JP6189026B2 - Printing paper - Google Patents

Description

  The present invention relates to printing paper.

  In recent years, in the printing industry, the printing method has shifted from conventional letterpress printing to offset printing, etc., as advertisements and magazines become full-colored and upgraded. This offset printing has excellent photographic gradation reproducibility and allows multicolor printing on many types of paper. At the same time as the transition of printing methods, improvements in the quality of paper used for offset printing are required. Yes.

  In addition to basic properties such as printability, whiteness, and opacity, the printing paper used for the offset printing is required to have a curling suppression function due to fiber orientation, fiber density, and dryness anisotropy. . As a technique for suppressing such curling that causes paper feeding failure in a printing press, printing paper in which a surface sizing agent such as modified starch is applied to printing paper has been reported (see Japanese Patent Application Laid-Open No. 2005-163191). ).

  However, as a curling suppression method, there is a method of applying a surface sizing agent as in the printing paper described in the above publication, but an increase in cost is inevitable. Moreover, it has the subject that it cannot manufacture in the line which does not have a coating equipment.

JP 2005-163191 A

  The present invention has been made based on the above-described circumstances, and an object thereof is to provide a printing paper capable of effectively suppressing the occurrence of curling.

The invention made to solve the above problems is
In the base paper mainly composed of pulp and filler, containing silica composite heavy calcium carbonate particles in which silica is combined with heavy calcium carbonate particles as filler,
The printing paper has a moisture retention time of 800 seconds or more on the front surface and the back surface, and a difference in moisture retention time between the front surface and the back surface is within 80 seconds.

  The printing paper contains porous silica composite heavy calcium carbonate particles having a relatively large particle size as a filler, and has a water retention time of 800 seconds or more on the front and back surfaces. Therefore, it is possible to prevent the paper surface from being locally and rapidly dried during the drying process after the dehydration process during papermaking. In addition, because the difference in moisture retention time between the front and back surfaces is within 80 seconds, the moisture contained in the front and back surfaces is dried at an equivalent drying rate, so the anisotropy of the paper surface accompanying the degree of drying of the front and back surfaces Improved. This is due to the characteristics of the silica composite heavy calcium carbonate particles as follows. First, since the silica composite heavy calcium carbonate particles are composited with silica in an irregular shape caused by the heavy calcium carbonate particles, the silica composite heavy calcium carbonate particles are easily retained in the gaps between the fibers. In addition, generally heavy heavy calcium carbonate particles exhibit a relatively sharp particle size distribution due to the silica composite, so that uniform dispersion is exhibited, and the particles are likely to exist without being biased in the base paper. In this way, the printing paper can suppress the anisotropy of the degree of drying and the occurrence of curling, and can more effectively prevent a paper feed failure during the printing process. Furthermore, since the printing paper contains silica composite heavy calcium carbonate particles, it has high opacity, whiteness, oil absorption, etc., and excellent writing characteristics.

  The silica composite heavy calcium carbonate particles may have an average particle diameter (D50) measured by a laser diffraction scattering method of 2 μm to 15 μm, and the silica composite heavy calcium carbonate particles may be contained in an amount of 50% by mass or more as the filler. By making the average particle size of the silica composite heavy calcium carbonate particles within the above range and containing 50% by mass or more of silica composite heavy calcium carbonate as a filler, the moisture retention (surface moisture retention time) and ash content of the printing paper can be reduced. It can be adjusted to an appropriate range. Moreover, since the said silica composite heavy calcium carbonate has a uniform dispersibility with respect to raw material pulp, when it is made to contain in raw material pulp, the curl suppression effect and various qualities of the said printing paper can be improved further.

  Aluminum oxide is preferably combined with the silica composite heavy calcium carbonate particles. In this way, by combining cationic aluminum oxide with silica composite heavy calcium carbonate particles in addition to silica, the silica composite has a sufficiently large particle size and high dispersibility, and is self-fixing to anionic pulp raw materials. Since heavy calcium carbonate particles are obtained, it is possible to further improve the yield improving effect, curling generation suppressing effect, opacity, whiteness, oil absorption and the like of silica composite heavy calcium carbonate.

The pulp is mainly composed of softwood bleached kraft pulp (NBKP) and hardwood bleached kraft pulp (LBKP), or hardwood bleached kraft pulp, the mass ratio of NBKP and LBKP is 0: 100 to 25:75, and the basis weight Is 50 g / m ² or more and 100 g / m ² or less, and the ash content is 12% or more and 22% or less. By using NBKP and LBKP having a mass ratio in the above range as the main components of pulp, LBKP, which has a high curling suppression effect and high printability, is the main component. Can be suppressed. In particular, by making the basis weight and ash content of the printing paper within the above ranges, the effects of the present invention can be effectively expressed, and the printing paper is preferably used as printing paper for color printing pages such as catalogs. it can.

  Here, “moisture retention time” refers to 90 μl of distilled water on one side of A4 size printing paper in a standard state environment (temperature 23 ° C., humidity 50%) in accordance with JIS-P8111 (1998). It is the time from immediately after application to the mass of the paper before application of water after application. “Basis weight” is a value measured in accordance with JIS-P8124 (2011). “Ash” is a value measured according to JIS-P8251 (2003).

  As described above, the printing paper of the present invention can be effectively used as a high-quality printing paper because curling can be effectively suppressed.

It is a typical schematic diagram which shows the apparatus used for one Embodiment of the manufacturing method of the silica composite heavy calcium carbonate particle used for this invention.

  Hereinafter, embodiments of the printing paper of the present invention will be described in detail.

  In the printing paper of the present invention, silica composite heavy calcium carbonate particles are internally added as a filler in the base paper. The printing paper is obtained by papermaking a pulp slurry containing pulp and filler.

<Pulp>
As said pulp, a well-known thing can be used, A virgin pulp, used paper pulp, or these combined things can be used suitably.

  Examples of the pulp include hardwood bleached kraft pulp (LBKP), softwood bleached kraft pulp (NBKP), hardwood unbleached kraft pulp (LUKP), softwood unbleached kraft pulp (NUKP), hardwood semi-bleached kraft pulp (LSBKP), Chemical pulp such as softwood semi-bleached kraft pulp (NSBKP), hardwood sulfite pulp, softwood sulfite pulp, stone grand pulp (SGP), pressed stone grand pulp (TGP), chemi-ground pulp (CGP), ground wood pulp (GP), Various well-known pulps such as mechanical pulps such as thermomechanical pulp (TMP); pulps chemically or mechanically produced from non-wood fibers such as kenaf, hemp, and straw can be used.

  As the pulp that can be suitably used in the present invention, NBKP and LBKP are preferable, and the mass ratio of NBKP and LBKP is preferably 0: 100 to 25:75, more preferably 10:90 to 20:80, 12:88 to 18:82 are more preferred. By using LBKP as a main component, the curl suppressing effect and the printability can be improved. When the mass ratio of NBKP with respect to the total amount of pulp exceeds the above upper limit, NBKP with low dimensional stability of pulp fibers increases, so that the formation is deteriorated and the curling suppressing effect is lowered and the printability may be lowered. . On the other hand, when the mass ratio of NBKP to the total amount of pulp is less than the lower limit, the rigidity is lowered and the printing workability may be lowered.

  Used paper pulp used in the present invention is manufactured from, for example, tea waste paper, craft envelope waste paper, magazine waste paper, newspaper waste paper, flyer waste paper, office waste paper, corrugated waste paper, upper white waste paper, Kent waste paper, imitation waste paper, old paper waste paper, etc. Examples thereof include disintegrated waste paper pulp, disaggregated / deinked waste paper pulp (DIP), and disaggregated / deinked / bleached waste paper pulp.

