JP3907693B1 - Recycled particle-added newsprint manufacturing method - Google Patents

Abstract

The present invention provides a method for producing resource-circulation-type recycled particle-added newsprint paper that collects and uses pulp fibers, fillers, and pigments, which are main components of waste paper.
[MEANS FOR SOLVING PROBLEMS] A deinking floss discharged from a used paper processing process as a filler is used as a main raw material, and the main raw material is obtained through a dehydration process, a drying process, a baking process, and a pulverization process, and has a predetermined composition An adjusted regenerated particle aggregate is produced, and this regenerated particle aggregate is internally added to the pulp. The pulp comprises 50 to 100% by weight of waste paper pulp, and the basis weight according to JIS P 8124 is 37 to 48 g / m ^2, and the paper ash content, as measured in accordance with JIS P 8251 in the paper is contained 4 to 15 wt%, Clark stiffness was measured according to JIS P 8143 is 30~55cm ^3/100, JIS A method for producing regenerated particle-added newsprint with a hot water extraction pH of 6.0 to 9.5 in accordance with P 8133.
[Selection figure] None

Description

  The present invention relates to a method for producing recycled particle-added newsprint. More specifically, the present invention relates to a method for producing recycled news paper with recycled particles that recovers, recycles, and reuses raw material pulp and filler, which are main components of newsprint, from used paper.

Due to environmental problems in recent years, there has been a movement to collect waste office paper generated from offices throughout the building for the purpose of environmental protection, resource protection, and garbage reduction, and the use of recycled paper using waste paper pulp has been seen. Along with the increase, the ratio of used paper to paper is also increasing.
In addition, from the viewpoints of resource saving, transportation cost reduction, and raw material cost reduction, the weight of each paper is increasing year by year. Furthermore, at the paper mill, the production ratio of recycled paper using recycled paper pulp and the ratio of used paper to paper have increased, and the production speed of the paper manufacturing process has increased further in order to improve paper production efficiency. Yes. Under such circumstances, the demand for newsprint is also progressing in the direction of weight reduction and higher blending of used paper. For example, the weight of newspapers has been reduced to increase the number of pages per copy without increasing the weight burden at the time of newspaper delivery, the ratio of used paper has been increased to cope with environmental problems, and offset rotary printing The speed of the machine and the colorization of paper are progressing.
For this reason, newsprint paper can be used not only for strength, such as tensile strength that can withstand high-speed offset rotary printing, but also for colorization of the paper surface, high-definition, good-quality print finish, double-page spread advertisement, etc. The required level of surface strength, ink absorptivity, printing contours and images can be seen through from the opposite side, so-called back-through and concealment, has become higher, hindering further weight reduction of newspapers and higher distribution of used paper It has become.

Conventionally, in order to improve the opacity of newsprint, mechanical pulp has been frequently used as raw material pulp. However, in recent years when high blending of used paper pulp is desired, newsprint is used as the main raw material. It is also difficult to configure. Also, with the widespread use of recycled paper, in recent years, recycled paper that is recycled paper has been further reused, that is, because pulp fibers are repeatedly reused, the resulting recycled paper pulp has fine fibers. Many have reduced strength. High blending of this waste paper causes a decrease in the strength and opacity of the newsprint, and there is a problem of show-through and concealment during printing.
In order to improve the concealing property of the newsprint as described above and reduce the back-through, it is common to improve the opacity and oil absorption of the paper by using a filler such as white carbon or calcium carbonate. Methods for adding the filler include an external addition in which a filler is surface-coated with a binder and the like, and an internal addition in which the filler is mixed with a pulp raw material to make paper.
Among the fillers, fine filler particles have good light scattering coefficient and absorption coefficient and high opacity improvement effect, but when used as an internal filler, the yield is low, and it is mainly applied by external addition. .
However, when the filler is externally applied, it is necessary to form a coating layer of a certain level or more, so that the weight reduction required for newsprint cannot be achieved. In addition, newsprint offset printing presses do not have drying equipment at high speed, so when externally applying fillers, the quality required for newsprint is satisfied in terms of ink drying, surface strength, plate stains, etc. The problem of not being able to do arises.

Therefore, for example, a paper containing pulp and calcium carbonate is made by adding white carbon to make a paper, and the filler-added paper in which the oil absorption amount, pore volume, average particle diameter, etc. of hydrated silicic acid are set within specific ranges. (See Patent Document 1) and newspaper paper (see Patent Document 2) in which white carbon and calcium carbonate are mainly used and the ratio of ash in the ash content is set within a specific range.
In the filler-added paper and newsprint, white carbon is often used as a filler, and therefore, the opacity and oil absorption are certainly improved as compared with the conventional one.
However, white carbon is expensive in the first place and causes an increase in cost. In addition, when white carbon is used frequently, there is a problem that due to its particle characteristics, it tends to be a major cause of paper dust generation and printing equipment contamination, so the amount of internal addition should be increased in consideration of maintaining paper quality. There are also limits.
When calcium carbonate is used as a filler, it is generally said that the wear of papermaking wire is fast because of its higher hardness than acidic newspaper fillers such as kaolin and talc. There is concern about plate wear for offset rotary printing. Therefore, a newspaper that is lightweight and suitable for offset rotary printing has not been developed.
Patent Document 3 which attempts to use this calcium carbonate for newsprint describes neutral newsprint that contains mechanical pulp and / or deinked waste paper pulp and calcium carbonate and is coated with a clear sizing agent. However, the papermaking in the neutral region using calcium carbonate has the problems that the papermaking equipment, especially the wire is likely to wear and deteriorate, and the pitch trouble caused by the elution of resin components derived from waste paper pulp and wood fibers and the cause of the papermaking equipment fouling. In order to express as a problem, when making paper in neutral or alkaline, after adding aluminum sulfate and fixing the resin component contained in the pulp to the fiber, specify calcium carbonate as a filler, and in the paper making process It is described that it is necessary to take a complicated operation method in which the resin component is incorporated into paper while the cationic property of aluminum sulfate is not lowered as much as possible after the addition.

On the other hand, in paper mills, the yield of fine fibers has increased due to the rapid and forced dehydration at the wire part due to the high blending of waste paper pulp with a lot of fine fibers, the weight reduction of paper, and the speedup of paper machines in recent years. The yield of ash is extremely low, and paper sludge such as drainage and dewatered sludge discharged from each paper making process is increasing.
That is, due to the increase in the production ratio of recycled paper using waste paper pulp and the high blending of waste paper pulp, a lot of waste paper pulp is required, and the amount of waste paper used is increasing. Waste paper such as newspaper and magazine waste paper contains a lot of inorganic substances derived from fillers used in uncoated paper and fillers and pigments used in coated paper. The amount of deinking floss that is separated from pulp fibers and contains a large amount of inorganic fillers and pigments is increasing.
Paper sludges such as deinking floss discharged from waste paper processing processes that contain a large amount of inorganic fillers and pigments, and wastewater and dewatered sludge discharged from each paper manufacturing process have been conventionally burned and reduced in volume. Many have been landfilled.
However, in order to continuously manufacture while maintaining and improving the quality of recycled paper that can contribute to environmental protection, resource protection, and dust reduction by the above-mentioned background technology, the paper mill can recycle and effectively use this paper sludge. Usage is a major issue.
Since the papermaking sludge contains a large amount of inorganic matter, a large amount of combustion ash (inorganic matter) remains even after combustion, and the effect of volume reduction is low. Therefore, efforts such as utilizing this combustion ash as a raw material for cement and soil improvement have been made, but in these methods, combustion ash is used as an auxiliary agent and is not used in large quantities. Most of the combustion ash will be landfilled.

