannot be obtained. On the other hand, if the density of the base paper is lower than 0.4 g / cm 3 , the paper strength is lowered, and paper breakage occurs frequently during operation, which is not preferable. In the curtain coating method used in the present invention, compared to other coating methods, even when the density of the base paper is low and the smoothness is low, white unevenness can be effectively suppressed. A relatively low range can be set.
- the base paper of the present invention can be pre-calendered. As mentioned above, although water absorption unevenness and low smoothness of the base paper can be covered by curtain coating, if the base paper is extremely low in smoothness, the smoothness of the coated paper also becomes low. To improve the smoothness of the base paper. As a means for improving the smoothness of the base paper, a clear paint or a paint containing a pigment containing starch as a main component can be preliminarily applied to the base paper before curtain coating. This pre-coated base paper may be subjected to curtain coating without undergoing a drying step, that is, with the paint on the base paper wet. Thus, the state of the base paper after pre-coating before being used for curtain coating is not limited.
- the base paper of the present invention can be blended with known additives such as known fillers and paper strength agents.
- known additives such as known fillers and paper strength agents.
- calcium carbonate is preferable.
- curtain coating In the present invention, a coating liquid containing a white pigment is curtain-coated on the base paper.
- curtain coating is a coating system in which a coating liquid is flowed down in a curtain shape to form a curtain film, and a base paper is passed through the curtain film to form a coating layer on the base paper.
- Curtain coating is a contour coating in which a coating layer is formed along a base paper, and has a characteristic that the coating amount can be easily controlled because of a so-called pre-weighing system.
- the blade coating method is the most common, but other methods such as a film transfer method or an air knife coating method are known.
- high required quality is cleared by adopting the curtain coating method.
- the coating liquid is pushed into the base paper by the blade, when the base paper has low smoothness and water absorption varies, the base paper variation can be covered by the coating layer. It is not possible to appear as white unevenness as it is.
- the film transfer method is a coating method in which a film of a coating solution is measured on an applicator and transferred to a base paper to provide a coating layer.
- the load applied to the base paper during coating is small, so that the coating liquid does not penetrate the base paper and the coating liquid has good coverage, but the applicator roll nips the base paper.
- the covering property is deteriorated, the whiteness is reduced, and white unevenness occurs.
- Another problem with the film transfer coating method is that an operation problem called boiling occurs during high-speed operation.
- the air knife coating method is a coating method in which an excess coating solution is adhered to a base paper, and then a pressure air stream called an air knife is sprayed on the coating surface to scrape off the excess.
- a pressure air stream called an air knife is sprayed on the coating surface to scrape off the excess.
- the load applied to the base paper is small compared to the blade coating method, it is inevitable that a certain amount of load is applied during coating compared to the curtain coating method.
- an air knife coater scrapes off an excessive paint by an air flow, only a coating solution having a low viscosity can be used. This is because if the viscosity is high, the flow velocity of the airflow needs to be increased, but if the airflow is high, turbulent vortices are generated and coating stripes are generated on the coating surface.
- the coated paper of the present invention is produced by applying a single layer or multiple layers by curtain coating on both sides or one side of the base paper.
- a coating apparatus other than the curtain coating apparatus for coating any layer.
- the blade The pigment coating liquid may be applied by a coating apparatus, or curtain coating may be performed after blade coating.
- a base paper having low water absorption unevenness and low smoothness is used. Therefore, in order to maximize the benefits of curtain coating, the coating layer adjacent to the base paper must be at least curtain coating. It is preferable to apply by.
- a known apparatus used for curtain coating can be used.
- a pump for feeding the coating liquid, a defoaming device for degassing the coating liquid, and the like can be used.
- the curtain coating speed is not particularly limited, but the coating speed is preferably 600 m / min or more, more preferably 800 m / min or more, and further preferably 1000 m / min or more.
- the higher the coating speed the more the curtain film is pulled by the base paper that runs at high speed, and so-called craters are more likely to be generated. If it is set as the breaking time of this, generation
- the coating amount of the printing coated paper of the present invention is preferably in the range of 12 to 30 g / m 2 , more preferably in the range of 15 to 20 g / m 2 per side. If the coating amount is less than 12 g / m 2, it is not preferable because sufficient whiteness and opacity cannot be obtained. On the other hand , if the coating amount is larger than 20 g / m 2 , binder migration occurs during drying, and uneven ink deposition or paper smearing tends to occur during printing. In the present invention, the coating amount is preferably in a relatively high range in order to maximize the high coverage by the curtain coating method.
- Pigment coating liquid In the present invention, a pigment coating liquid containing at least calcium carbonate is curtain-coated on the base paper.
- the pigment coating liquid of the present invention can be prepared by mixing water, a pigment, and other additives. In preparation of the pigment coating solution, water, pigment and other additives may be mixed at the same time. However, in consideration of workability, a slurry of water and pigment is prepared in advance, and other additives are added to this slurry. Are preferably mixed. For mixing, ordinary mixing means such as a mixer may be used. In addition to this, the coating liquid used in the present invention may contain other components such as a surfactant. Each component will be described below.