  However, since the ionic variation (anionization) of the raw material pulp due to the mechanical pulp derived from the used paper pulp adversely affects the yield and dispersibility of the silica composite heavy calcium carbonate, the content of the used paper pulp in the raw material pulp is 30 It is particularly preferable that the amount is not more than mass%, and it is not included. By making the content of used paper pulp in the raw material pulp below the above upper limit or not using the used paper pulp, uniform dispersibility and formation of the silica composite heavy calcium carbonate particles of the printing paper can be improved. , Curling can be suppressed. Further, the dimensional stability and printability of the printing paper can be improved, and a printing paper having excellent workability can be obtained along with curling improvement.

<Filler>
The printing paper contains silica composite heavy calcium carbonate particles as a filler. In addition to the silica composite heavy calcium carbonate particles, the printing paper can contain a filler conventionally used in papermaking applications. For example, the printing paper includes talc, light calcium carbonate, heavy calcium carbonate. Further, kaolin, titanium dioxide, white carbon, regenerated particles, regenerated particles obtained by dehydration, combustion, and pulverization using deinked floss as raw materials, composite regenerated particles of silica combined with regenerated particles, and the like may also be included.

  When the silica composite heavy calcium carbonate particles are used as a filler, the content of the silica composite heavy calcium carbonate particles with respect to the total amount of the filler is preferably 50% by mass or more and 100% by mass or less, and 60% by mass or more and 90% by mass. The mass% or less is more preferable. When the content of silica composite heavy calcium carbonate particles is less than the above lower limit, curl suppression and dispersion to raw pulp due to moisture retention (surface moisture retention time) and parallel moisture content caused by silica composite heavy calcium carbonate particles There is a risk that the effect of improving the property is reduced. On the other hand, when the content of the silica composite heavy calcium carbonate particles exceeds the above upper limit, the uniform dispersibility in the slurry is lowered, and there is a possibility that the yield improving effect and the curling generation suppressing effect are lowered.

<Silica composite heavy calcium carbonate particles>
The silica composite heavy calcium carbonate particles include heavy calcium carbonate particles and silica that covers at least a part of the surface of the heavy calcium carbonate particles.

  The silica composite heavy calcium carbonate particles may be composited only with silica, but it is more preferable that aluminum oxide is composited in addition to silica. Since aluminum oxide is cationic, silica composite heavy calcium carbonate combined with aluminum oxide is self-fixing to anionic pulp raw materials, and the yield of silica composite heavy calcium carbonate when added to pulp raw materials Is easy to improve. Moreover, since the average particle diameter of a silica composite heavy calcium carbonate becomes a sharp particle size distribution, it is easy to disperse | distribute uniformly. Therefore, the anisotropy of the degree of drying of the printing paper can be suppressed, and curling can be effectively suppressed. Since the silica composite heavy calcium carbonate particles improve the yield and dispersibility with respect to the raw material pulp and have a sharp particle size distribution as described above, the difference between the front and back of the printing paper can be reduced. When the silica composite heavy calcium carbonate particles are not contained, the yield with respect to the raw material pulp is deteriorated and it is easy to come out of the wire during paper making, and the dispersibility with respect to the raw material pulp is not improved, so that the difference between the front and back of the printing paper is increased. Moreover, the manufacturing method of the silica composite heavy calcium carbonate particle | grains which compounded this aluminum oxide is explained in full detail behind.

  The volume average particle diameter (D50) measured by the laser diffraction scattering method of the silica composite heavy calcium carbonate particles (hereinafter also including aluminum oxide composite) is preferably 2 μm or more and 15 μm or less, preferably 3 μm or more and 10 μm. The following is more preferable, and 3.5 μm or more and 8 μm or less is more preferable. When the average particle diameter of the silica composite heavy calcium carbonate particles is less than the above lower limit, the yield improving effect of the silica composite heavy calcium carbonate particles is not sufficiently exhibited, and the curl suppressing effect may be hardly exhibited. Conversely, when the volume average particle size of the silica composite heavy calcium carbonate particles exceeds the above upper limit, the large particle size decreases the uniform dispersibility in the slurry, and also reduces the curl generation suppressing effect. There is a possibility that opacity and oil absorption may not be sufficiently obtained.

  The silica ratio in terms of oxide in the silica composite heavy calcium carbonate particles is preferably 1% by mass to 30% by mass, and more preferably 5% by mass to 20% by mass. When the ratio of silica is less than the above lower limit, the surface of the silica composite heavy calcium carbonate particles is not sufficiently coated, so the porosity of the silica composite heavy calcium carbonate particles becomes low, and the moisture retention time and parallel moisture content are low. There is a possibility that the curling effect will be reduced and the whiteness and oil absorption may be reduced. Conversely, when the silica ratio exceeds the above upper limit, it is difficult to obtain an irregular shape due to heavy calcium carbonate or a sharp particle size distribution due to the silica composite, and the curl suppression effect that the present invention is subject to may be reduced. There is.

  As a more effective configuration in the present invention, the aluminum oxide content in the case where aluminum oxide is combined with the silica composite heavy calcium carbonate particles is preferably 8% by mass or more and 38% by mass or less, and more preferably 10% by mass or more and 20% by mass. The mass% or less is more preferable. When the content of aluminum oxide is less than the above lower limit, the effect of improving the cationic property of the silica composite heavy calcium carbonate particles combined with aluminum oxide is hardly obtained, and the effect of improving the dispersibility is reduced, and the effect of suppressing curling is reduced. In addition, there is a possibility that the yield improvement effect upon addition of silica composite heavy calcium carbonate particles may not be sufficiently obtained. On the contrary, when the content of aluminum oxide exceeds the above upper limit, not only is the cost high, but the original effect of silica composite heavy calcium carbonate is inhibited, the dispersibility to the raw material pulp is reduced, and The fixing effect may be reduced. In addition, the content rate of aluminum oxide can be measured by, for example, an X-ray analysis method.

  The amount of the silica composite heavy calcium carbonate particles added to the pulp slurry is 12% or more and 22% or less based on JIS-P8251 (2003) of the obtained printing paper. It is preferable. When the addition amount of the silica composite heavy calcium carbonate particles is less than the above lower limit, the curl generation suppressing effect may be reduced, or the yield improving effect when the silica composite heavy calcium carbonate particles are added may not be sufficiently obtained. . On the contrary, when the addition amount of the silica composite heavy calcium carbonate particles exceeds the above upper limit, the adhesiveness between the pulp fibers is lowered, and the strength of the paper may be lowered.

  In addition to the above-mentioned printing paper, for example, starch, polyacrylamide, epichlorohydrin and other paper strength enhancers, rosin, alkyl ketene dimer, ASA (alkenyl succinic anhydride), neutral rosin and other internal sizing agents, sulfate bands , Coagulants such as polyethyleneimine, and coagulants such as polyacrylamide and copolymers thereof.

<Coating>
A clear coating solution used in combination with a surface sizing agent or a paper strength improver may be applied to both sides of the printing paper. By performing such clear coating, the flexibility and printability of the printing paper can be increased.