It is conceivable to use the combustion ash as an internal filler for paper, but the combustion ash is not suitable for use as an internal paper filler because it has low whiteness. .
Therefore, a method has been proposed in which combustion ash (incineration ash) is reburned, and the whiteness is improved by slurrying and wet dispersion (see Patent Document 4).
However, in the case of the method of reburning the incinerated ash, in order to completely burn the unburned carbon, it is necessary to set the reburning temperature to 500 to 900 ° C., and the whiteness of the incinerated ash is about 50%. It has been found that it is not suitable for use as a paper filler. It has also been found that when the re-combustion temperature is set to over 900 ° C., the combustion ash (inorganic material) is sintered and melted and becomes extremely hard. In addition, when reburned ash is used as a filler for paper, the reburned ash has very hard properties, so the papermaking wire wears quickly and its life is very short. I could not.
For such papermaking wire wear, it is conceivable that the reburned ash is crushed and its particle size is reduced to reduce wear and improve smoothness, but when used as an internal filler for paper. However, there is a problem that the yield during paper making is low and the reburned ash itself is extremely hard, so that the energy cost for pulverization becomes extremely high.
Also, as a method of using paper sludge, water-containing paper mill waste sludge containing organic matter from paper fibers is supplied into a reactor into which oxygen-containing gas has been injected, and is heated to about 250 to 300 ° C. and 3000 psig (psig). There has been proposed a method of regenerating the inorganic substance in the waste sludge as a papermaking pigment (inorganic filler) by oxidation under pressure for 0.25 to 5 hours (see Patent Document 5).
However, since the above method is based on wet air oxidation treatment of papermaking sludge, organic matter removal is not sufficient, and the obtained pigment has low whiteness and irregular particle sizes, and is used as a filler for papermaking. However, there is a problem that the reaction operation is complicated and expensive.
In addition to these, a method has been proposed in which papermaking sludge is baked into PS charcoal and then incinerated with a kiln to produce white clay as a papermaking raw material (see Patent Document 6).
However, in this method, since the papermaking sludge is fried, not only energy cannot be effectively extracted from the papermaking sludge, but also there is a great demerit that input energy is required. Furthermore, the generated white clay also has a problem that the particle size is uneven and large, and cannot be used as a papermaking filler.
Furthermore, a method for producing a papermaking filler by adding a flocculant to the waste water and granulating the resulting sludge and drying, carbonizing, and firing continuously in a rotary kiln has also been proposed (see Patent Document 7). . In this method, the granulation and shaping are performed prior to firing in order to perform firing uniformly.
However, for example, when formed sludge having a solid content concentration of 40 to 60% (in other words, moisture content of 60 to 40%) is continuously dried, carbonized, and calcined in a rotary kiln, it depends on the dry state and carbonized state. First, the treatment of sludge particles is forced to proceed by the rotation of the kiln. Therefore, if the drying is insufficient, a large amount of unburned matter remains inside the particles, and as a result, the firing becomes incomplete and the whiteness is lowered. On the other hand, when overdried, the firing is complete but overfired and the hardness of the obtained regenerated particles is increased. Use of the recycled particles causes a problem that wire wear in a paper machine and cutter blade wear when cutting paper are likely to occur.
The biggest problem of the conventional methods of manufacturing paper fillers using papermaking sludge as a raw material described in Patent Documents 4 to 7 is that the papermaking sludge used as a raw material flows out through a wire in the papermaking process. , Collected from wastewater containing solids generated in the washing process in the pulping process, separated and recovered by solids separation equipment using precipitation or floating in the wastewater treatment process, waste paper treatment Various sludges such as those from which foreign substances are removed in the process are mixed.
Among the various sludges, for example, a paper strength agent or the like is mixed in sludge that has flowed out through the wire in the papermaking process, and the quality of the sludge varies due to changes in the papermaking process.
Moreover, flocculant is mixed in the sludge collected from the waste water, and the quality of the sludge varies greatly due to papermaking, production volume fluctuations, and in-process washing of the production equipment.
The sludge generated from the washing process in the pulping process contains substances that are not suitable for paper fillers and pigments, and the quality may vary due to fluctuations in chip moisture and pulp production conditions.
Therefore, when various papermaking sludges are used without selection, the quality and quality of the papermaking fillers and pigments are low, and the quality is extremely variable and unstable.

As described above, all of the conventional methods using papermaking sludge all start with the recovery of papermaking particles, and the regenerated particles from the papermaking sludge obtained by these methods have a quality as a papermaking pigment and filler. It was not suitable and lacked quality stability.
Therefore, although raw paper pulp, which is a major component of newsprint, is increasingly used as waste paper pulp, conventional white carbon and calcium carbonate must be used as a filler. Therefore, development of a technique capable of improving the opacity and paper strength while reducing costs and improving the wear problem of the papermaking equipment is desired.
Japanese Patent Laid-Open No. 09-176985 JP 2002-201590 A JP 09-78491 A JP-A-11-310732 Japanese Examined Patent Publication No. 56-27638 Japanese Patent Laid-Open No. 54-14367 JP 2004-176208 A

The present invention has been made in view of the above-mentioned background art, and from recycled paper, pulp fibers, fillers and pigments, which are main components of waste paper (paper), are recovered and used together. It is an object of the present invention to provide a method for producing newsprint.
More specifically, the pulp fibers and fillers / pigments that are the main components of waste paper (paper) are collected together, recycled at low cost by using resources, and papermaking in the neutral or alkaline region. Not only is excellent paper strength maintained and there are few paper breaks, but there are also little blanket stains due to resin and paper dust, printing white spots, etc., and excellent ink absorption, excellent opacity and little show through. It is an object of the present invention to provide a method for producing a recycled particle-added newsprint that can be suitably used for printing in high-speed offset rotary printing.

The present invention that has solved this problem is as follows.
[Invention of Claim 1]
A method for producing newsprint with a filler added to pulp,
The main material is deinked floss discharged from the waste paper processing process as the filler,
Producing a regenerated particle aggregate obtained by aggregating the main raw material through the dehydration step, the drying step, the firing step, and the pulverization step and aggregating in the firing step, and adjusted to have the following composition:
This regenerated particle aggregate is internally added to the pulp,
The pulp comprises 50-100% by weight of waste paper pulp,
The basis weight according to JIS P 8124 is 37 to 48 g / m ² ,
The paper ash content measured according to JIS P 8251 is contained in the paper in an amount of 4 to 15% by mass,
Clark stiffness was measured in accordance with JIS P 8143 is 30~55cm ^3/100,
The hot water extraction pH according to JIS P 8133 is 6.0 to 9.5.
A method for producing recycled particle-added newsprint.
(composition)
The regenerated particle aggregate contains calcium, silicon, and aluminum as constituents of the regenerated particle aggregate in a mass ratio of 30 to 82: 9 to 35: 9 to 35 in terms of oxides. The regenerated particle aggregate in which the total content of the calcium, the silicon, and the aluminum is 93% by mass or more in the regenerated particle aggregate component among the components of the aggregate.

[Invention of Claim 2]
The method for producing a newspaper with internal regenerated particles according to claim 1, wherein the blank paper opacity measured according to JIS P 8138 is 91 to 95%.

[Invention of Claim 3]
The 10-second bump size based on JIS P 8140 is 30 to 300 g / m ² .
3. A method for producing newspaper with internal regenerated particles according to claim 1 or 2.

[Invention of Claim 4]
Oil absorption based on JIS P 3001 is 50 to 150 seconds,
The manufacturing method of the regenerated particle internal newsprint of any one of Claims 1-3.

