JP5483918B2 - Book paper and manufacturing method thereof - Google Patents

Description

In the present invention, from the viewpoint of global environmental conservation and effective use of resources, waste paper pulp and inorganic particles in the waste paper pulp, and the deinking floss separated from the pulp fiber in the deinking process of the waste paper processing equipment as a main raw material, The present invention relates to a book paper in which regenerated particles obtained by dehydrating, drying, burning and pulverizing main raw materials are contained in a base paper, and a method for producing the same.

  Book paper used for comics and the like is required to have a thick paper thickness (low density and high bulk) and high whiteness with respect to the rice paper. Therefore, conventionally, it has become the design which mix | blended many bulky mechanical pulps with 60-100 mass%. However, when a large amount of mechanical pulp is blended, there is a problem that black defects occur due to pitch and the like. Therefore, it is generally known to reduce the size of black defects by adding a coagulant or a flocculant.

  Moreover, since whiteness falls when many mechanical pulps are mix | blended, inorganic compounds, such as calcium carbonate, are generally mix | blended. However, when a large amount of an inorganic compound is blended, the bulk is difficult to be produced, the surface strength is lowered, and paper peeling occurs at the time of printing, so the blending amount is limited. On the other hand, if the blending amount of the inorganic compound is small, sufficient opacity cannot be obtained, and there may be a case where a showthrough occurs when printing on book paper.

  Therefore, as shown in Patent Document 1 and Patent Document 2, for example, the main material is deinked floss separated from pulp fibers in the deinking process of the used paper processing equipment, and the main material is dehydrated, dried, burned and pulverized. There has been proposed a book paper in which the regenerated particle agglomerates obtained through the above are blended as a filler.

  However, in such a conventional method for producing a regenerated particle aggregate, the regenerated particle raw material turns yellow due to high temperature combustion, so the whiteness of the regenerated particle aggregate is low. Therefore, in order to increase the whiteness, it is necessary to increase the blending amount of the regenerated particle aggregate. However, if the blending amount of the regenerating particle aggregate is increased, the ash content in the paper increases, so that the bulk is not easily generated. There was a problem of becoming.

  Furthermore, when the above-mentioned recycled particle aggregate is blended with raw pulp containing 30% by mass or more of mechanical pulp, there is a problem that aggregates are generated and black defects are generated on the paper surface. This is considered to be due to the fact that the pitch derived from mechanical pulp and the regenerated particle agglomerate are bonded and grow into a large agglomerate by the coagulant / aggregant added later.

  In addition, as shown in Patent Document 3, for example, means using hardwood mechanical pulp and a bulking agent has been proposed. However, when a bulking agent is added, the bonding strength between fibers decreases, so that the surface strength decreases, and during printing, Paper peeling or paper breakage may occur, which is a practical problem.

JP 2008-156774 A JP 2007-146351 A JP 2006-225774 A

The present invention has been made in view of the above-described circumstances, and its object is to separate from pulp fibers in the deinking process of used paper processing equipment for producing used paper pulp without adding a bulking agent. Using the deinked floss as the main raw material, it consists of a dehydration process, a drying process, and at least a first combustion process and a second combustion process, and burns at 300 to 500 ° C. in the first combustion furnace of the first combustion process. After performing the treatment, in the second combustion furnace of the second combustion process, adding the regenerated particles obtained through the combustion process for recombusting the main raw material burned in the first combustion process and the pulverization process Then, it is providing the book paper which is bulky, does not have a black defect, has high whiteness, and does not show through, and its manufacturing method .