- the coating liquid used in the present invention contains calcium carbonate as a white pigment, and preferably contains spindle-shaped calcium carbonate.
- calcium carbonate if calcium carbonate is used, other pigments are not particularly limited, and pigments conventionally used for coated paper can be used.
- pigments conventionally used for coated paper can be used.
- the white pigment may consist solely of calcium carbonate. If two or more kinds of white pigments are used in combination, a combination of calcium carbonate, kaolin and clay is preferable.
- the coating liquid of the present invention contains calcium carbonate such as heavy calcium carbonate and light calcium carbonate.
- the average particle diameter ( D50) is 0.3 to 0.8 ⁇ m
- the ratio (D75 / D25) of the particle diameter (D75) at 75 cumulative mass% and the particle diameter (D25) at 25 cumulative mass% of the particle size distribution curve by the sedimentation method is 1
- spindle-shaped light calcium carbonate which is .5 or more and less than 3.5. Since the calcium carbonate has a sharp particle size distribution, it has the effect of improving the base paper hiding property.
- the aspect ratio is also high.
- when using calcium carbonate as a white pigment it is preferable to use the said heavy calcium carbonate and spindle-shaped light calcium carbonate together.
- curtain coating which is a non-contact coating method, tends to make it difficult for the pigment to orient in the direction of travel of the base paper compared to the contact coating method.
- the smoothness of the surface tends to deteriorate, but when curtain coating is performed at high speed, the curtain film is pulled by the base paper that runs at high speed, so that the pigment tends to be regularly oriented.
- calcium it is considered that a coating layer having high smoothness and less unevenness can be easily obtained.
- the present invention is not bound by this consideration.
- the dynamic surface tension of the coating liquid can be adjusted using a surfactant.
- the surfactant includes an anionic surfactant, a cationic surfactant, and a nonionic surfactant.
- an anionic surfactant is preferable.
- the cationic surfactant tends to aggregate the pigment in the coating solution. Further, the nonionic surfactant is difficult to give sufficient wettability to the coating solution.
- the anionic surfactant include sulfonic acid surfactants, sulfate ester surfactants, and carboxylic acid surfactants. Among these, sulfonic acid-based surfactants are preferable and alkylsulfosuccinic acid is particularly preferable because the wettability of the coating liquid can be improved.
- the amount of the anionic surfactant added is preferably 0.1 to 1% by weight based on the total pigment solid content in the coating solution. If the addition amount is less than 0.1% by weight, the wettability of the coating liquid to the base paper may be insufficient. On the other hand, when the addition amount is larger than 1% by weight, the coating liquid may permeate the base paper excessively due to excessive wettability of the coating liquid to the base paper, and the quality of the coated paper may be deteriorated.
- These surfactants can be used alone, but two or more of them may be used in combination.
- the curtain coating solution may contain a viscosity improver for adjusting the viscosity.
- a viscosity improver composed of a W / O emulsion in which an aqueous solution of a polycarboxylic acid copolymer having a weight average molecular weight of 4 million to 50 million is dispersed in an organic solvent is preferable.
- this viscosity improver is also referred to as “W / O emulsion viscosity improver”.
- a viscosity improver is a drug used to change the viscosity of a system.
- a polycarboxylic acid-based copolymer refers to a polymer obtained by polymerizing a monomer containing a carboxyl group or a derivative thereof.
- monomers containing a carboxyl group include acrylic acid, maleic acid, and methacrylic acid.
- derivatives of monomers containing carboxyl groups include mono- or dialkaline earth metal salts, mono- or diesters, amides, imides, and anhydrides of these monomers.
- maleic acid, methacrylic acid, or a derivative thereof is used as the monomer, a branched chain is introduced into the molecular structure of the polymer, so that the spinnability of the resulting coating liquid may not be sufficient.
- the polycarboxylic acid copolymer is used in the state of a W / O emulsion. Therefore, from the viewpoint of easily forming a W / O emulsion, the monomer is preferably a sodium salt of acrylic acid and acrylamide.
- the ratio of these monomers may be arbitrary, but it is preferably 50:50 to 5:95 in terms of molar ratio.
- the viscosity improver used in the present invention is a W / O emulsion in which an aqueous solution of the polycarboxylic acid copolymer is dispersed in an organic solvent.
- a W / O emulsion viscosity improver can be produced, for example, as follows. 1) Add a surfactant to an organic solvent at room temperature and mix uniformly. 2) Add a monomer dissolved in water to the mixture to prepare a pre-emulsion. 3) Add a polymerization initiator to the pre-emulsion. Stir the mixture to polymerize the monomer.
- the organic solvent known organic solvents such as toluene, xylene, kerosene, and isoparaffin can be used.
- the surfactant a known surfactant such as sorbitan monostearate can be used.
- the solid content in the W / O emulsion viscosity improver is preferably 20 to 60% by weight.