  The recycled particle-added newsprint of the present invention utilizes deinking floss that has been incinerated or landfilled as industrial waste as a filler material for papermaking, and by using wastepaper pulp made of wastepaper as the main raw material pulp, It is manufactured at low cost by recycling resources, has a high ash yield at the time of paper making, and maintains excellent paper strength with little deterioration of wear of the paper making equipment such as wire wear and contamination of the printing equipment due to elution of resin components. In addition to low paper breakage, there are few blanket stains due to paper dust, printed white spots, etc., and excellent ink absorption, high opacity and low back-through. It can be suitably used for rotary printing, offset rotary color printing and high-definition printing.

Next, an embodiment of the present invention will be described.
The method for producing a newsprint with regenerated particles according to this embodiment is a method for producing newsprint in which a filler is internally added to pulp,
The main material is deinked floss discharged from the waste paper processing process as the filler,
A regenerated particle aggregate obtained by subjecting the main raw material to a dehydration step, a drying step, a firing step, and a pulverization step (without adding a step of aggregating particles after the pulverization step) and adjusted to have the following composition: Manufacture and
This regenerated particle aggregate is internally added to the pulp,
The pulp comprises 50-100% by weight of waste paper pulp,
The basis weight according to JIS P 8124 is 37 to 48 g / m ² ,
The paper ash content measured according to JIS P 8251 is contained in the paper in an amount of 4 to 15% by mass,
Clark stiffness was measured in accordance with JIS P 8143 is 30~55cm ^3/100,
The hot water extraction pH according to JIS P 8133 is 6.0 to 9.5.
It is characterized by this.
(composition)
The regenerated particle aggregate contains calcium, silicon, and aluminum as constituents of the regenerated particle aggregate in a mass ratio of 30 to 82: 9 to 35: 9 to 35 in terms of oxides. The regenerated particle aggregate in which the total content of the calcium, the silicon, and the aluminum is 93% by mass or more in the regenerated particle aggregate component among the components of the aggregate.

  Since pulp fibers and fillers, which are the main components of paper, are all collected, recycled and reused, the paper that can be provided by the present invention is completely different from conventional newsprint paper. Defined as recycled newspaper.

First, the raw material pulp used for this embodiment is demonstrated. Such raw material pulp is composed of 50 to 100% by weight of waste paper pulp made from waste paper such as newspaper waste paper, magazine waste paper, imitation / colored waste paper, and OA waste paper. Thus, in this embodiment, since used paper pulp is 50 mass% or more, it contributes greatly to the effective use of resources and can achieve cost reduction. In particular, newsprint paper has a high recovery rate as waste paper, and is said to be an excellent student of recycling. Newspaper paper made of completely recycled paper based on the present invention is used for its use, thereby further promoting the circulation of newsprint paper. It becomes possible.
There is no limitation in particular in the kind of used paper pulp, For example, a diinking pulp (DIP), a waist pulp (WP) etc. are mention | raise | lifted, These can be used individually or simultaneously.
As the raw material pulp, pulp used for ordinary paper can be used as appropriate in addition to the waste paper pulp. Examples of raw material pulp other than waste paper pulp include Stone Grand Pulp (SGP), Pressurized Stone Grand Pulp (PGW), Refiner Grand Pulp (RGP), Chemi Grand Pulp (CGP), Thermo Grand Pulp (TGP), and ground wood. Pulp (GP), thermomechanical pulp (TMP), chemithermomechanical pulp (CTMP), refiner mechanical pulp (RMP) and other mechanical pulp; softwood kraft pulp (NBKP), hardwood kraft pulp (LBKP) and other chemical pulp; The pulp etc. which bleached these are mention | raise | lifted and it can select and use 1 type (s) or 2 or more types from these.
As described above, the ratio of the waste paper pulp in the raw material pulp is 50 to 100% by mass. However, 60 to 100% by mass, particularly 70 to 100% by mass, is achieved from the point of realizing resource saving and cost reduction. It can be 100 mass%.

Next, the filler used in this embodiment will be described. As such a filler, at least a regenerated particle aggregate containing a specific amount of calcium, silicon and aluminum, which is obtained by using deinked floss as a main raw material and undergoing a dehydration step, a drying step, a firing step and a pulverization step, is used.
At least the surface of the regenerated particle aggregate is coated with silica, and the silica-coated regenerated particle aggregate adjusted to the above composition is used as the filler, and a specific amount is internally added to the raw material pulp containing 50 to 100% by weight of waste paper pulp. This is one of the major features of this embodiment. Since the recycled particle aggregate can be recycled by baking deinked froth, it does not require disposal such as landfill as waste, greatly reducing the environmental burden and saving resources. It contributes. Further, since the raw material is deinking floss generated in the waste paper processing step, there is an advantage that it is inexpensive, the amount of new inorganic particles used can be suppressed, and the manufacturing cost is sufficiently reduced. Furthermore, by using the recycled particle aggregate, the ash yield during paper making is high. Unlike calcium carbonate, for example, there is no wear deterioration of paper making equipment such as wire wear, and the resin component is regenerated in a fine state. By adsorbing to the particles, pitch troubles caused by resin agglomeration can be prevented, printing equipment can be hardly contaminated, and paper can be manufactured at low cost and high operability. Transparency and paper strength are imparted to the paper, and there are fewer breakthroughs and paper breaks.

  The regenerated particle aggregate used in the present embodiment is obtained by using deinked floss as a raw material and passing through a dehydration step, a drying step, a firing step, and a pulverization step. Furthermore, as will be described later, a deinking floss aggregation process, a granulation process, a classification process provided between the processes, and the like may be performed. In addition, it is desirable to provide various sensors in the production facility for regenerated particles to control the state of the object to be processed and the equipment, the processing speed, and the like.

  Furthermore, in the present embodiment, as the regenerated particle aggregate internally added to the raw material pulp, it is particularly preferable to use a silica-coated regenerated particle aggregate in which the surface of the particles obtained through the above-described steps is coated with silica. It can be done.

  Silica is further precipitated on the surface of the regenerated particle aggregate to form a silica-coated regenerated particle agglomerate, so that it is reacted with sodium hydroxide in the used paper processing step in circulation use and used as a buffering agent or bleaching aid as a papermaking raw material. In addition, it can contribute to the recycling of inorganic particles. Further, when such a silica-coated regenerated particle aggregate is internally added to the raw material pulp as a filler, the whiteness of the paper, opacity, surface strength, and more than when using a regenerated particle aggregate not coated with silica, Each effect such as ink drying property, ink absorption unevenness and bulkiness can be improved.

  In addition, the deinking floss produced in the used paper processing step used in the present embodiment has a tendency to increase the content of calcium carbonate with the recent neutral paper making, the proportion of calcium in the obtained regenerated particle aggregate Tend to be higher. When regenerated particle agglomerates with a high calcium content are added internally to the raw material pulp, the opacity of the paper may be slightly reduced, but the silica-coated regenerated particle agglomerates with silica precipitated on the surface are used for papermaking. The regenerated particle aggregate has a very high function, and the opacity of the paper obtained by internally adding the silica-coated regenerated particle aggregate to the raw material pulp is remarkably improved.

  The silica covering the surface of the regenerated particle aggregate can be used without particular limitation as long as it is not naturally produced silica but synthetic silica by some chemical reaction. Specific examples include colloidal silica, silica gel, and anhydrous silica. These synthetic silicas make use of excellent properties such as high specific surface area, high gas adsorbing capacity, fineness, permeability to pores and large adsorbing power, high adhesion, and high oil absorption. It is used in a wide range of fields. Among these, colloidal silica has a shape such as a spherical shape, a chain shape, and an amorphous shape, in which impurities are removed from a silicic acid compound to form an anhydrous silicic acid sol, and the sol is stabilized by adjusting pH and concentration. Amorphous silica. Silica gel is hydrous silicic acid obtained by decomposing sodium silicate with an inorganic acid. Anhydrous silica is obtained by hydrolysis of silicon tetrachloride.