The above object of the present invention is to have a mechanical pulp blending ratio measured in accordance with JIS P8120 (1998) of 30 to 80% by mass, and to have a base paper with a filler internally added. And a cationic coagulant and an anionic flocculant, and the recycled particles are mainly made of deinked floss separated from pulp fibers in the deinking process of the used paper processing equipment for manufacturing used paper pulp. The dehydration step, the drying step, and at least the first combustion step and the second combustion step, the main raw material is dehydrated to a moisture content of 40 to 90% in the dehydration step, and the first combustion step of the first combustion step A combustion step of again burning the main raw material burned in the first combustion step in the second combustion step of the second combustion step after performing drying and combustion treatment at 300 to 500 ° C. in one combustion furnace; Obtained through the crushing process This is accomplished by providing a book paper characterized by being.

Further, the above object of the present invention is that the regenerated particles have a whiteness of 75 to 85%, and the base paper has an ash content of 5 to 20% by mass measured according to JIS P8251 (2003). Further, by providing a book paper characterized in that the density is 0.4 to 0.6 g / cm ³ and the whiteness according to JIS P8148 (2001) is 60 to 75%, Is achieved.

The above-mentioned object of the present invention is achieved more effectively by providing a book paper characterized in that the anionic flocculant has an anion amount of 0.5 to 6.0 meq / g. .

Furthermore, the object of the present invention is to add a filler to the raw material pulp in which the mechanical pulp is blended so that the blending ratio of the mechanical pulp measured in accordance with JIS P8120 (1998) is 30 to 80% by mass. A book paper manufacturing method comprising a base paper, wherein regenerated particles, a cationic coagulant, and an anionic flocculant are added as the filler,
This is achieved more effectively by providing a method for producing book paper, wherein the regenerated particles are produced by a production process comprising the following (a) to (d).
(I) a dehydration step in which the deinking floss separated from the pulp fiber in the deinking step of the used paper processing facility for producing the used paper pulp is used as a main raw material, and the main raw material is dehydrated to a moisture content of 40 to 90%;
(B) Drying and first combustion stroke in which the main raw material is dried and burned at 300 to 500 ° C. in a first combustion furnace;
(C) a second combustion step in which the main raw material burned in the first combustion step is burned again in a second combustion furnace;
(D) After the second combustion step, regenerated particles are obtained by pulverization in a pulverization step.

  According to the book paper according to the present invention, the blending ratio of mechanical pulp measured in accordance with JIS P8120 (1998) is 30 to 80%, and has a base paper in which a filler is internally added. Recycled particles, a cationic coagulant and an anionic flocculant are contained, and the recycled particles are mainly deinked floss separated from pulp fibers in the deinking process of the used paper processing equipment for producing used paper pulp. The raw material comprises at least two stages of a dehydration process, a drying process, and a first combustion furnace and a second combustion furnace. After the combustion treatment is performed at 300 to 500 ° C. in the first combustion furnace, the second combustion furnace Thus, it is obtained through a combustion process in which the main raw material combusted in the first combustion furnace is burned again and a pulverization process, so that there is no black defect, a high whiteness, and a bulky book paper. Can be obtained.

It is a schematic diagram of a manufacturing facility. It is a schematic diagram of a 2nd combustion furnace, (a) is a longitudinal cross-sectional view, (b) is an expanded view of an inner surface.

  Hereinafter, the book paper according to the present invention will be described in detail by taking as an example a case where the base paper is composed of two paper layers, a front layer and a back layer. The book paper according to the present invention is not limited to the following embodiments, and it goes without saying that the configuration thereof can be changed as appropriate without departing from the scope of the claims.

  The book paper according to the present invention (hereinafter referred to as “book paper”) has a water-soluble resin applied to the front and / or back of the base paper, and in this base paper, JIS P8120 (1998). The blending ratio of mechanical pulp measured according to the above is 30 to 80% by mass, and a filler is internally added.

  As the raw material pulp forming each layer of the base paper of this book paper, the main raw material is a blend of mechanical pulp and hardwood bleached kraft pulp (LBKP), and 30 to 80% by mass of mechanical pulp in all pulp, LBKP 20-70 mass% is mix | blended. Mechanical pulp is bulky but has low whiteness. For this reason, when the compounding quantity of mechanical pulp is less than 30 mass%, it is difficult to obtain the desired volume of the book paper. On the other hand, if the blending amount of mechanical pulp exceeds 80% by mass, the book paper can be made bulky, but it is difficult to obtain the desired whiteness of the present application.