- the weight average molecular weight of the polycarboxylic acid copolymer is 4 million to 50 million. When the weight average molecular weight is less than 4 million, sufficient spinnability cannot be given to the coating solution. On the other hand, if the weight average molecular weight is larger than 50 million, the thickening effect on the coating solution is too strong, and it becomes difficult to feed the coating solution. Considering the balance between spinnability and liquid feeding property, the weight average molecular weight is more preferably 10 million to 30 million. The weight average molecular weight is obtained by analyzing the polymer by gel permeation chromatography and converting to polystyrene.
- Polycarboxylic acid-based copolymers are generally used as thickeners or water retention agents in the field of coated paper for printing, but the weight average molecular weight of the commonly used copolymers is from several tens of thousands to It is in the range of hundreds of thousands.
- the spinnability of the coating liquid is improved and craters in curtain coating are suppressed. it can.
- W / O type emulsion viscosity improver is excellent in handleability because its own viscosity is not too high.
- a viscosity improver is used to increase the viscosity of a coating solution.
- a W / O emulsion viscosity improver increases moderately without excessively increasing the viscosity of a coating solution, and It also gives stringiness. Therefore, the W / O emulsion viscosity improver can improve the spinnability of the coating liquid without impairing the handleability of the coating liquid. Although this reason is not limited, it is guessed as follows.
- the W / O type emulsion viscosity improver since the copolymer exists in a state of being confined in the aqueous phase that is the dispersed phase, the molecular chain does not spread and the molecular chain is less entangled. For this reason, even if it contains a very high molecular weight copolymer as described above, the viscosity of the viscosity modifier itself is not too high, and it is excellent in handleability.
- the W / O emulsion viscosity improver is mixed with water to form a coating liquid, a phase inversion in which the aqueous phase that is the dispersed phase becomes a continuous phase occurs, and the molecular chain of the copolymer spreads. It exerts a thickening effect to cause entanglement.
- the copolymer since the copolymer is present in the dispersed phase, the molecular chains are entangled and the viscosity improver itself has a high viscosity.
- the weight average molecular weight of the copolymer is 1,000,000 or more, the viscosity is very high and handling becomes extremely difficult.
- such a viscosity modifier is difficult to mix uniformly with a coating liquid, it is also difficult to increase the viscosity of the coating liquid uniformly. For this reason, handling properties, such as a liquid feeding property of a coating liquid, are impaired remarkably, Furthermore, sufficient spinnability cannot be provided to a coating liquid.
- the addition amount of the viscosity modifier is preferably 0.05 parts by weight or more with respect to 100 parts by weight of the total pigment in the coating liquid.
- the addition amount is less than 0.05 parts by weight, there are cases where sufficient spinnability cannot be imparted to the coating solution.
- the addition amount is more than 0.5 parts by weight, the occurrence of craters can be suppressed, but the viscosity of the coating solution becomes too high, and the solid content concentration of the coating solution has to be greatly reduced, It may permeate excessively into the base paper and cause a decrease in the quality of the coated paper.
- the amount added is more preferably 0.1 to 0.3 parts by weight.
- an adhesive (binder) to the curtain coating liquid.
- the adhesive is not particularly limited, and an adhesive conventionally used for coated paper can be used.
- adhesives include styrene / butadiene, styrene / acrylic, ethylene / vinyl acetate, butadiene / methyl methacrylate, vinyl acetate / butyl acrylate, and other copolymers, polyvinyl alcohol, maleic anhydride copolymer And synthetic adhesives such as acrylic acid / methyl methacrylate copolymers; proteins such as casein, soy protein, synthetic protein; oxidized starch, positive starch, urea phosphated starch, hydroxyethyl etherified starch, etc.
- adhesives for coated paper such as starches such as etherified starch and dextrin; cellulose derivatives such as carboxymethylcellulose, hydroxyethylcellulose, and hydroxymethylcellulose are included.
- starches such as etherified starch and dextrin
- cellulose derivatives such as carboxymethylcellulose, hydroxyethylcellulose, and hydroxymethylcellulose are included.
- One or more types of adhesives can be appropriately selected and used. In a preferred embodiment, these adhesives are used in the range of about 5 to 50 parts by weight, more preferably about 8 to 30 parts by weight per 100 parts by weight of the pigment. Synthetic adhesives are preferred because they do not significantly increase the viscosity of the coating solution.
- polyvinyl alcohol with a low degree of polymerization because the adhesive effect can be enhanced without significantly increasing the viscosity.
- the degree of polymerization is preferably 1000 or less, more preferably 700 or less, and the degree of polymerization may be about 500.
- auxiliary agents blended in ordinary pigments for coated paper such as dispersants, thickeners, water retention agents, antifoaming agents, water resistance agents, and colorants, can be used as necessary.
- the coating solution used in the present invention preferably has a break time of 200 ms or more.
- the breaking time of the coating liquid is an index of the ease of elongation (threading property) of the coating liquid.
- a coating solution having a longer breaking time results in a coating solution having higher spinnability. If the breaking time is shorter than 200 ms, the coating liquid hardly follows the elongation that occurs instantaneously when the curtain film contacts the base paper due to the difference between the falling speed of the curtain film and the traveling speed of the base paper. For this reason, a coating film fractures
- the upper limit of the breaking time is not particularly limited, but if it is longer than 500 ms, the fluidity of the coating liquid deteriorates and it becomes difficult to feed the paint. In this case, it is conceivable to lower the solid content of the coating liquid in order to improve fluidity, but this is not preferable because the quality of the coated paper deteriorates due to excessive penetration of the coating liquid into the base paper.