  The surface sizing agent is not particularly limited and includes, for example, starch, styrene sizing agent, acrylate sizing agent, alkyl ketene dimer, etc. Among them, starch, styrene sizing agent and acrylate sizing agent can be mentioned. Sizing agent is preferred, starch is particularly preferred, among them oxidized starch, hydroxyethylated starch, cationized starch, cationized oxidized starch, acetylated starch, esterified starch, heat-denatured starch, enzyme-modified starch, aldehyde-modified starch, etc. It is preferable to select and use a starch having a B-type viscosity of 60 mPa · s at 60 rpm when the concentration is 10% and the liquid temperature is 30 ° C. Alternatively, these generally available modified starches are further subjected to low molecular weight treatment by known methods such as enzyme modification and oxidation modification, and the B-type viscosity at 60 rpm is 100 mPa · s or less when the concentration is 10% and the liquid temperature is 30 ° C. Is preferably used in order to provide a printing paper that can effectively suppress the occurrence of curling, which is the subject of the present invention, without impairing the properties of the silica composite heavy calcium carbonate.

  The paper strength improver is not particularly limited. For example, polyacrylamide (PAM), polyvinyl alcohol (PVA), acrylic resin, polyamide / polyamine resin, urea / formalin resin, melamine / formalin resin, polyethylene Among them, PAM, acrylic resin and PVA are preferable, and PAM is more preferable. Polyacrylamide is not limited to ionicity, polymerization degree, carboxyl group content, etc., but when used as a clear coating liquid with the above surface sizing agent, the ratio of the surface sizing agent to the paper strength improver is 2: 1. From 4: 1, the combined use at a ratio of 4: 1 suppresses the film property resulting from PAM while maintaining the effect of PAM, and does not hinder the properties of silica-composite heavy calcium carbonate. Is preferable in providing a printing paper capable of effectively suppressing the above.

The coating amount of the coating liquid in the coating is not particularly limited, in terms of solid content, preferably per side 0.1 g / ^{m 2} or more 1 g / ^{m 2} or less, 0.3 g / ^{m 2} or more 0. 7 g / m ² or less is more preferable. When this coating amount is less than the above lower limit, the above-described effects of the coating are not sufficiently exhibited, and when there is unevenness in moisture retention and parallel moisture content on the surface of the printing paper due to uneven coating, printability is reduced. There is a case. On the other hand, when the coating amount exceeds the above upper limit, the coating property of the surface of the printing paper is increased by this coating, the water retention property of the printing paper surface and the parallel moisture content are deteriorated, and the curl generation suppressing effect is reduced. In some cases, the surface strength is increased, the flexibility is lowered, and the printability is lowered.

<Printing paper manufacturing method>
The method for producing the printing paper is not particularly limited, and a known method for producing printing paper may be used. Specifically, for example, a paper pulp slurry is made, subjected to a press part and a predryer part, and then subjected to a calendar process.

  The printing paper can also be used as a coated paper by providing a coating layer on one side or both sides.

<Quality etc.>
The basis weight of the printing paper is preferably 50 g / m ² or more and 100 g / m ² or less, and more preferably 60 g / m ² or more and 80 g / m ² or less in order to effectively exhibit the curl suppressing effect based on the present invention. . When the basis weight is less than the above lower limit, curling problems hardly occur, but the feel of paper becomes soft and workability may be reduced. On the other hand, if the basis weight exceeds the above upper limit, the printing paper becomes tough and the effect of the present invention is hardly exhibited, and it goes against the recent weight saving and resource saving.

  The ash content of the printing paper is preferably 12% or more and 22% or less, and more preferably 14% or more and 20% or less. When the ash content is less than the above lower limit, the effect of the silica composite heavy calcium carbonate in the present invention cannot be effectively expressed, and there is a possibility that the printing opacity may be lowered, or the water retention property is lowered and the curl suppressing effect may be impaired. is there. On the other hand, when the ash content exceeds the above upper limit, although the printing opacity is increased, there is a risk that the strength of the paper may be reduced due to a decrease in the adhesion between the pulp fibers, or the silica composite heavy calcium carbonate in the raw material pulp. Uniform dispersion is impaired, moisture retention is uneven, curling suppression effect is impaired, and printability may be reduced.

  The thickness of the printing paper is preferably 56 μm or more and 143 μm or less. If the paper thickness is less than the above lower limit, the tensile strength may decrease. On the other hand, when the paper thickness exceeds the above upper limit, there is a risk that it is against the request for weight reduction. The paper thickness is a value measured according to JIS-P8118 (1998).

The density of the printing paper is preferably 0.7 g / cm ³ or more and 0.9 g / cm ³ or less, and more preferably 0.75 g / cm ³ or more and 0.85 g / cm ³ or less. If the density is less than the above lower limit, there is a risk of show-through when printing on the printing paper. On the other hand, if the density exceeds the above upper limit, the stiffness may be reduced and printability may be reduced. The density is a value measured according to JIS-P8118 (1998).

  The printing paper has a moisture retention time on the front and back surfaces of 800 seconds or more, and a moisture retention time difference between the front and back surfaces of the printing paper is within 80 seconds. Furthermore, the moisture retention time on the surface of the printing paper is preferably 900 seconds to 1200 seconds, and more preferably 950 seconds to 1150 seconds. When the moisture retention time on the surface is less than the above lower limit, curling may easily occur on the printing paper. On the other hand, when the moisture retention time on the surface exceeds the above upper limit, the printability of the printing paper may be reduced.

  The printing paper has a difference in moisture retention time between the front and back surfaces of 80 seconds or less. Further, the difference in moisture retention time between the front surface and the back surface of the printing paper is preferably within 60 seconds, and more preferably within 40 seconds. Since the moisture retention time difference between the front surface and the back surface is within 80 seconds, the moisture contained in the front and back surfaces is dried at an equivalent drying speed, so that anisotropy associated with the degree of drying on the front and back surfaces is improved. On the other hand, when the difference in moisture retention time between the front surface and the back surface exceeds the upper limit, the printing paper may be easily curled.

  The equilibrium moisture content of the printing paper is preferably adjusted to be 5% or more and 10% or less by adjusting the content of silica composite heavy calcium carbonate as a filler, and is preferably 6% or more and 8% or less. It is further preferable to adjust to. When the equilibrium moisture content is less than the above lower limit, the moisture retention of the printing paper is lowered, and curling may occur easily. On the other hand, when the equilibrium moisture content exceeds the above upper limit, the moisture retention becomes too high, and the printability of the printing paper may be reduced. The equilibrium moisture content is the weight of the printing paper when the humidity is adjusted to a constant weight under the standard conditions (temperature 23 ° C., humidity 50%) defined in JIS-P8111 (1998). This is a value obtained from (W1−W2) / W2 × 100, where W2 is the mass of the printing paper when it becomes a constant weight after drying at 105 ° C. according to P8127 (2010).

  The average curl height of the printing paper obtained by the configuration of the present invention can be adjusted to 1.5 mm or less, preferably 1 mm or less, more preferably 0.5 mm or less. When the average curl height exceeds the above upper limit, paper feedability (printing workability) and printability in offset printing may be deteriorated. The average curl height means that the printing paper cut into a 100 mm square with the paper making direction as one side is placed on a flat surface so that the convex side comes into contact in an environment of temperature 23 ° C. and humidity 50%. The average height of the four corners measured.

  The whiteness of the printing paper is preferably 80% to 95%, more preferably 83% to 95%, and still more preferably 84% to 95% so as not to cause eye strain of the subscriber. The whiteness is a value measured according to JIS-P8148 (2001).

  The lower limit of the printing opacity of the printing paper is preferably 83%, more preferably 84%, and still more preferably 85%. Printing paper having such printing opacity can be obtained by the uniform dispersibility of the silica composite heavy calcium carbonate. On the other hand, the upper limit of the printing opacity of the printing paper is preferably 96%. If the printing opacity is less than the above lower limit, there is a risk that show-through is likely to occur. On the other hand, if the printing opacity exceeds the above upper limit, the required pigment increases and the surface strength of the printing paper becomes weak, which may increase the paper dust at the time of printing due to the dropout of the pigment and the appearance of the printing paper. May get worse. The printing opacity is determined by JAPAN TAPPI No. It is a value measured according to 45.