  The mechanical pulp is not particularly limited, and various types can be used. However, coniferous trees are more suitable than hardwoods because they are more bulky. There is no particular limitation on the method for producing mechanical pulp, and a pulping method for mechanically pulverizing wood such as crushed wood pulp (GP) and refiner pulp crushed wood pulp (RGP), or thermomechanical pulp (TMP), chemithermomechanical pulp. Any of mechanical pulping methods such as (CTMP), chemiground pulp (CGP), and semi-chemical pulp (SCP) may be used. Also, the mechanical pulp bleaching method is not particularly limited, and various conventionally known means can be used.

  The raw material pulp that forms the base paper of this book paper is not particularly limited as long as mechanical pulp is blended in an amount of 30 to 80% by weight. Hardwood bleached kraft pulp (LBKP), hardwood unbleached Various known materials such as kraft pulp (LUKP), softwood bleached kraft pulp (NBKP), softwood unbleached kraft pulp (NUKP), softwood, hardwood sulfite pulp, and other chemically treated pulp Can be used. In addition, waste paper pulp made from used waste paper such as waste newspaper, upper white waste paper, Kent waste paper, imitation waste paper, and OA waste paper can also be used. Furthermore, non-wood fibers such as kenaf, hemp, and cocoon, which are fiber materials other than wood, can also be used. However, non-wood pulp has low pulp strength, and the unit price of the pulp itself is high, which increases costs. It is preferable to use kraft pulp and waste paper pulp.

  Among these raw material pulps, in particular, in order to maintain the whiteness while maintaining the desired volume of the book paper, 30 to 80% by mass of mechanical pulp is blended, and further LBKP or recycled paper pulp is 20 to 70% by mass. % Is optimal.

  In the raw material pulp of the book paper, at least specific regenerated particles, a cationic coagulant, and an anionic flocculant are internally added as fillers. Since the regenerated particles internally added to the book paper have both anionic and cationic properties, a cationic coagulant and an anionic flocculant that work effectively on each ionicity are internally added. Thereby, this book paper can be made bulky with high whiteness. In particular, by adding a cationic coagulant and an anionic flocculant, black defects can be eliminated and the whiteness can be effectively increased. In addition, when fillers (for example, calcium carbonate) other than the above-mentioned specific regenerated particles are used alone, the opacity is lower than when specific regenerated particles are used, and the back-through easily occurs. The reason is not clear, but when a cationic coagulant and an anionic flocculant are used in combination, the filler having only one charge of either anion or cation is poorly dispersed and the filler is not evenly distributed in the paper. This is thought to be the cause.

  As the cationic coagulant internally added to the book paper, polyacrylamide, polyethyleneimine, methacrylic acid, polyamine, polydadomac, polyacrylamide, and the like can be used, and polyacrylamide that generates less aggregates is particularly preferable. . It is desirable to add this cationic coagulant especially before the screen. This is because the cationic coagulant is divided by the share of the screen, and it is considered that aggregation is caused again by an anionic flocculant (described later) added thereafter.

  Moreover, colloidal silica, polyacrylamide, bentonite, etc. can be used as the anionic flocculant internally added to the book paper. Among these, colloidal silica is particularly preferable.

  The anionic flocculant preferably has an anion amount of 0.5 to 6.0 meq / g, more preferably 0.6 to 3.0 meq / g. If the amount of anion is less than 0.5 meq / g, it is internally added to the book paper, and the yield of regenerated particles described later deteriorates. On the other hand, when the amount of anions exceeds 6.0 meq / g, the amount of aggregates increases, it is difficult to reduce black defects, and it is difficult to increase the whiteness of book paper. The anion amount can be measured with a cation demand measuring device (model number PCD03) manufactured by mutek. This measuring device puts the sample in the cell of the test machine, and when the upper and lower pistons are operated, the sample liquid flows between the cell cylinder and the piston, and electricity is generated by the distortion of the surface charge of the colloidal particles. The charge requirement amount is measured by polymer electrolyte measurement.