  There is no particular limitation on the method for obtaining silica-coated regenerated particle aggregates by precipitating silica on the surface of the regenerated particle aggregates. For example, the following methods can be suitably employed. First, regenerated particle aggregates are added and dispersed in an alkali silicate solution, and after preparing a slurry, while heating and stirring, an acid is added while maintaining the liquid temperature at about 70 to 100 ° C. to produce a silica sol. Subsequently, silica can be deposited on the surface of the regenerated particle aggregate by adjusting the pH of the final reaction solution to a range of 8-11. Silica deposited on the surface of the regenerated particle aggregate in this way reacts at a high temperature with a dilute solution of mineral acid such as sulfuric acid, hydrochloric acid, nitric acid, etc., using alkali silicate (eg, sodium silicate: water glass) as a raw material. And silica sol particles having a particle size of about 10 to 20 nm, which are obtained by hydrolysis reaction and polymerization of silicic acid.

  In addition, silica sol fine particles with a particle size of several nanometers, which are generated by adding an acid such as dilute sulfuric acid to an alkali silicate solution such as sodium silicate solution, cover the entire porous surface of the regenerated particle aggregate. The surface of the regenerated particle aggregate is caused by the bond between the silica sol fine particle on the surface of the inorganic fine particle and the silicon, calcium, or aluminum included in the regenerated particle aggregate accompanying the crystal growth of the silica sol fine particle. Silica can also be deposited on the substrate. In this case, the pH when adding the acid to the alkali silicate solution is in a neutral to weakly alkaline range, and the pH is preferably adjusted in the range of 8-11. This is because if the acid is added until the pH reaches an acidic condition of less than 7, white carbon may be generated instead of silica sol particles.

The type of the alkali silicate solution is not particularly limited, but a sodium silicate solution (No. 3 water glass) is particularly desirable from the viewpoint of easy availability. The concentration of the alkali silicate solution is such that the silica component in the regenerated particle aggregate decreases and the silica content (SiO _{2) in the} solution does not become difficult to precipitate on the surface of the regenerated particle aggregate. (Converted) is preferably 3% by mass or more, and the silica deposited on the surface of the regenerated particle aggregate becomes white carbon from the form of the silica sol, and the porosity of the regenerated particle aggregate is hindered. In order to eliminate the possibility that the effect of improving the fixability will be insufficient, the silicic acid content (in terms of SiO ₂ ) is preferably 10% by mass or less.

  In order to make the particle size of the regenerated particles uniform in each step, classification is preferably performed, and the quality can be further stabilized by feeding back coarse particles and fine particles to the previous step.

  In addition, it is preferable to granulate the deinked floss that has been dehydrated in the previous stage of the drying process, and more preferably to classify the granulated product uniformly so that coarse or fine particles are formed. The quality can be further stabilized by feeding back the grains to the previous process. In granulation, ordinary granulation equipment can be used, and equipment such as a rotary type, a stirring type, and an extrusion type is preferable.

  It is preferable to remove foreign substances other than regenerated particles in the production facility. For example, it is possible to remove foreign substances such as sand, plastic, metal, etc. with a pulper, screen, cleaner, etc. before reaching the deinking process of the used paper pulp manufacturing process. From the viewpoint of removal efficiency. In particular, the iron content is preferably removed by avoiding the mixing of iron content, since it causes the whiteness of the regenerated particles to be reduced due to oxidation. Therefore, each process is designed or lined with materials other than iron, and iron is prevented from being mixed into the system due to wear, etc., and a high magnetic material such as a magnet is installed and selected in the drying / classifying equipment. It is preferable to remove iron.

In the present embodiment, in the drying step, the firing step, and the classification step as necessary, the particles having a particle size of 40 μm or less are preliminarily processed to 90% by mass or more before the pulverization step. Is preferred. Accordingly, a single-stage pulverization process by wet pulverization can be performed without performing a multistage pulverization process such as pulverization of coarse particles by dry pulverization and fine particle formation by wet pulverization. Thereby, the peak height of the average particle diameter in the differential curve of the particle size distribution by the Coulter counter method can be set to 30% or more. Furthermore, by adjusting calcium, silicon, and aluminum in the deinking floss as a raw material in advance to a mass ratio described later, for example, the pore volume of the regenerated particle aggregate is 0.15 to 0.60 cc / g, fine. The pore surface area may be 10 to 25 m ² / g, and the pore radius may be 30 to 100 nm.

The regenerated particle aggregate thus obtained contains calcium, silicon and aluminum. The ratio of these calcium, silicon, and aluminum in the regenerated particle aggregate is subjected to elemental analysis using an X-ray microanalyzer (model number: E-MAX S-2150, Hitachi, Ltd./Horiba, Ltd.). In terms of oxide, calcium: silicon: aluminum is 30 to 82: 9 to 35: 9 to 35, further 40 to 82: 9 to 30: 9 to 30, particularly 60 to 82: 9 to 20: 9 to 20 The mass ratio is preferably.
In particular, when the regenerated particle aggregate is silica-coated regenerated particles, the ratio of calcium, silicon and aluminum is 30 to 62:29 to 55: 9 to 35 in terms of oxides: calcium: silicon: aluminum. It is preferable. At the same time, the total content in terms of oxides in the elemental analysis of calcium, silicon and aluminum is 90% by mass or more, preferably 93% by mass or more.

  Thus, for example, when a regenerated particle aggregate containing 30 mass% or more of calcium in terms of oxide is internally added to the raw material pulp as a filler, the whiteness of the obtained paper can be improved.

  In order to adjust the ratio of calcium, silicon, and aluminum in the regenerated particle aggregate within the above range, for example, in terms of oxide, it is originally preferable to adjust the raw material composition in the deinking floss, but the drying step and the firing step Further, if necessary, in the classification step, it is also possible to employ a method in which a coating floss having a clear origin or an adjustment step floss is contained by spraying or a method in which incinerator scrubber lime is contained.

  For example, neutral paper-making wastewater sludge for the adjustment of calcium in recycled particle aggregates and wastewater sludge from the coated paper manufacturing process, and newsprint manufacturing with a large amount added as an opacity improver for silicon adjustment For the adjustment of aluminum, a papermaking wastewater sludge using an acid papermaking system or other sulfuric acid band or a high quality papermaking process wastewater sludge using a large amount of clay can be used as appropriate.

  Moreover, in order to adjust the total content of calcium, silicon and aluminum to 90% by mass or more in terms of oxides, for example, means for using a flocculant containing no iron in the agglomeration treatment of drainage sludge, and manufacturing equipment processes other than iron Designed or lined with other materials to prevent iron from being mixed into the system due to wear, etc., and further adopting means to remove iron by installing high magnetic materials such as magnets in the drying and classification equipment Is possible. In particular, iron content is preferably a causative substance that lowers the whiteness by oxidation, and thus is preferably removed selectively.

  By the way, calcium carbonate has homogeneous images such as hexagonal calcite crystals (calcite) and orthorhombic aragonite crystals (aragonite). Most limestones produced in nature are calcite crystals, and shellfish contain aragonite crystals in addition to calcite crystals. Furthermore, although not natural, calcium carbonate also has vaterite crystals. There are various kinds of calcium obtained from the deinking floss, but it becomes a substantially uniform calcium carbonate property by calcination and aggregation. Accordingly, the calcium contributes to the quality stability of the regenerated particle aggregate itself, and the regenerated particle aggregate exhibits stable properties while being an aggregate composed of different components such as calcium, silicon, and aluminum.