<Method for producing silica composite heavy calcium carbonate particles>
Hereinafter, a method for producing silica composite heavy calcium carbonate particles used for the printing paper will be described in detail.

  The silica composite heavy calcium carbonate particles used for the printing paper are composites of heavy calcium carbonate particles and silica. Specifically, the silica is combined with the heavy calcium carbonate particles with a silicic acid alkali salt and mineral acid. Obtained by the process.

  Further, it is preferable that the silica composite heavy calcium carbonate particles are further combined with aluminum oxide using an aluminum salt. Since the silica composite heavy calcium carbonate particles contain a large amount of cationic aluminum, the silica composite heavy calcium carbonate particles combined with aluminum oxide have a self-fixing property to an anionic pulp raw material. It is easy to disperse uniformly when added to the raw material. Therefore, by combining aluminum oxide, the curl can be suppressed more effectively, and the yield to the raw material pulp is high and the whiteness and the like can be improved while suppressing the thickening of the pulp slurry. -Aluminum oxide composite heavy calcium carbonate particles can be obtained. Although it does not specifically limit as this aluminum salt, For example, a sulfuric acid band (aluminum sulfate), sodium aluminate, etc. can be used. Among these, sodium aluminate that can reduce the viscosity of the slurry when added to the pulp slurry without decomposing calcium carbonate particles and generating calcium oxide is particularly preferable.

The silica composite heavy calcium carbonate particles that can be suitably used for the printing paper are, for example,
(1) Particle condensing step for condensing calcium carbonate particles with a coagulant,
(2) A slurry preparation step for obtaining a slurry containing calcium carbonate particles and an alkali silicate salt,
(3) A first reaction step of adding a mineral acid to the slurry, and (4) a second reaction step of adding sodium aluminate and a mineral acid to the slurry.

  The apparatus of FIG. 1 used in the method for producing silica composite heavy calcium carbonate particles includes a condensation reaction tank 1, a first silica composite reaction tank 2, a second silica composite reaction tank 3, a first aluminum treatment reaction tank 4, A dialuminum treatment reaction tank 5 and a storage tank 6 are provided in this order.

  As the heavy calcium carbonate particles X1, which are the raw materials for the silica composite heavy calcium carbonate particles, heavy calcium carbonate particles ground in advance into fine particles are used. The heavy calcium carbonate particles X1 may be combined with silica as it is, but it is preferable that the heavy calcium carbonate particles X1 are aggregated by the coagulant G in the condensation reaction tank 1 to form the heavy calcium carbonate particle aggregate X2. The heavy calcium carbonate particle aggregate X2 is subjected to the first reaction step in the first silica composite reaction vessel 2 and the second silica composite reaction vessel 3 after the slurry adjustment step is performed in the first silica composite reaction vessel 2. It becomes the silica composite heavy calcium carbonate particle X3 in which the silica is composited. Thereafter, the silica composite heavy calcium carbonate particles X3 are subjected to the second reaction step in the first aluminum treatment reaction tank 4 and the second aluminum treatment reaction tank 5, and the silica composite heavy calcium carbonate particles X4 composited with aluminum oxide. And stored in the storage tank 6.

  As the heavy calcium carbonate particles X1, heavy calcium carbonate particles obtained by mechanically pulverizing natural limestone dry or wet are used. Heavy calcium carbonate is inexpensive to produce, but because it is manufactured by physical pulverization, it has an irregular and broad particle size distribution, so it has high wire wear and is used as a filler for internal addition. However, the composite particles can reduce the wear of the wire in the paper making process and can be suitably used as a filler for the printing paper.

  In this production method, it is preferable to perform a particle size adjusting step for adjusting the volume average particle size of the heavy calcium carbonate particles X1 to a range suitable for condensation and silica and aluminum oxide composite. In this particle size adjusting step, pulverization, classification, and the like are performed so that the volume average particle size of the heavy calcium carbonate particles X1 falls within a suitable range. As a pulverizer used as a means for pulverizing the heavy calcium carbonate particles X1, for example, a dry pulverizer such as a jet mill or a high-speed rotary mill, or a wet pulverizer such as an attritor, a sand grinder or a ball mill can be used. .

  The volume average particle diameter of the heavy calcium carbonate particles X1 is not particularly limited, but the lower limit is preferably 0.2 μm, and more preferably 1.0 μm. On the other hand, the upper limit of the volume average particle diameter of the heavy calcium carbonate particles X1 is preferably 10.0 μm, and more preferably 5.0 μm. When the volume average particle size of the heavy calcium carbonate particles X1 is less than the above lower limit, in order to obtain a coagulation having a sufficient particle size, agglomeration with a large number of particles is necessary and the coagulation becomes brittle. There is a possibility that the aggregates collapse and the yield of the composite particles cannot be obtained sufficiently. On the contrary, when the volume average particle diameter of the heavy calcium carbonate particles X1 exceeds the above upper limit, the particle size distribution of the heavy calcium carbonate particles X1 becomes broad, and a sharp particle size distribution cannot be obtained even when condensation is performed. As a result, there is a possibility that the silica composite effect and the aluminum composite effect due to the aluminum salt may be insufficient, and the paper containing the silica composite heavy calcium carbonate particles obtained by this production method due to the presence of coarse particles is added. There is a risk that the quality may not be sufficient. In addition, the volume average particle diameter of the heavy calcium carbonate particles X1 is a sample (heavy calcium carbonate particles X1) using a laser diffraction particle size distribution meter (manufactured by Nikkiso Co., Ltd., model number: Microtrack MTII-3000). The particle size distribution is measured, the particle diameter (D50) when the cumulative volume with respect to the volume of all particles is 50% is determined, and this particle diameter is defined as the volume average particle diameter.

[(1) Particle condensation step]
(1) In the particle condensation step, the heavy calcium carbonate particles X1 are obtained by coagulating the heavy calcium carbonate particles X1 with the coagulant G in the condensation reaction tank 1.

  The coagulant G used in the present production method is not particularly limited, and a known synthetic coagulant can be used, but it is cationic that easily causes the heavy calcium carbonate particles X1 to coagulate to an appropriate particle size. A coagulant is preferred. As this cationic coagulant, for example, diallyldimethylammonium chloride, cationic polyacrylamide and the like can be used.

  The lower limit of the mass average molecular weight of the coagulant G is preferably 100,000, and more preferably 200,000. On the other hand, the upper limit of the mass average molecular weight of the coagulant G is preferably 1.5 million, and more preferably 800,000. By setting the molecular weight of the coagulant G within the above range, the heavy calcium carbonate particles X1 can be suitably coagulated. When the mass average molecular weight of the coagulant G is less than the above lower limit, sufficient coagulation force may not be obtained. On the contrary, when the mass average molecular weight of the coagulant G exceeds the above upper limit, a heavy calcium carbonate particle aggregate X2 having an excessively large particle size is formed, and the particle size distribution may be broadened to reduce the yield, When the coagulant G is added to the slurry of the heavy calcium carbonate particle aggregate X2, the viscosity becomes too high and workability and yield may be reduced. In particular, when the viscosity of the slurry of the heavy calcium carbonate particle aggregate X2 exceeds 500 cps, the load of the pump for transferring the slurry of the heavy calcium carbonate particle aggregate X2 may increase, There is a possibility that the miscibility with the pulp raw material is lowered. In addition, there is a possibility that inconveniences in which dirt in the papermaking system becomes obvious. The mass average molecular weight is a numerical value measured using a gel permeation chromatography method (GPC method).