  The regenerated particles internally added to the book paper will be described later.

  Moreover, in order to make this book paper more bulky, a conventionally known bulking agent can be internally added. The type and blending amount of the bulking agent are not particularly limited. However, increasing the blending amount lowers the surface strength and may cause paper peeling at the time of printing.

  In addition, a conventionally known sulfuric acid band can be blended to fix the filler to the pulp, and conventionally known fluorescent dyes, coloring dyes, and coloring pigments are also arbitrarily selected in order to improve whiteness and apparent whiteness. You can choose.

  Furthermore, known additives can be used as additives to be added to the paper slurry. For example, starches, vegetable gums, aqueous cellulose derivatives and the like are used as paper strength enhancers, and rosin, starch, and the like as sizing agents. CMC (carboxyl methyl cellulose), polyvinyl alcohol, alkyl ketene dimer, ASA (alkenyl succinic anhydride), neutral rosin, and the like, and polyacrylamide and copolymers as the yield improver. Furthermore, you may add colorants, such as dye and a pigment, as needed.

  In addition, a coating layer may be provided by applying a water-soluble resin to at least the surface of the base paper of the book paper. As a result, it is possible to prevent paper peeling during printing.

  Moreover, as water-soluble resin which can be apply | coated to the base paper of this book paper, starches, polyacrylamide, a copolymer, polyvinyl alcohol, etc. can be used, for example.

  The base paper of this book paper formed as described above has an ash content (hereinafter, simply referred to as “ash content”) measured in accordance with JIS P8251 (2003) of 5 to 20 mass%. When the ash content is less than 5% by mass, the whiteness of the book paper tends to be low. On the other hand, if the ash content exceeds 20% by mass, the density of the book paper increases, and it becomes difficult to obtain a bulky book paper that is the object of the present invention.

The book paper has a density of 0.4 to 0.6 g / cm ³ . Thereby, the object of the present invention can be achieved effectively. If the density is less than 0.4 g / cm ³ , the inside of the paper layer becomes rough and the internal strength may be lowered, so troubles such as paper dust may occur when cutting the book paper. It becomes easy. On the other hand, when the density exceeds 0.6 g / cm ³ , it becomes difficult to provide a bulky book paper that is an object of the present invention.

  Further, the book paper has a whiteness (hereinafter referred to as “product whiteness”) in accordance with JIS P8148 (2001) of 60 to 75%, preferably 65 to 75%. If the product whiteness is less than 60%, the book paper looks black or yellow, which tends to cause problems in the printed finish. On the other hand, when the product whiteness exceeds 75%, the printed finish becomes clear, but the show-through tends to be conspicuous.

  Next, regenerated particles that are fillers that can be internally added to the base paper of the book paper will be described. The method for producing regenerated particles used in the present invention is a deinking process of a used paper processing facility for producing used paper pulp, with the deinking floss separated from the pulp fibers as the main material, dehydrating and drying the main material, Recycled particles are obtained through each step of combustion and pulverization, and the drying and combustion step is a first combustion furnace (internal heat kiln furnace) to which the raw material after dehydration is dried and burned in series. And a second combustion furnace after the deinking floss burned in the first combustion furnace is burned again, and has at least two stages of combustion processes, and then pulverized to obtain regenerated particles .

  More specifically, the combustion process is performed in the first combustion furnace at a temperature of 300 to 500 ° C. so that the oxygen concentration in the first combustion furnace (internal heat kiln furnace) is 0.2 to 20%. Furthermore, a 2nd combustion furnace performs a combustion process on the combustion thing from a 1st combustion furnace at the temperature of 550-780 degreeC.