  The regenerated particle aggregate contains silicon, but since the primary particles of silica composed of silicon are fine, the optical refractive index is high. Therefore, for example, when a regenerated particle aggregate containing 9 mass% or more of silicon in terms of oxide is internally added to the raw material pulp as a filler, the opacity of the obtained paper can be improved.

  Furthermore, since the regenerated particle aggregate used in the present embodiment has a flexible and porous property in which fine particles are secondarily aggregated, it contributes to the formation of a bulky paper layer, and the regenerated particle aggregate is used as a filler in raw pulp. Newspaper paper obtained by internal addition has a low density and a high rigidity for handling.

  The particle diameter of the regenerated particle aggregate used in the present embodiment is, for example, as a secondary particle in which primary particles are aggregated, in terms of yield in the raw material pulp and prevention of loss of regenerated particles into white water. Is measured with a Coulter counter particle size distribution measuring apparatus (TA-II type, manufactured by COULTER ELECTRONICS), and the average particle size is preferably 0.05 μm or more, more preferably 0.1 μm or more, and the printing quality is maintained. In view of preventing clogging of the sword tip, the average particle size is preferably 16 μm or less, and more preferably 15 μm or less.

  When the content of the regenerated particle aggregate is too small, for example, in a calendar process on a paper machine, a smoothing effect is hardly exhibited, and the opacity after printing is lowered due to a decrease in paper opacity. Or the rigidity of the newsprint is increased, and the running performance on a rotary press may be reduced. Therefore, the content is preferably 2% by mass or more, more preferably 5% by mass or more based on the raw material pulp. . Conversely, if the content of regenerated particle aggregates is too high, it is desirable in terms of surface properties and rigidity, but ash tends to fall off during transport in the printing press, resulting in reduced surface strength, Since there is a possibility that fluffing, printing white spots, and paper dust may occur, the content is preferably 20% by mass or less, more preferably 15% by mass or less, based on the raw material pulp.

  In the present embodiment, the regenerated particle aggregate can be used alone as a filler, but in addition to this, calcium carbonate such as heavy calcium carbonate and light calcium carbonate, talc, etc. And at least one filler selected from clays such as kaolin clay and delaminated clay, inorganic fillers such as titanium dioxide, synthetic silica and aluminum hydroxide, and synthetic polymer fine particles such as polystyrene resin and urea formaldehyde resin You can also

  In addition, when the addition rate of the filler containing the regenerated particle agglomerates is too small, the effect of using the filler is not sufficiently expressed, and conversely, when it is too large, the paper strength may be reduced. The filler is preferably contained in the paper in an amount of 4 to 15% by mass, more preferably 5 to 10% by mass, as paper ash.

  In addition, as additives to be added to the paper slurry obtained from raw pulp and filler, those added to ordinary paper can be used, such as starches, vegetable gums, aqueous cellulose derivatives, sodium silicate, etc. Paper strength enhancers: rosin, starch, CMC (carboxyl methylcellulose), polyvinyl alcohol, alkyl ketene dimer, ASA (alkenyl succinic anhydride), neutral rosin and other internal sizing agents; polyacrylamide and copolymers thereof, silica Examples thereof include a yield improving agent such as sodium acid.

  Furthermore, in this embodiment, after preparing a paper slurry from raw material pulp and making paper, a surface treatment agent containing, as a component, a polymer material such as starch, modified starch, PVA (polyvinyl alcohol), or polyacrylamide is formed on the surface. You may apply | coat or color materials, such as dye and a pigment, may be added to paper stock slurry.

  The modified starch is not particularly limited, and ordinary starch raw materials are used. Examples thereof include starch obtained by subjecting corn, potato, tapioca, wheat, rice, etc. to oxidation treatment, enzyme treatment, and the like. When this modified starch is used, the amount in the surface treatment agent is preferably adjusted so as to be 40% by mass or more in the total solid content in order to obtain a desired effect.

  As the surface treatment agent, other adhesives as appropriate, for example, latexes such as styrene-butadiene copolymer, polyvinyl alcohol and polyacrylamide, and pigments such as kaolin and calcium carbonate, antifoaming agents, water-proofing agents, surface size, etc. Various auxiliaries such as agents and preservatives can also be added. Moreover, the solid content concentration of the surface treatment agent is not particularly limited, and is preferably adjusted to, for example, about 2 to 25% by mass according to the coating apparatus and the coating amount.

  If the surface treatment agent is used in an excessively large amount, not only the cost is increased, but also the adhesiveness of the paper surface called “Nepari” property tends to be expressed when the paper surface is wet. If this sharpness increases, there is a risk that blanket piling, especially in non-image areas, will increase and the paper surface will stick to the blanket during printing, resulting in running problems such as wrinkles and paper breaks. Because there is, it is not preferable. Further, when the amount of the surface treatment agent used is increased, the transparency of the target paper may be increased, that is, the opacity may be decreased, or the ink drying property may be deteriorated. Of these surface treatments, starch and polyacrylamide are widely used because of their relatively low nepariness, but they are both highly soluble in water, so that they can be easily eluted in dampening water during printing. At the same time, it is deposited on the blanket, and blanket piling is likely to occur. Also, the eluted surface treatment agent is transferred to and accumulated on the printing plate via the blanket, so that the non-image area of the printing plate becomes sensitized, and ink stains on the non-image area, that is, paper contamination called background contamination, is induced. Therefore, it is not preferable to use a large amount.

  The surface treatment agent is a coating apparatus commonly used in the papermaking field, such as a size press, a blade metering size press, a rod metalling size press, a gate roll coater, a blade coater, a bar coater, a rod coater, an air knife coater, etc. And apply.

The coating amount of the surface treating agent, in order to sufficiently improve the surface strength of the paper is preferably adjusted so that 0.4 g / m ² or more by dry weight, also may become a cost, Ya opacity to prevent or cause a reduction in the ink drying property is dried as heavy weight becomes 3.0 g / m ² or less, more preferably, it is adjusted to below 0.7 to 2.5 g / m ² Is preferred.

  Thus, the stock prepared from the stock slurry and, if necessary, the additive can be made by a known paper machine, and further passed through a calender device as necessary, followed by pressurization and smoothing treatment. Can be finished into newspaper. As the calendering device, a soft calender using a combination of a metal roll and a resin roll is used to smooth the paper layer without pressing strongly, rather than a machine calender using a combination of a normal metal roll and a metal roll. Further, it is more preferable because a decrease in paper layer strength can be sufficiently suppressed.

  In the use of the soft calendar, the flatness and bulkiness can be further improved by passing the paper so that the back side, which is the rough side of the newspaper, contacts the metal roll surface of the soft calendar first, Newspaper paper with high flatness and little difference in front and back can be obtained in high-speed papermaking at 1500 m / min or more.

  More preferably, by increasing the coating amount of the surface treatment agent provided on the front and back sides on the back side from the front side, better flatness and bulkiness can be obtained, and it is possible to obtain a newsprint with a waist.

  The pH of the newsprint at the time of papermaking is determined by adding aluminum sulfate (sulfuric acid band) and fixing the resin component to the fiber through aluminum or forming an aggregate of the resin component. In order to prevent adhesion of the resin component in the manufacturing process by incorporating it into the paper support, it is common to make newsprint within the range of pH 4 to less than 6 where the cationicity of the aluminum ion species is most active, The waste paper pulp used in the present invention is manufactured by deinking from waste paper, so that the pH is as high as 6 or more, and the use of calcium carbonate, which is considered to be auxiliary use in terms of stability and pH adjustment due to high pH. At this time, the calcium carbonate dissolves to eliminate the risk of yield loss and the cause of soiling in the papermaking process. In than paper, the grounds improvement in paper strength is achieved by paper with 6 or more, it is preferable to adjust such that the order of 6 to 9.5.