  Further, the lower limit of the cationic charge density of the coagulant G is preferably 3 meq / g, more preferably 5 meq / g. On the other hand, the upper limit of the cation charge density is preferably 25 meq / g, more preferably 20 meq / g. By setting the cationic charge density of the coagulant G within the above range, the heavy calcium carbonate particles X1 can be suitably coagulated. When the cationic charge density of the coagulant G is less than the above lower limit, there is a possibility that sufficient coagulation force cannot be obtained. On the contrary, when the cationic charge density of the coagulant G exceeds the above upper limit, the entire surface of the heavy calcium carbonate particles X1 has a cationic charge, which may make it difficult for condensation to occur due to repulsion due to charge. There is a risk that the heavy calcium carbonate particle aggregate X2 having a large particle size is formed, the particle size distribution becomes broad, and the yield decreases. In addition, this cation charge density says the cation charge density as the whole coagulant, when using a some component as a coagulant.

In the present invention, the cationic charge density is a value measured by the following method. First, after adjusting the sample to an aqueous solution of pH 4.0, the amount of anion required by titration using a 1/1000 normal aqueous potassium potassium sulfate solution with a particle charge measuring device (Muteck PCD-03) based on the streaming potential method. Measure. The cation charge density (meq / g) per 1 g of sample is calculated by the following formula (1) using the obtained anion demand.
Cationic charge density = A / B × 1000 (1)
A: Anion requirement of the aqueous coagulant solution adjusted to pH 4.0 (μeq / l)
B: Solid content concentration of coagulant aqueous solution (g / l)

  In this way, in the coagulation of the heavy calcium carbonate particles X1, it is possible to use the coagulant G having the above-mentioned preferable ranges in both the mass average molecular weight and the cation charge density. It is preferable because both of the above and the thickening suppression of the slurry can be suitably achieved. The reason for this is not clear, but for example, the reason for the aggregation is that there is variation in the charge distribution on the surface of the heavy calcium carbonate particles X1, so that a cationic synthetic polymer having a molecular weight and a cation charge density within a predetermined range is used. It is thought that it is because an electric coagulation action can be exhibited by using.

  The method for coagulating the heavy calcium carbonate particles X1 with the coagulant G is not particularly limited. For example, the heavy calcium carbonate particles X1 are dispersed in water to form a heavy calcium carbonate particle slurry. A method in which the coagulant G is added to the fine calcium carbonate particle slurry and stirred can be used. As a stirring device used at this time, for example, a propeller blade, a turbine blade, a paddle blade, or the like can be used.

  When using the method of adding the coagulant G to the heavy calcium carbonate particle slurry described above, the solid content concentration of the heavy calcium carbonate particle X1 in the heavy calcium carbonate particle slurry is not particularly limited, 10 mass% or more and 30 mass% or less are preferable. By making the density | concentration of a heavy calcium carbonate particle slurry into the said range, coexistence with efficiency improvement of the heavy calcium carbonate particle X1 and suppression of a raise of slurry viscosity can be aimed at. When the concentration of the heavy calcium carbonate particle slurry is less than the above lower limit, even if the coagulant G is added, the heavy calcium carbonate particle X1 may not be condensed to a suitable size. Conversely, when the concentration of the heavy calcium carbonate particle slurry exceeds the above upper limit, the viscosity is too high and workability is reduced, or the particle size distribution of the heavy calcium carbonate particle aggregate X2 becomes broad, Yield may be reduced.

  The coagulant G is preferably added as an aqueous solution to the heavy calcium carbonate particle slurry. Further, the amount of the coagulant G added is preferably 100 ppm or more and 3000 ppm or less in terms of solid content with respect to the solid content of the heavy calcium carbonate particles X1. When the addition amount of the coagulant G is less than the lower limit, the heavy calcium carbonate particles X1 cannot be sufficiently aggregated, and the yield improvement effect may not be exhibited. On the contrary, when the addition amount of the coagulant G exceeds the above upper limit, the thickening of the slurry may occur remarkably, and tertiary and quaternary aggregation may occur, and the silica composite heavy calcium carbonate particles obtained by this production method may be reduced. The paper strength of the added paper may be reduced.

  The volume average particle diameter of the heavy calcium carbonate particle aggregate X2 obtained through the particle aggregation step is preferably 1.1 to 10.0 times the volume average particle diameter of the heavy calcium carbonate particle X1. 2 times or more and 8.0 times or less are more preferable, and 1.3 times or more and 6.0 times or less are particularly preferable. Further, the lower limit of the volume average particle diameter of the heavy calcium carbonate particle aggregate X2 is preferably 0.45 μm, more preferably 1.0 μm, and particularly preferably 1.2 μm. On the other hand, the upper limit of the volume average particle diameter of the heavy calcium carbonate particle aggregate X2 is preferably 10.5 μm, more preferably 8.4 μm, and particularly preferably 6.2 μm. By making the volume average particle diameter of the heavy calcium carbonate particle aggregate X2 in the above range, the yield of the silica composite heavy calcium carbonate particles obtained in the production process can be efficiently improved. When the volume average particle diameter of the heavy calcium carbonate particle aggregate X2 is less than 1.1 times the volume average particle diameter of the heavy calcium carbonate particle X1 or less than 0.45 μm, the particle size sufficient when combining silica and aluminum oxide In addition to the possibility of being obtained, there is a risk of clogging in the form of glass when silica is combined. Conversely, when the volume average particle diameter of the heavy calcium carbonate particle aggregate X2 exceeds 10.0 times the volume average particle diameter of the heavy calcium carbonate particle X1, the aggregate becomes brittle. There is a possibility that the yield of the silica composite heavy calcium carbonate particles obtained by this production method may not be sufficiently obtained. Moreover, when the volume average particle diameter of the heavy calcium carbonate particle aggregate X2 exceeds 10.5 μm, the particle diameter of the silica composite heavy calcium carbonate particles obtained by this production method is increased and enters the gaps between the pulp fibers. Otherwise, the opacity of the added paper may be reduced. In addition, the volume average particle diameter of the heavy calcium carbonate particle aggregate X2 can be adjusted by the addition amount of the coagulant G, the volume average particle diameter of the heavy calcium carbonate particle X1, and the like.

[(2) Slurry preparation step]
(2) In the slurry preparation step, a slurry containing the heavy calcium carbonate particle aggregate X2 and the alkali silicate is prepared. This slurry may be prepared, for example, by adding the alkali silicate solution L to the slurry containing the heavy calcium carbonate particle aggregate X2 obtained in the above-described particle condensing step. You may prepare by adding the body X2 to the alkali silicate solution L, and making it disperse | distribute.

  The alkali silicate solution L used in this production method is not particularly limited, but it is preferable from the viewpoint of availability to use a sodium silicate solution (No. 3 water glass).

  As a minimum of silicic acid concentration in silicic acid alkali solution L, 6 g / L is preferred, 8 g / L is still more preferred, and 10 g / L or less is especially preferred. On the other hand, the upper limit of the silicic acid concentration is preferably 18 g / L, more preferably 16 g / L, and particularly preferably 14 g / L. When the silicic acid concentration is less than the above lower limit, the silica sol is not sufficiently formed, and there is a possibility that a heavy calcium carbonate particle aggregate X2 in which silica is not combined is generated. On the contrary, when the silicic acid concentration exceeds the above upper limit, white carbon is generated instead of silica sol, and the heavy calcium carbonate particle aggregate X2 is coated with white carbon, so that the porous calcium carbonate particle aggregate X2 is porous. Therefore, the whiteness, opacity and oil absorption of the silica composite heavy calcium carbonate particles obtained by this production method may be reduced.