- the breaking time in the present invention is measured with an extensional viscometer.
- the breaking time is as follows: 1) Using a viscometer having a pair of circular plates with a diameter of 8 mm arranged coaxially and perpendicular to the axis, the liquid temperature is 30 between the plates (gap 1 mm). 2) The upper plate is pulled up vertically by 8 mm at a speed of 400 mm / second and held as it is, and 3) The time from when the plate starts to be pulled until the coating solution filament breaks is sealed. It is obtained by measuring. The time before the filament breaks is preferably measured with a laser, and the time resolution at this time is preferably about 2 ms.
- An example of a viscometer capable of such measurement includes an extension viscometer (model name: CaBER1) manufactured by Thermo Harke.
- the coating liquid used in the present invention preferably has a B-type viscosity at 30 ° C. in the range of 500 to 3000 mPa ⁇ s, more preferably 800 to 3000 mPa ⁇ s.
- the B-type viscosity of the coating solution is No. It is measured at a rotational speed of 60 rpm using a rotor of 4. In the present invention, the numerical range includes its end points.
- the breaking time of the coating liquid is 200 ms or more, if the B-type viscosity is lower than 500 mPa ⁇ s, it is not preferable because the coating liquid excessively penetrates into the base paper and the quality of the coated paper is deteriorated. On the other hand, when the B-type viscosity is larger than 3000 mPa ⁇ s, the fluidity of the coating liquid is deteriorated, and it becomes difficult to feed the coating liquid.
- the breaking time and viscosity characteristics of the coating liquid used in the present invention can be adjusted mainly by the amount of viscosity improver added. Moreover, these characteristics can be adjusted to some extent by increasing the solid content concentration of the coating liquid. This is because by increasing the solid content concentration, the interaction between the pigment particles and other blends in the coating liquid is likely to occur, and the breaking time of the coating liquid can be lengthened. When the solid content concentration of the coating liquid is high, the printing quality of the coated paper is also improved.
- the curtain coating liquid can be given a moderate viscosity that is not too high. Therefore, the solid content concentration of the coating liquid can be increased, and the printing quality of the coated paper can be improved.
- the solid concentration of the coating liquid is preferably 58% by weight or more, and more preferably 62% by weight or more. When the solid content is lower than 58% by weight, the quality of the coated paper may deteriorate due to excessive penetration of the coating liquid into the base paper.
- the upper limit of the solid content concentration is not particularly limited, but is preferably 75% by weight or less and more preferably 70% by weight or less in consideration of liquid feeding properties.
- the coating liquid used in the present invention preferably has a dynamic surface tension in a fluid state, that is, a dynamic surface tension of 25 to 45 mN / m.
- the dynamic surface tension is a surface tension in the middle of reaching an equilibrium state between the liquid surface and the inside when a new liquid surface is generated, and is an index of wettability in a fluid state of the coating liquid.
- the wettability is an index representing the ease with which the coating liquid spreads on the substrate surface. High wettability generally indicates that the coating liquid tends to spread on the surface of the substrate. That is, since the coating liquid having a dynamic surface tension in the above range exhibits good wettability immediately after contact with paper, it is easy to suppress the occurrence of craters.
- the dynamic surface tension is determined by the maximum bubble pressure method.
- the maximum bubble pressure method bubbles (interface) are continuously generated from a probe having a radius r inserted in a liquid, and the pressure applied to the bubbles when the bubble radius becomes the same as the probe radius r (maximum bubble pressure). ) To obtain the surface tension by the following formula.
- the dynamic surface tension measures the dynamic surface tension at each lifetime while changing the time (lifetime) from the time when a new interface is generated in the probe tip until the maximum bubble pressure is reached.
- the dynamic surface tension measures the dynamic surface tension at each lifetime while changing the time (lifetime) from the time when a new interface is generated in the probe tip until the maximum bubble pressure is reached.
- the dynamic surface tension measures the dynamic surface tension at each lifetime while changing the time (lifetime) from the time when a new interface is generated in the probe tip until the maximum bubble pressure is reached.
- the dynamic surface tension in a short time the wettability of a liquid in a flowing or stirring state can be evaluated. That is, the shorter the lifetime, the closer to the fluid state, the dynamic surface tension in the very initial state can be measured.
- the value of the surface tension when the lifetime is 100 ms is preferably the dynamic surface tension.
- This dynamic surface tension can be measured using an automatic dynamic surface tension meter (“BP-D5” manufactured by Kyowa Interface Chemical Co., Ltd.) or the like.
- the dynamic surface tension of the coating liquid used in the present invention can be adjusted by adding a surfactant.