  Addition of the regenerated particle agglomerates can be performed at any stage of the prior art, but is preferably performed between the raw material blending chest and the inlet. Addition during this time makes it easy to disperse the regenerated particle aggregates, improving the fixability to pulp fibers, and as a result, improving the yield of the filler. Further, since the regenerated particle aggregate does not inhibit the binding between the pulp fibers, the rigidity of the paper is not lowered. In order to disperse the regenerated particle aggregate more uniformly and to improve the fixability to the pulp fiber, it is particularly preferable to add the regenerated particle aggregate as close as possible to the inlet.

  The newsprint thus obtained has an ash content of 4 to 15% in accordance with JIS P 8251, and hot water measured in accordance with “Test method for pH of paper, paperboard and pulp-water extract” described in JIS P 8133. The extraction pH is preferably 6.0 or more, more preferably 6.1 or more, and is preferably 9.5 or less, more preferably 8.5 or less. When the hot water extraction pH is in such a range, calcium carbonate, which is considered to be an auxiliary use, or a little, but it is considered that the elution of calcium carbonate contained in the regenerated particle aggregate is prevented, and regenerated particles are used. The shape of the aggregate is stable, the formation of calcium hydroxide is prevented, the occurrence of dirt and scale in the papermaking process system is suppressed, paper deterioration can be suppressed, and resource circulation can be achieved. In addition, the ink drying property of paper can be improved, the ink absorption unevenness can be reduced, the deterioration can be sufficiently suppressed, and the storage stability and the fixing property of the auxiliary agent can be further improved.

Further, the basis weight of the paper according to the present embodiment is based on the “basis weight measurement method” described in JIS P 8124 from the viewpoint of weight reduction, for example, ensuring the paper quality strength in high-speed rotary printing and ensuring the printing opacity. Measured, it is preferably 37 g / m ² or more, more preferably 40 g / m ² or more, and the basis weight is 48 g / m ² or less, further 46 g / m ² or less from the viewpoint of weight reduction. It is preferable. If it is less than 37 g / m ² , for example, it is difficult to ensure the strength in a high-speed offset rotary printing press, and if it exceeds 48 g / m ² , it goes against the recent weight saving and resource saving.

  The whiteness of paper varies depending on the application, but in order to prevent eye strain of subscribers in newspapers, it conforms to the “Testing Method for Hunter Whiteness of Paper and Pulp” described in JIS P 8123. Measured at least 50% or more, and the whiteness is preferably 52 to 56%, more preferably 53 to 55%.

  Newspaper paper opacity is required to have high opacity because it is difficult to see through during printing, but it is measured in accordance with “Paper Opacity Test Method” described in JIS P 8138. Thus, it is preferably 91 to 95%, more preferably 92 to 94%.

Further, the density of newsprint is measured in accordance with “Paper and paperboard—Test method of thickness and density” described in JIS P 8118 from the viewpoint of maintaining the strength accompanying weight reduction and weight reduction in recent years. .55~0.60g / cm ^3, preferably further it is 0.56~0.59g / cm ^3.

In addition, the stiffness in the MD direction of the paper is measured in accordance with “a stiffness test method using a paper Clark stiffness tester” described in JIS P 8143, for example, in order to give a waist suitable for high-speed rotary printing. It is preferable that it is 30-55 cm < ³ > / 100, Furthermore, it is 32-50 cm < ³ > / 100.

  Offset rotary printing used in newsprint is a method in which dampening water and printing ink are supplied to a printing plate, then the ink is transferred to a rubber plate called a blanket, and then transferred to paper for printing. Compared to the conventional letterpress printing method, ink with relatively high viscosity is used, so that the ink does not penetrate into the paper layer, the ink is well-positioned, and there is little ink penetration after printing. It has the advantage (high opacity).

  Further, in recent years, with the colorization and weight reduction of newsprint, there is a further demand for good ink fillability and high opacity after printing. Of these, as a means for improving ink fillability, it is widely practiced to smooth newspaper paper by the above-described flattening process using a soft calendar or the like. However, if the nip pressure in the calendar process is increased or smoothed by increasing the number of nips, the ink inking property is increased, but the bulkiness of the paper is impaired, so the opacity after printing decreases, Since the rigidity becomes low, it may cause troubles such as poor running performance during printing.

  On the other hand, if the calendar process is reduced, a bulky paper can be obtained, but the difference in front and back of the paper surface is increased. There arises a problem that the density of the image is significantly different from the back. This is because the dehydration conditions in the wire part and press part are slightly different between the front and back sides during the paper making process, so there is a difference in the smoothness of the paper, and the distribution of filler and fine fibers in the thickness direction. It is considered that there is a difference between the front and the back of the ink transferability.

In the transfer of dampening water and printing ink on newsprint paper having a basis weight of 37 to 48 g / m ² according to JIS P 8124, the inventors have a 10 second Cobb sizing degree based on JIS P 8140 of the newsprint paper. Is 30 to 300 g / m ² , and the oil absorption based on JIS P 3001 is preferably 50 to 150 seconds. By suppressing the relationship between so-called hydrophilicity and lipophilicity within a predetermined range, it is possible to improve the appropriateness of offset rotary printing in combination with the flattening process.

  Furthermore, considering the paper quality strength in high-speed rotary printing, the surface strength of the paper is preferably at least grade 3 or higher as measured by an RI tester (manufactured by Akira Seisakusho Co., Ltd.) described later.

  As described above, the newsprint according to the present embodiment uses, as a main raw material, deinking floss generated in the waste paper processing step in raw pulp containing 50% by mass or more of waste paper pulp, and a total of 90 masses of calcium, silicon, and aluminum. % Of the regenerated particle agglomerates also contained as a filler. Therefore, the newsprint according to the present embodiment has a high ash yield at the time of papermaking, and is produced at low cost by reusing resources without causing wear deterioration of the papermaking equipment such as wire wear and printing equipment contamination. Excellent paper strength is maintained and there is no paper breakage, and there is no blanket stains due to paper dust, clogging of the sword, color misalignment, etc. Moreover, the newsprint according to the present embodiment is excellent in various characteristics during printing, particularly color printing, and can be suitably used for high-speed offset rotary color printing such as about 1 to 170,000 copies / hour.

Next, the newspaper of the present invention will be described in more detail based on the following examples, but the present invention is not limited to these examples.
[Production of regenerated particles (Production Examples 1 to 19 and Comparative Examples 1 to 4)]
As shown in Table 1, as a raw material, deinking floss (deinking floss obtained from a waste paper treatment process for producing waste paper pulp, Production Examples 1 to 19) or paper sludge (mainly drainage / drainage discharged from the paper making process) Using dehydrated sludge and comparative (manufacturing) Examples 1 to 4), after undergoing a dehydration step, a drying step and a firing step under the conditions shown in Table 1, a wet pulverization treatment was performed to obtain a regenerated particle aggregate.
Furthermore, in Production Examples 15 to 17, a regenerated particle aggregate was added to and dispersed in a sodium silicate solution (water glass) to prepare a slurry, and then the liquid temperature was maintained at about 85 ° C. while heating and stirring. Sulfuric acid was added to produce a silica sol. Subsequently, the pH of the reaction solution was adjusted to 8 to 11, and silica was deposited on the surface of the regenerated particle aggregate to obtain a silica-coated regenerated particle aggregate.
With respect to the obtained regenerated particle aggregate and silica-coated regenerated particle aggregate, the contents of calcium, silicon and aluminum were determined in terms of oxides, respectively, and the total content ratio of calcium, silicon and aluminum was calculated. The results are shown in Table 2. The average particle size is also shown in Table 2. Furthermore, the wire wear degree, productivity, quality stability and appearance were also examined. These results are also shown in Table 2.