  In this step, the lower limit of the concentration of the heavy calcium carbonate particle aggregate X2 in the slurry containing the heavy calcium carbonate particle aggregate X2 and the alkali silicate is preferably 95 g / L, more preferably 100 g / L, and 105 g. / L is particularly preferred. On the other hand, the upper limit of the concentration of the heavy calcium carbonate particle aggregate X2 is preferably 125 g / L, more preferably 120 g / L, and particularly preferably 115 g / L. When the density | concentration of the heavy calcium carbonate particle aggregate X2 is less than the said minimum, there exists a possibility that a silica production | generation reaction may become dull and the productivity of a composite particle may deteriorate. On the other hand, when the concentration of the heavy calcium carbonate particle aggregate X2 exceeds the upper limit, the viscosity of the slurry may increase and the dispersibility of the heavy calcium carbonate particle aggregate X2 may decrease.

As the silicic acid concentration in the slurry (SiO ₂ conversion) is preferably 5 mass% to 15 mass%. When the silicic acid concentration is less than the lower limit, the silica composite effect is weakened, and the effect of improving the whiteness, opacity and oil absorption of the silica composite heavy calcium carbonate particles obtained by the present production method may be reduced. On the contrary, when the silica concentration exceeds the upper limit, the absorption capacity of the paper coating liquid to which the silica composite heavy calcium carbonate particles obtained by this production method are added is increased, and thus a coating layer is provided. In addition, the flatness of the coating layer surface may be reduced.

  The temperature of the alkali silicate solution L when the alkali silicate solution L is added to the heavy calcium carbonate particle aggregate X2-containing slurry or when the heavy calcium carbonate particle aggregate X2 is added to the alkali silicate solution L is particularly limited. Although not, it is preferably 50 ° C. or higher. When the heavy calcium carbonate particle aggregate X2 is mixed in a state where the alkali silicate solution L is heated to 50 ° C. or higher, the slurry can be easily homogenized by improving the fluidity.

[(3) First reaction step]
(3) In the first reaction step, silica composite heavy calcium carbonate in which mineral acid N is added to the slurry, the pH of the slurry is lowered, and silica is precipitated on the surface of the heavy calcium carbonate particle aggregate X2. Particle X3 is obtained.

  Specifically, in this step, while heating and stirring so that the liquid temperature of the slurry is 50 to 90 ° C., the slurry is held at a predetermined pressure in a sealed container, and the alkali silicate solution L contained in the slurry is 20 to 50. % Mineral acid N is added in an amount to be neutralized. As a result, alkali silicate, which is a raw material of silica, reacts with a dilute solution of mineral acid N such as sulfuric acid, hydrochloric acid, and nitric acid at high temperature, and silica sol fine particles are generated by hydrolysis reaction and polymerization of silicic acid. It precipitates on the surface of the calcium particle aggregate X2. The particle size of the silica sol fine particles can be adjusted by the stirring conditions during the reaction, the addition conditions of the mineral acid N, and the like. Then, by attaching the silica sol fine particles of about several nanometers so as to cover the entire surface of the heavy calcium carbonate particle aggregate X2, silica sol crystals grow, and the silica sol on the surface of the heavy calcium carbonate particle aggregate X2 is grown. Bonding occurs between the fine particles and the calcium contained in the heavy calcium carbonate particle aggregate X2, and silica can be deposited on the surface of the heavy calcium carbonate particle aggregate X2. In this production method, since the silica is coated on the surface of the heavy calcium carbonate particle aggregate X2, the calcium oxide contained in the heavy calcium carbonate particle aggregate X2 reacts with calcium hydroxide in water. It is considered that the viscosity of the slurry can be suppressed by suppressing.

  The mineral acid N used in this production method is not particularly limited, and for example, sulfuric acid, hydrochloric acid, nitric acid and the like can be used. Among these, sulfuric acid is particularly preferable from the viewpoint of cost and handling.

  As a density | concentration of the mineral acid N used in this manufacturing method, 0.1 mol / L or more and 5.0 mol / L or less are preferable. When the concentration of the mineral acid N is less than the above lower limit, the generation rate of silica is slow, and there is a possibility that the silica is not sufficiently formed. On the other hand, when the concentration of the mineral acid N exceeds the above upper limit, a local reaction occurs, silica is unevenly formed, and the curl generation suppressing effect may be reduced. The yield improvement effect of calcium carbonate particles may be reduced.

  The temperature of the slurry during stirring in this step is preferably 50 ° C. or higher and 90 ° C. or lower. Since the temperature of the slurry affects the generation and growth of the silica sol, if the temperature of the slurry is less than the lower limit, silica may not be generated, or the generation and growth rate of the silica sol is slowed down and the silica has sufficient strength. Since it is not combined with the heavy calcium carbonate particle aggregate X2, silica may be peeled off during papermaking. On the contrary, when the temperature of the slurry exceeds the above upper limit, it becomes difficult to produce, and since silica is densely formed on the surface of the heavy calcium carbonate particle aggregate X2, oil absorption of the silica composite heavy calcium carbonate particles The degree may decrease.

  The pH of the slurry in this step is preferably 8 or more and 11 or less. When pH is less than the said minimum, a silica precipitates heterogeneously and there exists a possibility that the whiteness, opacity, and oil absorption of the silica composite heavy calcium carbonate particle obtained by this manufacturing method may fall. On the other hand, when the pH exceeds the above upper limit, the reaction between the alkali silicate salt and the mineral acid becomes dull and it becomes difficult for silica to be precipitated on the surface of the heavy calcium carbonate particle aggregate X2. The opacity of the composite heavy calcium carbonate particles may be reduced.

  In this step, it is preferable to add mineral acid N to the slurry in two stages in order to suppress precipitation of white carbon and more uniformly precipitate silica on the surface of the heavy calcium carbonate particle aggregate X2. In this case, mineral acid N is added in such an amount that the alkali silicate solution L contained in the slurry is neutralized by 20 to 50% in the first stage, and then the liquid temperature is raised by 10 ° C. or more than in the first stage. By adding the mineral acid N so that the pH of the reaction solution is 8 or more and 11 or less, homogeneous silica composite heavy calcium carbonate particles X3 can be obtained.

[(4) Second reaction step]
(4) In the second reaction step, sodium aluminate A and mineral acid N are added to the slurry, and aluminum oxide is precipitated on the surface of the silica composite heavy calcium carbonate particles X3, thereby combining the aluminum oxide with the silica composite. Heavy calcium carbonate particles X4 are obtained. In addition, this process can be abbreviate | omitted when obtaining the composite particle which compounded only silica.

  Specifically, in this step, as in the first reaction step, while the slurry is heated and stirred, the slurry is maintained at a predetermined pressure in a sealed container, and sodium aluminate A and mineral acid N are added. Thereby, aluminum oxide is deposited on the outer layer of silica deposited on the surface of the silica composite heavy calcium carbonate particles X3 obtained in the first reaction step. As a result, silica composite heavy calcium carbonate particles X4 in which the surface is composited with cationic aluminum oxide are obtained.

  In this step, it is preferable to add mineral acid N after adding sodium aluminate A to the slurry. Thus, by adding sodium aluminate A first and then neutralizing by adding mineral acid N, aluminum oxide can be uniformly deposited on the outer layer of silica. Further, it is more preferable to add the mineral acid N to the slurry in two stages in order to precipitate aluminum oxide more uniformly on the surface of the silica composite heavy calcium carbonate particles X3.