- the dynamic surface tension of the coating liquid used in the present invention is preferably 45 mN / m or less. If the dynamic surface tension is greater than 45 mN / m, the wettability of the coating liquid to the base paper becomes insufficient, and crater generation may not be sufficiently suppressed. On the other hand, if the dynamic surface tension is less than 25 mN / m, the crater can be suppressed, but the coating liquid permeates the base paper excessively due to the excessive wettability of the coating liquid to the base paper, and the quality of the coated paper May decrease. From the above, the dynamic surface tension of the coating liquid used in the present invention is preferably 25 to 45 mN / m, more preferably 25 to 35 mN / m.
- the coated paper of the present invention is produced through a normal drying process after a coating layer is provided on the base paper.
- the calendar treatment of the coating layer is widely performed, and the calendar treatment may be performed in the present invention, but it is preferable not to perform the surface treatment process by the calendar.
- the curtain coating method used in the present invention since no load is applied to the base paper and the coating layer at the time of coating, the bulkiness of the base paper and the coating layer is maintained, but when the calendar process is performed, the bulkiness is offset. End up. Further, when the void amount of the coating layer is reduced by the calendar process, the light scattering property of the coating layer is lowered, the base paper layer having a low whiteness is easily noticeable, and the whiteness is also lowered. Therefore, the present invention is suitable for matte coated paper that is not subjected to calendaring after coating.
- Coated paper for printing In the present invention, a high-quality printed matter with little printing unevenness can be obtained by the curtain coating method without performing calendar processing.
- the printing coated paper of the present invention can be applied to various printing methods, but is particularly suitable for an offset printing method.
- the coated paper for printing of the present invention has a relatively low basis weight (light weight), and the basis weight is in the range of 60 to 90 g / m 2 , more preferably 70 to 90 g / m 2 .
- the coated paper for printing in this basis weight zone is required to have high opacity because the paper thickness is thin, but according to the present invention, such an effect is easily exhibited.
- the opacity of the coated paper for printing of the present invention is 95% or more. If it is lower than 95%, the image printed on the back surface can be seen through the front surface, and the value as a printed matter is inferior.
- the whiteness of the coated paper for printing of the present invention is 75% or more. If it is lower than 75%, it cannot be said that it is sufficient as a general coated paper for printing, and the printed image looks darker than the original, which is not preferable because it is inferior in the ability to transmit the content.
- the curtain coating method used in the present invention even if there is a large difference in whiteness between the base paper and the coating layer, good white unevenness is obtained, so the difference between the whiteness of the base paper and the whiteness of the coated paper for printing Is not particularly limited.
- the density of the coated paper for printing of the present invention is preferably in the range of 0.8 to 1.1 g / cm 3 .
- the glossiness of the coated paper for printing of the present invention is preferably 40% or less.
- Dynamic surface tension When bubbles are continuously generated from a probe (capillary tube) inserted into the coating solution using an automatic dynamic surface tension meter (BP-D5, manufactured by Kyowa Interface Chemical Co., Ltd.) The maximum pressure (maximum bubble pressure) was measured by the maximum bubble pressure method to determine the surface tension. Specifically, the value of the surface tension when the lifetime (the time from when a new interface is generated in the probe tip to the time when the maximum bubble pressure is reached) is 100 ms is defined as the dynamic surface tension.
- Example 1 [Manufacture of base paper] As a raw material pulp, bleached kraft pulp (whiteness 80%) 5%, mechanical pulp (whiteness 60%) 20%, waste paper pulp (whiteness 51%) 75% mixed and disaggregated, Canadian standard freeness A pulp slurry with (CSF) adjusted to 200 cc was obtained. To this pulp slurry, 0.1% polyacrylamide and 0.15% yield improver are added per weight of completely dry pulp, and light calcium carbonate (Rosetta type, average particle size 3.0 ⁇ m) is newly added as a filler. Was added to the base paper to prepare a paper stock.
- 0.1% polyacrylamide and 0.15% yield improver are added per weight of completely dry pulp, and light calcium carbonate (Rosetta type, average particle size 3.0 ⁇ m) is
- the obtained paper stock was subjected to neutral papermaking with a gap former type paper machine so that the basis weight was 40.0 g / m 2 .
- the density of the base paper was 0.62 g / cm 3 , the opacity was 95%, and the whiteness was 55%.
- Example 2 In Example 1, a coated paper for printing was obtained in the same manner as in Example 1, except that the pulp composition of the base paper was exposed and changed to kraft pulp 25%, mechanical pulp 20%, and used paper pulp 55%.
- the density of the base paper was 0.48 g / cm 3 , the opacity was 86%, and the whiteness was 70%.
- Example 3 In Example 1, a coated paper for printing was obtained in the same manner as in Example 1 except that the basis weight of the base paper was changed from 40 g / m 2 to 30 g / m 2 .
- the density of the base paper was 0.62 g / cm 3 , the opacity was 88%, and the whiteness was 55%.
- Example 1 a coated paper for printing was obtained in the same manner as in Example 1, except that the pulp composition of the base paper was changed to 55% kraft pulp, 20% mechanical pulp, and 25% used paper pulp.
- the density of the base paper was 0.68 g / cm 3 , the opacity was 80%, and the whiteness was 75%.