Various measured values shown in Tables 1 and 2 were measured by the following methods.
(A) Average particle diameter of dried product after drying process (firing process inlet) X-ray microanalyzer (model number: EMAX2770, Hitachi, Ltd./Horiba, Ltd.) at an acceleration voltage of 15 kV, black and white polaroid film Twenty X-ray images of the X-ray microanalyzer display were taken and measured at Polaroid (8.5 cm × 10.8 cm).
(A) Ratio of particles having a particle size of 355 to 2000 μm after the drying step (calcination step inlet) The mass ratio of dry matter particles having a particle size of more than 2000 μm is obtained with a 42 mesh sieve. The mass ratio of dried particles having a particle diameter of less than 355 μm was measured, and the mass ratio was calculated.
(C) Content of calcium, silicon and aluminum in the regenerated particle aggregate (as oxide)
Elemental analysis was performed with an X-ray microanalyzer (model number: E-MAX · S-2150, Hitachi, Ltd./Horiba, Ltd.).
(D) Average particle diameter of regenerated particles 10 mg of a regenerated particle sample was added to 8 mL of a methanol solution and dispersed with an ultrasonic disperser (output: 80 W) for 3 minutes. This solution was measured with a Coulter counter particle size distribution measuring apparatus (TA-II type, manufactured by COULTER ELECTRONICS) using an aperture of 50 μm. However, for a 50 μm aperture that cannot be measured, a 200 μm aperture was used. Moreover, ISOTON II (trade name, manufactured by COULTER ELECTRONICS, 0.7% high-purity NaCl aqueous solution) was used as the electrolytic solution.
(E) Degree of wire wear Using a wear degree test apparatus (manufactured by Nippon Filcon Co., Ltd.), the degree of wear of the plastic wire was measured for 3 hours at a slurry concentration of 2% by mass.
(F) Productivity The raw material dewatering efficiency, productivity, and electric power required for pulverization were each evaluated in four stages, and evaluated based on the following evaluation criteria.
(Evaluation criteria)
A: All were highly evaluated and the balance was the best.
○: The evaluation may be averaged.
(Triangle | delta): There existed a problem in either the dehydration efficiency, productivity, and the electric power required for a grinding | pulverization.
X: Actual operation was difficult.
(G) Quality stability The degree of variation was measured for each item of whiteness, particle size, and production volume at a fixed time interval, ranked in ascending order of variation, and evaluated based on the following evaluation criteria.
(Evaluation criteria)
A: Up to the top 10 O: 11-22, Δ: 23-25, X: 26 or less (K) Appearance The color of the regenerated particle aggregate was visually observed and classified into white and gray.

CaO, SiO2, and Al2O3 in Table 2 indicate the content ratios of the three components in terms of oxides in the particle constituents, and "Total content ratio" in Table 2 indicates the total content ratio of the three components in the particles.
From the results shown in Table 2, it can be seen that the regenerated particle aggregates of Production Examples 1 to 19 each have a low degree of wire wear and excellent productivity and quality stability. On the other hand, it can be seen that the regenerated particle aggregates of Comparative Examples 1 to 4 all have high wire wear and are inferior in productivity and quality stability.

[Production of Newspaper (Production Examples 1-19 and Comparative Examples 1-7)]
Dinking pulp (DIP), pressed stone ground pulp (PGW), and softwood kraft pulp (NBKP) were blended in the proportions shown in Table 3, and the freeness was 120 mL with a refiner. S. A pulp slurry adjusted to F (based on JIS P 8121) was obtained. To this pulp slurry, 0.5 part by mass of cationized starch is added per 100 parts by mass of absolutely dry pulp, and the regenerated particle aggregates obtained in Production Examples 1 to 19 and Comparative Production Examples 1 to 4 are used as fillers. Aggregates were added at the ratios shown in Table 3 and the pH was adjusted with a sulfuric acid band, and newspapers with basis weights shown in Table 4 were made with a twin wire paper machine. Further, 1 g / m ² of oxidized starch was applied on both sides as a surface sizing agent.
Various physical properties of the obtained newspaper were examined. These results are shown in Table 4. Moreover, commercially available newsprint was prepared as test papers A to C, and various physical properties were examined in the same manner as the newsprints of Production Examples 1 to 19 and Comparative Examples 1 to 4. The results are shown in Table 4 together as Comparative Examples 5 to 7.

The various measured values shown in Tables 3 and 4 were measured by the following methods.
(A) The ratio of each pulp in raw material pulp It measured based on the "fiber composition test method" of JISP8120.
(B) Basis weight It measured based on the "basis weight measuring method" as described in JISP8124.
(C) Density Measured according to “Paper and paperboard—Test method for thickness and density” described in JIS P 8118.
(D) Hot water extraction pH
It was measured according to “Test method for pH of paper, paperboard and pulp-water extract” described in JIS P 8133.
(E) Ash content Measured according to “Paper, paperboard and pulp-ash content test method” described in JIS P 8251.
(F) Cobb water absorption (size)
In accordance with “paper and paperboard—water absorption test method—Cobb method” described in JIS P 8140, the measurement was performed at a measurement time of 10 seconds.
(G) Oil Absorbance Measured with diesel oil No. 1 in accordance with “Oil Absorbency Test Method” described in JIS P 3001-1976.
(H) Whiteness The whiteness was measured in accordance with “Testing Method for Hunter Whiteness of Paper and Pulp” described in JIS P 8123.
(I) White paper opacity It was measured in accordance with “Paper Opacity Test Method” described in JIS P 8138.
(J) Stiffness (MD direction)
It was measured in accordance with “A stiffness test method using a paper Clark stiffness tester” described in JIS P 8143.
(K) Surface strength After passing a paper sample twice through a calendar made of a metal roll in a laboratory at a linear pressure of 40 kg / cm, the surface of the paper sample was subjected to RI tester (manufactured by Akira Seisakusho). Printing was performed using Ink Tack 6 (manufactured by Toyo Ink Manufacturing Co., Ltd.). The state where the fibers per 10 cm ² were peeled off was visually observed and evaluated based on the following evaluation criteria (grade).
(Evaluation criteria)
1: There is considerable peeling of the fiber 2: There is peeling of the fiber 3: Slightly peeling of the fiber 4: Slightly peeling of the fiber 5: Little peeling of the fiber In practice, it is grade 3 at the minimum.