  The second reaction step is preferably performed after about 5 to 20 minutes have elapsed after the addition of the mineral acid N in the first reaction step. By providing the reaction holding period in this manner, silica can be uniformly deposited on the surface of the heavy calcium carbonate particle aggregate X2 in advance before the second reaction step.

  As a minimum of the addition amount of sodium aluminate A, 10 mass parts is preferable with respect to 100 mass parts of heavy calcium carbonate particles, 12 mass parts is further more preferable, and 15 mass parts is especially preferable. On the other hand, as an upper limit of the addition amount of sodium aluminate A, 30 mass parts is preferable, 25 mass parts is more preferable, and 22 mass parts is especially preferable. When the amount of sodium aluminate A added is less than the lower limit, aluminum oxide is not sufficiently combined with the silica composite heavy calcium carbonate particles X3, the binding strength with the pulp raw material is weakened, and the yield improvement effect is not exhibited. There is. Conversely, when the amount of sodium aluminate A added exceeds the above upper limit, the production cost is increased and the yield improvement effect may reach its peak.

  The final reaction solution in this step is preferably in the neutral to weakly alkaline range, and the pH is preferably 8 or more and 11 or less. When the pH is less than the above lower limit, the whiteness, opacity and oil absorption of the silica-composite heavy calcium carbonate particles obtained by this production method are deteriorated due to excessive addition of mineral acid, resulting in deterioration of the heavy calcium carbonate particles. There is a fear. Conversely, when the pH exceeds the above upper limit, the reaction between sodium aluminate A and mineral acid N becomes dull and it becomes difficult for aluminum oxide to precipitate on the surface of heavy calcium carbonate particles. There is a possibility that the opacity of the silica composite heavy calcium carbonate particles combined with aluminum may decrease.

  The slurry preparation step, the first reaction step, and the second reaction step can be performed by a batch method in which these steps are repeated for each predetermined processing amount, or in a continuous method in which each step is continuously performed. From this point of view, it is preferable to adopt a continuous type.

  When the slurry preparation step, the first reaction step, and the second reaction step are performed in a continuous manner, for example, the silica composite heavy calcium carbonate particles X4 combined with aluminum oxide can be manufactured according to FIG. 1 according to the following procedure. it can. In this procedure, mineral acid N is added in two stages in the first reaction step and the second reaction step. First, the heavy calcium carbonate particle aggregate X2, the alkali silicate solution L and the mineral acid N are continuously supplied to the first silica composite reaction tank 2, and these are stirred under a predetermined temperature and pressure, Part of the first reaction step is performed simultaneously. The slurry obtained in the first silica composite reaction tank 2 is continuously transferred to the second silica composite reaction tank 3. The mineral acid N is further added to the slurry transferred to the second silica composite reaction tank 3 and continuously transferred to the first aluminum treatment reaction tank 4. Since the second silica composite reaction tank 3 has a constant volume, generation and growth of silica proceeds until the slurry is transferred to the first aluminum treatment reaction tank 4, and the heavy calcium carbonate particle aggregate X2 Are continuously supplied to the first aluminum treatment reactor 4 as silica composite heavy calcium carbonate particles X3. Next, sodium aluminate A and mineral acid N are continuously supplied to the first aluminum treatment reaction tank 3, and these are mixed with the slurry of the silica composite heavy calcium carbonate particles X3 to produce the second reaction. Part of the process is performed. This slurry is continuously transferred to the second aluminum treatment reaction tank 5 and further added with the mineral acid N and then transferred to the storage tank 6. Since the second aluminum treatment reaction tank 5 has a certain volume, the reaction proceeds and aluminum oxide is deposited on the surface of the silica composite heavy calcium carbonate particles X3 until the slurry is transferred to the storage tank 6. Then, silica composite heavy calcium carbonate particles X4 composited with aluminum oxide are formed. The slurry containing the silica composite heavy calcium carbonate particles X4 combined with aluminum oxide is stored in a storage tank 6 and supplied to a papermaking production line as a filler, a pigment and the like.

  In addition, in this manufacturing method, addition of the mineral acid N is not performed in the 2nd silica composite reaction tank 3 and the 2nd aluminum treatment reaction tank 5, but addition of the mineral acid N in the 1st reaction process and the 2nd reaction process is 1 It may be done in stages. When the mineral acid N is added in one stage in the first reaction step, the mineral acid N may be added simultaneously with the alkali silicate solution L in the first silica composite reaction tank 2, or after the addition of the alkali silicate solution L, the second Mineral acid N may be added in the silica composite reaction tank 3. Similarly, when adding the mineral acid N in one stage in the second reaction step, the mineral acid N may be added simultaneously with the sodium aluminate A or the sodium aluminate A in the first aluminum treatment reaction tank 4. The mineral acid N may be added later in the second aluminum treatment reactor 5.

  Further, a slurry containing heavy calcium carbonate particles, alkali silicate solution and sodium aluminate may be prepared, and mineral acid may be added to the slurry to combine silica and aluminum oxide with the heavy calcium carbonate particles.

  EXAMPLES Hereinafter, the present invention will be described more specifically with reference to examples. However, the present invention is not limited to the following examples.

  In addition, each measured value in a present Example is the value measured with the following method.

[Volume average particle diameter of filler (unit: μm)]
A 10 mg sample of the filler for measuring the volume was dispersed for 3 minutes with an ultrasonic disperser (output: 80 W). Using this solution, the average particle size (D50) was measured with a laser particle size distribution measuring device (manufactured by Nikkiso Co., Ltd., model number: Microtrack MTII-3000).

[Basis weight (unit: g / m ² )]
It was measured according to “Paper and paperboard—basis weight measurement method” described in JIS-P8124 (2011).

[Paper thickness (unit: μm)]
It was measured in accordance with “Paper and paperboard—Test method for thickness and density” described in JIS-P8118 (1998).

[Ash content (unit:%)]
It was measured in accordance with “Paper, paperboard and pulp-ash content test method—525 ° C. combustion method” described in JIS-P8251 (2003).

[Ash yield (unit:%)]
The raw materials having the pulp composition, filler and ash conditions shown in Table 1 were used as specimens, diluted with tap water to a pulp concentration of 0.9% by weight, and the yield was measured with a Brit dynamic jar tester. Specifically, the measurement was performed according to the following procedure. First, the raw material was stirred at a rotation speed of 1000 rpm, and after 30 seconds from the start of stirring, white water was discharged for 10 seconds, and then white water was collected for 30 seconds. Next, the collected white water was filtered with a filter paper (wire 125P screen (corresponding to 200 mesh), ADVANTEC NO. 2). The filter paper was dried and then incinerated at 600 ° C., and the ash content was measured to calculate the filler yield.

[Moisture retention time for front and back surfaces (unit: seconds)]
In an environment of standard conditions (temperature 23 ° C., humidity 50%) in accordance with JIS-P8111 (1998), 90 μl of distilled water was dropped onto one side of A4 size printing paper to form a cylinder with a diameter of 1.5 cm. This is the time from when the film is stretched and applied with a glass rod and immediately after the water application to the mass of the paper after the water application becomes the mass of the paper before the water application.

[Equilibrium moisture content (unit:%)]
According to JIS-P8127 (2010), the mass (W1) of the printing paper when the humidity is adjusted to a constant weight in an environment of standard conditions (temperature 23 ° C., humidity 50%) specified in JIS-P8111 (1998) Then, the mass (W2) of the printing paper when it was dried at 105 ° C. and became a constant weight was measured, and the equilibrium moisture content was calculated by the following equation (2).
Equilibrium moisture content = (W1-W2) / W2 × 100 (%) (2)

[Curl height (unit: mm)]
In an environment with a temperature of 23 ° C and a humidity of 50%, print paper cut into a 100mm square with the paper making direction as one side is placed on a flat surface so that the convex side is in contact, and the measured average height of the four corners Was measured.