- Example 2 In Example 1, except that the coating method was changed from the curtain coating method to the coating method using a blade coater, and the surfactant and viscosity improver were not added to the coating solution, the printing method was the same as in Example 1. Coated paper was obtained. The B-type viscosity of the coating solution was 500 mPa ⁇ s.
- Example 3 Comparative Example 3 In Example 1, except that the coating method is changed from the curtain coating method to the coating method by rod metering size press (RMSP), and the surfactant and viscosity improver are not added in the coating liquid. In the same manner as in No. 1, a coated paper for printing was obtained. The viscosity of the coating solution was 500 mPa ⁇ s.
- RMSP rod metering size press
- Example 1 by performing curtain coating on a low whiteness base paper, the coated paper has a high light absorption property, a uniform coating amount, and a high light scattering property of the coating layer. As a result, high opacity, whiteness, and good whiteness unevenness can be obtained. Further, in Example 2, the whiteness and density of the base paper are adjusted within an appropriate range with respect to Example 1, so that the matte tone printing with higher whiteness is achieved although the opacity is lower than in Example 1. Coated paper is obtained. In Example 3, by reducing the basis weight of the base paper compared to Example 1, a lighter coated paper for printing can be obtained although the opacity is lower than that of Example 1.
- Comparative Example 1 since the whiteness of the base paper is higher than the appropriate range compared to Example 1, the whiteness of the coated paper is high but the opacity is low. Further, in Comparative Example 2, since the curtain coating was changed to the blade coating in Example 1, white unevenness occurred due to the nonuniform coating amount, and the scattering property of the coating layer was inferior. Both opacity and whiteness are inferior. Further, in Comparative Example 3, since the curtain coating was changed to the rod metering size press in Example 1, the base paper was not concealed by the paint as in Comparative Example 2, but it was still not sufficient and recognizable white unevenness occurred. Inferior in opacity and whiteness.
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Abstract
Description
(1) 坪量が60~90g/m2、白色度が75%以上、不透明度が95%以上であるマット調印刷用塗工紙の製造方法であって、古紙パルプおよび/または機械パルプを合計で50%以上含有する原料パルプから抄紙される白色度が45~70%の原紙上に、炭酸カルシウムを含む塗工液をカーテン塗工することを含む上記方法。
(2) 片面あたりの塗工量が12~30g/m2である、(1)に記載の方法。
(3) 前記炭酸カルシウムとして、平均粒子径(D50)が0.3~0.8μmであり、沈降方式による粒度分布曲線の75累積質量%における粒子径(D75)と25累積質量%における粒子径(D25)の比(D75/D25)が1.5以上3.5未満である紡錘状軽質炭酸カルシウムを用いる、(1)または(2)に記載の方法。
(4) 前記カーテン塗工の塗工速度が800m/分以上である、(1)~(3)のいずれかに記載の方法。
(5) 前記塗工液が、重量平均分子量400万~5000万のポリカルボン酸系共重合体の水溶液が有機溶媒に分散しているW/O型エマルションである粘性改良剤を含む、(1)~(4)のいずれかに記載の方法。
(6) (1)~(5)のいずれかの方法により製造されるマット調印刷用塗工紙。