Next, each characteristic was investigated based on the following test examples 1-9 about the newspapers of manufacture examples 1-19 and comparative examples 1-7. The results are shown in Table 5.
[Test Example 1 (Stuffing)]
Using an RI printing suitability tester (manufactured by Akira Seisakusho Co., Ltd.), the newspaper paper surface was repeatedly printed five times with the rubber roll not applied with the test ink. Using a loupe, the surface of the paper web was visually observed in the range of 100 mm × 100 mm, and evaluated based on the following evaluation criteria.
(Evaluation criteria)
A: Very little standing
○: Little standing.
(Triangle | delta): There is a little bit of standing.
×: There are very many standing spots.
[Test example 2 (ink absorption unevenness)]
Using an offset color printer (model number: SYSTEM C-20, manufactured by Komori Corporation), four-color printing was performed in the order of indigo, red, yellow, and black at a printing speed of 160,000 copies / hour. The ink density unevenness of the deep blue / red color portion was visually observed and evaluated based on the following evaluation criteria.
(Evaluation criteria)
A: Ink density unevenness is not recognized at all, and the image is uniform and clear.
○: Ink density unevenness is hardly recognized, and the image is uniform.
Δ: Ink density unevenness is recognized and the image is slightly non-uniform.
X: Ink density unevenness is obvious and the image is non-uniform.
[Test Example 3 (Paper dust accumulation on blanket)]
(1) Using the same offset color printer as in Test Example 2, four-color printing was performed in the order of indigo, red, yellow, and black at the same printing speed. After printing 10,000 copies, the degree of paper powder accumulation on the blanket non-image area was visually observed and evaluated based on the following evaluation criteria.
(Evaluation criteria)
A: Generation of paper dust is not recognized.
○: Slight generation of paper dust is observed, but there is no practical problem.
Δ: The occurrence of paper dust is clearly recognized.
X: A lot of paper dust is accumulated on the blanket, and the blanket is white.
(2) Using a web offset press (Toshiba web offset press, manufactured by Toshiba Corp.), black monochrome printing was performed at a printing speed of 900 rpm. After printing 60,000 copies, the paper dust deposited on the blanket was scraped off, and the mass was measured and expressed as the mass per 100 cm ² . The film thickness of the fountain solution was 0.9 μm.
[Test Example 4 (Opacity after printing)]
Using the same RI printing suitability testing machine as in Test Example 1, printing was performed while changing the ink amount of black ink. The back surface reflectance after printing with respect to the back surface reflectance before printing (opposite surface of the printing surface) when the reflectance of the printing surface was 9% was determined. A spectral whiteness colorimeter (manufactured by Suga Test Instruments Co., Ltd.) was used for the reflectance measurement.
[Test Example 5 (Printing White)]
The same offset color printing machine as in Test Example 2 was used, and single-color printing of offset rotary printing ink (black) was performed at a dot area ratio of 30 to 100%. About a solid part with a halftone dot area ratio of 100%, the degree of white spots on the printed surface was visually observed and evaluated based on the following evaluation criteria.
(Evaluation criteria)
A: Almost no white spots are observed.
○: Little white spots are observed.
Δ: White spots are observed.
X: White spots are remarkable.
[Test Example 6 (Nepari property)]
Two newspaper paper samples were cut to a suitable size and immersed in water for 10 seconds, and then the two sheets were quickly brought into close contact and passed through a calendar at a linear pressure of 100 kg / cm. After drying at room temperature for 24 hours, the peel strength of the two sheets was measured using a tensile tester (model number: Autograph AGS-500NG, manufactured by Shimadzu Corporation). In addition, the larger the numerical value, the higher the Nepari property (adhesiveness).
[Test Example 7 (ink drying property)]
Using the same offset color printing machine as in Test Example 2, four-color printing was performed in the order of indigo, red, yellow, and black with newspaper printing ink having a vegetable oil content of 45% at the same printing speed. Overlap the 500 copies of the printed material so that the printed surface and the white paper surface overlap, and leave it for 1 day under a load of 5 kgf (about 49 N), and then visually observe the degree of dirt on the white paper surface based on the following evaluation criteria: And evaluated.
(Evaluation criteria)
(Double-circle): Dirt is hardly recognized.
○: Only a small amount of dirt is observed.
Δ: Dirt is observed.
X: Dirt is remarkable.
[Test Example 8 (Number of sheet breaks)]
Using an offset rotary press (Toshiba offset rotary press, manufactured by Toshiba Corporation), black monochrome printing was performed at a printing speed of 900 rpm, and the number of occurrences of sheet breakage was measured during 60,000 copies.
[Test Example 9 (Back-through)]
Using the same web offset press as in Test Example 8, black single color printing was performed at the same printing speed. After printing 60,000 copies, the black solid surface was visually observed from the back side and evaluated based on the following evaluation criteria.
(Evaluation criteria)
A: Almost no see-through is observed.
○: Only a small amount of strikethrough is recognized.
(Triangle | delta): See-through is recognized.
X: The showthrough is remarkable.

From the above results, the newspapers of Production Examples 1 to 19 contain calcium, silicon, and aluminum in an amount of 90% by mass or more, and the deinked floss is made of recycled particle aggregates as raw materials, and the waste paper pulp is in an amount of 50% by mass or more. Since it is made by adding paper to the raw material pulp that contains it, not only can it be obtained at low cost by recycling resources, but it also has an appropriate basis weight, density and hot water extraction pH, whiteness, stiffness and surface strength. It can also be seen that it has both excellent opacity and paper strength. Moreover, these newsprints of Production Examples 1 to 19 have no or little fluffing, ink absorption unevenness, accumulation of paper dust on the blanket and paper breakage, and high opacity after printing. It can be seen that it has characteristics that are very suitable for, for example, high speed web offset printing because there is little or no.
On the other hand, the newspapers of Comparative Examples 1 to 4 are not deinked floss, but regenerated particles made from paper sludge are used as fillers, and the amount of used paper pulp is small as raw material pulp. Therefore, resource saving and cost reduction are not achieved, and in addition to eruption, ink absorption unevenness, paper powder accumulation on the blanket, and paper breakage, most of opacity after printing, white spots on prints and back-through are bad. As a result, it is understood that the characteristics suitable for high-speed offset printing are not provided.
In addition, the commercially available newsprint of Comparative Examples 5 to 7 is also less crisp, ink absorption unevenness, paper powder accumulation on the blanket, paper breakage, opacity after printing, and printing blank compared to Production Examples 1 to 19. It can be seen that the present invention has characteristics more suitable for high-speed, color, and high-definition offset rotary printing, with almost no result of bad show-through and show-through.

  The newsprint of the present invention can be used as newsprint particularly suitable for high-speed offset color printing in, for example, satellite-type or tower press-type offset color printing machines.

Claims (4)

A method for producing newsprint with a filler added to pulp,
The main material is deinked floss discharged from the waste paper processing process as the filler,
Producing a regenerated particle aggregate obtained by aggregating the main raw material through the dehydration step, the drying step, the firing step, and the pulverization step and aggregating in the firing step, and adjusted to have the following composition:
This regenerated particle aggregate is internally added to the pulp,
The pulp comprises 50-100% by weight of waste paper pulp,
The basis weight according to JIS P 8124 is 37 to 48 g / m ² ,
The paper ash content measured according to JIS P 8251 is contained in the paper in an amount of 4 to 15% by mass,
Clark stiffness was measured in accordance with JIS P 8143 is 30~55cm ^3/100,
The hot water extraction pH according to JIS P 8133 is 6.0 to 9.5.
A method for producing recycled particle-added newsprint.
(composition)
The regenerated particle aggregate contains calcium, silicon, and aluminum as constituents of the regenerated particle aggregate in a mass ratio of 30 to 82: 9 to 35: 9 to 35 in terms of oxides. The regenerated particle aggregate in which the total content of the calcium, the silicon, and the aluminum is 93% by mass or more in the regenerated particle aggregate component among the components of the aggregate.   The method for producing a newspaper with internal regenerated particles according to claim 1, wherein the blank paper opacity measured in accordance with JIS P 8138 is 91 to 95%. The 10-second bump size based on JIS P 8140 is 30 to 300 g / m ² .
3. A method for producing newspaper with internal regenerated particles according to claim 1 or 2. Oil absorption based on JIS P 3001 is 50 to 150 seconds,
The manufacturing method of the regenerated particle internal newsprint of any one of Claims 1-3.