  In this example, the following qualities were evaluated.

(1) Printing workability Using an offset printing machine (manufactured by Komori Corporation, model number: Komori SYSTEMC-20), continuous 5000 copies were printed. At this time, the presence or absence of an uptake failure due to curling was visually observed, and the number of uptake failures was measured.

(Manufacture of silica composite heavy calcium carbonate particles)
Using coarsely crushed limestone, a bead mill was used to finely pulverize the volume average particle diameter (D50) to 4.0 μm to obtain a raw material heavy calcium carbonate slurry.

  A coagulant (Himax SC-100, manufactured by Hymo Co., Ltd.) was added to the heavy calcium carbonate particle slurry in an amount of 200 ppm in terms of solid content with respect to the solid content of the heavy calcium carbonate particles. The volume average particle diameter (D50) of the heavy calcium carbonate particles after the addition of the coagulant was 4.6 μm.

Next, a sodium silicate solution (silicic acid concentration 12 g / L) is added to the heavy calcium carbonate particle slurry to which a coagulant is added so that the silicic acid concentration (SiO ₂ equivalent) in the heavy calcium carbonate particle slurry becomes 8% by mass. To prepare a slurry. To this slurry, dilute sulfuric acid having a concentration of 0.1 to 5 mol / L and a pH of 9 after reaction was added in two stages, and the slurry was stirred using a mixer to perform the first reaction step. The liquid temperature of the slurry was 70 ° C. in the first stage of dilute sulfuric acid addition and 80 ° C. in the second stage. Moreover, the addition of the mineral acid at the first stage in the first reaction was performed simultaneously with the addition of the sodium silicate solution. Thereafter, the liquid temperature of the slurry is raised to 95 ° C., 8 parts by mass of sodium aluminate is added to 100 parts by mass of heavy calcium carbonate particles, and the dilute sulfuric acid in such an amount that the pH becomes 8 is again divided into two stages. In addition, the slurry was stirred to obtain silica composite heavy calcium carbonate particles. In addition, the addition of the mineral acid in the first stage in the second reaction step was performed simultaneously with the addition of sodium aluminate.

[Example 1]
Only virgin pulp was used as a raw material pulp, and softwood bleached kraft pulp (NBKP tree species: Radiata pine) and hardwood bleached kraft pulp (LBKP tree species: Eucalyptus) were blended at a mass ratio of 15:85. Silica composite heavy calcium carbonate particles obtained by the above production method as a filler (solid aluminum oxide in Example 1) and light calcium carbonate, each as a filler, with respect to this pulp (absolute dry amount) (TP-121-6S manufactured by Okutama Kogyo Co., Ltd.) was added at a mass ratio of 1: 1 such that the ash content was 17% to obtain a pulp slurry. In addition, the ratio of the silica composite heavy calcium carbonate in a filler is 60 mass%.

  Next, printing paper was obtained in a winder part using a papermaking system including a wire part, a press part, a pre-dryer part, a size press part, an after-dryer part, a scuff dryer part, a calendar part, and a reel part.

Specifically, the pulp slurry is first made with a wire part and then used for a press part and a predryer part. Then dried after dryer part, by calendar part, subjected to a flattening process at a linear pressure of 200 kN / m, rate of 1,500 m / min to obtain a printing paper having a basis weight of 64 g / ^{m 2} was subjected to winder Part . In addition, paper was made using a gap former in the wire part, and a rod metering size press coater was used in the size press part. In the calendar part, a multi-nip calendar was used. All the above parts used an on-machine papermaking system.

  The silica composite heavy calcium carbonate particles used had a volume average particle diameter of 6 μm, and the content of aluminum oxide in the silica composite heavy calcium carbonate particles was 15% by mass.

[Examples 2 to 16]
In the same manner as in Example 1, printing paper was produced using the pulp formulation, filler and ash conditions shown in Table 1. However, in Example 2, silica composite heavy calcium carbonate particles not composited with aluminum oxide were used as the silica composite heavy calcium carbonate particles. Moreover, Example 16 mix | blended 30 mass% of waste paper (magazine waste paper) with the raw material pulp.

[Comparative Examples 1 and 2]
In the same manner as in Example 1, a printing paper was produced using silica composite light calcium carbonate particles as a filler instead of silica composite heavy calcium carbonate particles. In Comparative Example 1, silica composite light calcium carbonate particles combined with aluminum oxide were used, and in Comparative Example 2, silica composite light calcium carbonate particles not combined with aluminum oxide were used.

[Comparative Example 3]
In the same manner as in Example 1, printing paper was produced using heavy calcium carbonate particles (Hydro Curve 75 manufactured by Bihoku Flour & Chemical Co., Ltd.) instead of silica composite heavy calcium carbonate particles as a filler.

[Comparative Example 4]
In the same manner as in Example 1, printing paper was produced using light calcium carbonate particles (TP-121-6S manufactured by Okutama Kogyo Co., Ltd.) instead of silica composite heavy calcium carbonate particles as a filler.

[Comparative Example 5]
In the same manner as in Example 1, printing paper was produced using talc (DN-37 manufactured by Fuji Talc Kogyo Co., Ltd.) instead of silica composite heavy calcium carbonate particles as a filler.

For the printing papers of Examples 1 to 16 and Comparative Examples 1 to 5, the basis weight, paper thickness, ash content, moisture retention time of the front and back surfaces, equilibrium moisture content and curl height were measured by the above-described methods, and further printing work Sexuality was evaluated. Table 1 shows the measurement and evaluation.

  As shown in Table 1, the printing paper of the present invention has a curling reduction effect and is excellent in printing workability.

  The printing paper of the present invention can effectively suppress curling during paper making.

DESCRIPTION OF SYMBOLS 1 Condensation reaction tank 2 1st silica composite reaction tank 3 2nd silica composite reaction tank 4 1st aluminum treatment reaction tank 5 2nd aluminum treatment reaction tank 6 Storage tank X1 Heavy calcium carbonate particle X2 Heavy calcium carbonate aggregate X3 Silica composite Heavy calcium carbonate particles X4 Silica composite heavy calcium carbonate particles combined with aluminum oxide G Coagulant L Silicate alkali solution N Mineral acid A Sodium aluminate

Claims (3)

In the base paper mainly composed of pulp and filler, containing silica composite heavy calcium carbonate particles in which silica is combined with heavy calcium carbonate particles as filler,
Ash content is 14% or more and 22% or less,
The content of the silica composite heavy calcium carbonate particles with respect to the total amount of the filler is 50% by mass or more and 100% by mass or less,
Aluminum oxide is combined with the silica composite heavy calcium carbonate particles,
Printing paper in which the moisture retention time on the front and back surfaces is 800 seconds or more, and the difference in moisture retention time between the front and back surfaces is 80 seconds or less. Printing paper according to claim 1, wherein the average particle diameter measured by a laser diffraction scattering method of the silica composite heavy calcium carbonate particles (D50) is 2μm or more 15μm or less. The pulp is mainly composed of softwood bleached kraft pulp (NBKP) and hardwood bleached kraft pulp (LBKP), or hardwood bleached kraft pulp, the mass ratio of NBKP and LBKP is 0: 100 to 25:75,
The printing paper according to claim 1 or 2 , wherein the basis weight is 50 g / m ² or more and 100 g / m ² or less.

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