本発明では、古紙パルプおよび/または機械パルプを合計で50%以上含有する原料パルプから抄紙され、白色度が45~70%の原紙が使用される。原紙は通常使用するパルプの白色度が反映されるので、例えば、使用するパルプの白色度を45%~70%とすればよい。
本発明においては、白色顔料を含んでなる塗工液を上記原紙にカーテン塗工する。本発明においてカーテン塗工とは、塗工液をカーテン状に流下させてカーテン膜を形成し、当該カーテン膜に原紙を通して原紙上に塗工層を設ける塗工方式である。カーテン塗工は、原紙に沿って塗工層が形成される輪郭塗工であり、また、いわゆる前計量方式であるため塗工量の制御が容易であるという特徴を有する。
本発明では、少なくとも炭酸カルシウムを含んでなる顔料塗工液を原紙上にカーテン塗工する。本発明の顔料塗工液は、水と顔料とその他の添加物とを混合して調製することができる。顔料塗工液の調製は、水と顔料とその他の添加物とを同時に混合してよいが、作業性を考慮すると、予め水と顔料のスラリーを調製しておき、このスラリーにその他の添加物を混合することが好ましい。混合には、ミキサー等の通常の混合手段を用いてよい。本発明で用いる塗工液は、この他に、界面活性剤等他の成分を含んでいてもよい。各成分等について以下に説明する。
具体的に動的表面張力は、プローブ先端内で新しい界面が生成した時点から最大泡圧となるまでの時間(ライフタイム)を変化させながら、各ライフタイムにおける動的表面張力を測定する。このように短時間における動的表面張力を測定することで、流動または攪拌状態にある液体の濡れ性が評価できる。つまり、ライフタイムが短いほどより流動状態に近い、ごく初期の状態における動的表面張力が測定できる。本発明においては、測定精度の観点から、ライフタイムを100msとした場合における表面張力の値を動的表面張力とすることが好ましい。この動的表面張力は自動動的表面張力計(「BP-D5」協和界面化学社製)等用いて測定することができる。
本発明の塗工紙は、原紙上に塗工層を設けた後、通常の乾燥工程を経て製造される。一般に、塗工層をカレンダー処理することが広く行われ、本発明においてカレンダー処理を行ってもよいが、カレンダーによる表面処理工程は行わないことが好ましい。本発明で使用するカーテン塗工方式では、塗工時に原紙および塗工層に負荷がかからないため、原紙および塗工層の嵩高性が維持されるものの、カレンダー処理を行うと嵩高性が相殺されてしまう。また、カレンダー処理によって塗工層の空隙量が減少すると、塗工層の光散乱性が低下し、白色度の低い原紙層が目立ちやすくなり、白色度も低下するため好ましくない。したがって、本発明は、塗工後にカレンダー処理を行わないマット調塗工紙に適している。
本発明においてはカーテン塗工方式により、カレンダー処理を行わなくても印刷ムラが少ない高品質の印刷物が得られる。本発明の印刷用塗工紙は各種印刷方式に適用することができるが、中でもオフセット印刷方式に好適である。
(1)坪量:JIS P8124「紙及び板紙-坪量測定方法」に準拠して測定した。
(2)密度:JIS P8118「紙及び板紙-厚さ及び密度の試験方法」に準拠して測定した。
(3)不透明度:JIS P8149「紙及び板紙-不透明度試験方法(紙の裏当て)-拡散照明法」に準拠し、色差計(CMS-35SPX、村上色彩製)を用いて、紫外光を含む光源にて測定した。
(4)白色度:JIS P8148「紙,板紙及びパルプ-ISO白色度(拡散青色光反射率)の測定方法」に準拠し、色差計(CMS-35SPX、村上色彩製)を用いて測定した。
(5)白色ムラ:以下の基準により目視により3段階で評価した。
○:ムラが認識できない、△:認識できるムラがある、×:目立つムラがある
(6)破断時間:伸長粘度計(機種名:CaBER1、サーモハーケ社製)を用い、1)前記粘度計の同軸かつ軸が垂直になるように配置された一対の直径8mmの円形プレート間(ギャップ1mm)に液温が30℃の塗工液を封入し、2)上方のプレートを400mm/秒の速度で8mm垂直に引き上げてそのまま保持し、3)前記プレートの引き上げ開始時点から塗工液フィラメントが破断するまでの時間を測定した。
(7)動的表面張力:自動動的表面張力計(BP-D5、協和界面化学社製)を用いて、塗工液中に挿したプローブ(細管)から気泡を連続的に発生させたときの最大圧力(最大泡圧)を最大泡圧法により測定し、表面張力を求めた。具体的には、ライフタイム(プローブ先端内で新しい界面が生成した時点から最大泡圧となるまでの時間)が100msである場合の表面張力の値を動的表面張力とした。
[原紙の製造]
原料パルプとして、晒しクラフトパルプ(白色度80%)5%、メカニカルパルプ(白色度60%)20%、古紙パルプ(白色度51%) 75%の割合で混合して離解し、カナダ標準型フリーネス(CSF)を200ccに調整したパルプスラリーを得た。このパルプスラリーに、絶乾パルプ重量当たり、0.1%のポリアクリルアミド、0.15%の歩留まり向上剤を添加して、填料として新たに軽質炭酸カルシウム(ロゼッタ型、平均粒子径3.0μm)を原紙重量当たり8.0%添加し、紙料を調成した。
重質炭酸カルシウム(FMT-97、ファイマテック社製)50部、紡錘状軽質炭酸カルシウム(タマパール TP-221-70GS、奥多摩工業社製 D75/D25=2.5)50部からなる顔料に対し、全顔料に対して、接着剤としてスチレン・ブタジエンラテックス(NP-200B、JSR社製)を10部、PVA(クラレ社製、ポバール105、重合度500)0.5部を加え、さらに蛍光染料(Blankophor Z-NSP、Kemira社製)1部、界面活性剤(Newcol 291PG、日本乳化剤社製)0.2部、W/O型粘性改良剤(ソマール社製、ソマレックス530)0.1部を加え、さらに水を加えて固形分濃度65%の塗工液を得た。30℃、60rpmにおけるこの顔料塗工液のB型粘度は1000mPa・sであった。
上記の塗工液を、カーテンコーターで片面あたりの塗工量が20g/m2になるように、塗工速度1000m/分で両面に塗工し、乾燥して印刷用塗工紙を得た。カレンダー処理は行わなかった。
実施例1において、原紙のパルプ配合を晒しクラフトパルプ25%、メカニカルパルプ20%、古紙パルプ55%に変更した以外は、実施例1と同様に印刷用塗工紙を得た。原紙の密度は0.48g/cm3、不透明度は86%、白色度は70%であった。
実施例1において、原紙の坪量を40g/m2から30g/m2に変更した以外は、実施例1と同様に印刷用塗工紙を得た。原紙の密度は0.62g/cm3、不透明度は88%、白色度は55%であった。
実施例1において、原紙のパルプ配合をクラフトパルプ55%、メカニカルパルプ20%、古紙パルプ25%に変更した以外は、実施例1と同様に印刷用塗工紙を得た。原紙の密度は0.68g/cm3、不透明度は80%、白色度は75%であった。
実施例1において、塗工方式をカーテン塗工方式からブレードコーターによる塗工方式に変更し、かつ塗工液において界面活性剤および粘性改良剤を添加しない以外は、実施例1と同様に印刷用塗工紙を得た。塗工液のB型粘度は500mPa・sであった。
実施例1において、塗工方式をカーテン塗工方式からロッドメタリングサイズプレス(RMSP)による塗工方式に変更し、かつ塗工液において界面活性剤および粘性改良剤を添加しない以外は、実施例1と同様に印刷用塗工紙を得た。塗工液の粘度は500mPa・sであった。
Claims (6)
- 坪量が60~90g/m2、白色度が75%以上、不透明度が95%以上であるマット調印刷用塗工紙の製造方法であって、古紙パルプおよび/または機械パルプを合計で50%以上含有する原料パルプから抄紙される白色度が45~70%の原紙上に、炭酸カルシウムを含む塗工液をカーテン塗工することを含む上記方法。
- 片面あたりの塗工量が12~30g/m2である、請求項1に記載の方法。
- 前記炭酸カルシウムとして、平均粒子径(D50)が0.3~0.8μmであり、沈降方式による粒度分布曲線の75累積質量%における粒子径(D75)と25累積質量%における粒子径(D25)の比(D75/D25)が1.5以上3.5未満である紡錘状軽質炭酸カルシウムを用いる、請求項1または2に記載の方法。
- 前記カーテン塗工の塗工速度が800m/分以上である、請求項1~3のいずれかに記載の方法。
- 前記塗工液が、重量平均分子量400万~5000万のポリカルボン酸系共重合体の水溶液が有機溶媒に分散しているW/O型エマルションである粘性改良剤を含む、請求項1~4のいずれかに記載の方法。
- 請求項1~5のいずれかの方法により製造されるマット調印刷用塗工紙。
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
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| CN2012800160067A CN103459722A (zh) | 2011-03-29 | 2012-03-22 | 印刷用涂布纸及其制造方法 |
| US14/008,086 US9034435B2 (en) | 2011-03-29 | 2012-03-22 | Coated printing papers and processes for preparing them |
| EP12765253.5A EP2692947A4 (en) | 2011-03-29 | 2012-03-22 | COATED PAPER FOR PRINTING AND MANUFACTURING METHOD THEREFOR |
| KR1020137028330A KR101455187B1 (ko) | 2011-03-29 | 2012-03-22 | 인쇄용 도공지 및 그 제조 방법 |
| JP2012547768A JP5174998B1 (ja) | 2011-03-29 | 2012-03-22 | 印刷用塗工紙及びその製造方法 |
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| JP2011-071778 | 2011-03-29 | ||
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| WO2012133088A1 true WO2012133088A1 (ja) | 2012-10-04 |
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| US (1) | US9034435B2 (ja) |
| EP (1) | EP2692947A4 (ja) |
| JP (1) | JP5174998B1 (ja) |
| KR (1) | KR101455187B1 (ja) |
| CN (1) | CN103459722A (ja) |
| WO (1) | WO2012133088A1 (ja) |
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| CN108999012A (zh) * | 2018-06-25 | 2018-12-14 | 金东纸业(江苏)股份有限公司 | 涂布纸、铜版纸、涂布纸的制作方法及铜版纸的制作方法 |
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| JP6200213B2 (ja) * | 2013-06-10 | 2017-09-20 | 理想科学工業株式会社 | 油中水型エマルション接着剤 |
| JP6092127B2 (ja) * | 2014-01-10 | 2017-03-08 | 北越紀州製紙株式会社 | 白板紙 |
| NL2030210B1 (en) * | 2021-12-21 | 2023-06-29 | Lumicks Ca Holding B V | Method for cleaning a microfluidic device using an ionic liquid |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108999012A (zh) * | 2018-06-25 | 2018-12-14 | 金东纸业(江苏)股份有限公司 | 涂布纸、铜版纸、涂布纸的制作方法及铜版纸的制作方法 |
| CN108999012B (zh) * | 2018-06-25 | 2020-10-27 | 金东纸业(江苏)股份有限公司 | 涂布纸、铜版纸、涂布纸的制作方法及铜版纸的制作方法 |
Also Published As
| Publication number | Publication date |
|---|---|
| US20140023844A1 (en) | 2014-01-23 |
| CN103459722A (zh) | 2013-12-18 |
| EP2692947A4 (en) | 2014-11-19 |
| JPWO2012133088A1 (ja) | 2014-07-28 |
| JP5174998B1 (ja) | 2013-04-03 |
| KR101455187B1 (ko) | 2014-10-27 |
| EP2692947A1 (en) | 2014-02-05 |
| KR20140026432A (ko) | 2014-03-05 |
| US9034435B2 (en) | 2015-05-19 |
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