  However, the deinking floss separated from the pulp fiber in the deinking process of the used paper processing equipment for producing the used paper pulp, which is the main raw material of the regenerated particles to be used in the present invention, contains inorganic fine particles and is also used paper. It contains many fine fibers that are difficult to use as pulp, latex that is an organic polymer frequently used in coated paper, and ink components applied by printing. For this reason, in the combustion process of the combustion process, since the deinking floss itself generates a combustion reaction (oxidation) and burns, heat is generated more than the heat treatment with hot air, and there is a problem that causes excessive combustion of the raw material. did.

  Such excessive combustion (1) yellowing of the raw material due to high-temperature combustion causes a decrease in whiteness, (2) hard material such as gehlenite is likely to occur due to melting of the raw material, and the degree of wire wear in papermaking equipment (3) In order to form agglomerates by melting the raw material, the pulverization energy is increased and the processing efficiency is lowered in the subsequent fine pulverization step. Since it is melted first, the combustion reaction (oxidation reaction) does not proceed to the inside of the raw material, and organic matter (carbon) remains, resulting in problems such as a decrease in whiteness.

  Therefore, as a means for solving such problems, paying attention to measures for controlling excessive combustion, and as a result of intensive studies, the combustion process is composed of at least two stages of a first combustion furnace and a second combustion furnace, Combustion temperature (combustible gas) generated by gasification of organic components contained in the deinking floss without burning the main deinking floss as the main raw material. It is found that the above problem can be solved by keeping only the temperature necessary for the reaction and promoting only the combustion reaction (oxidation reaction) of the organic component gas, and the regenerated particles internally added to the book paper are completed. It is a thing.

  Moreover, in the 1st combustion furnace, the oxygen concentration 0.2-20% required in order to burn the deinking floss which is a main raw material is ensured. As a result, an in-furnace environment in which combustion is promoted is generated, and thus excessive deinking floss combustion is likely to occur.

  Furthermore, in order to prevent excessive combustion of the deinking floss, it has been found that a measure for increasing the water content of the deinking floss as a main raw material in addition to supplying hot air is effective. More specifically, the deinking floss as the main raw material has a moisture content of 40 to 90%, preferably 40 to 70%, more preferably 45 to 70% after dehydration. It has been found that the supply to the first combustion furnace is suitable for preventing excessive combustion of the deinking floss. That is, by supplying deinking floss as a main raw material into the first combustion furnace in the first combustion process in a high water content state, moisture is evaporated in the first combustion furnace, and thereby the temperature in the first combustion furnace. Decreases. As a result, it is considered that self-combustion of the deinking floss can be suppressed, combustion of only the generated combustion gas (combustible gas) can be promoted, and excessive combustion can be suppressed.

  Furthermore, on the inner wall in the second combustion furnace of the second combustion process, which is a combustion process after the first combustion process, parallel to the spiral lifter and / or the axis center from one end side to the other end side. It is preferable to arrange a parallel lifter, whereby the raw material can be combusted uniformly, and the quality of the regenerated particles can be made uniform.

  That is, as described above, in the first combustion furnace in the first combustion step, the deinking floss as the main raw material is burned at a low combustion temperature of 300 to 500 ° C., and is contained in the raw material from the raw material. It is necessary to burn as much carbon as possible, which causes organic matter to become a combustion gas, burns (oxidizes) this combustion gas to obtain a homogeneous combustion product of the first combustion furnace, and causes a decrease in whiteness. There is. For this reason, it is necessary to burn the raw material slowly, and in order to continuously carry out uniform combustion as much as possible, the most suitable measure is to appropriately control the raw material conveyance speed in the second combustion furnace in the second combustion step. The present inventors have also found that it is possible to adjust the feed speed of the raw material by using a lifter as a means. However, since known lifters are generally manufactured from iron materials, iron content is contained in the raw material as contamination, resulting in a decrease in whiteness due to iron oxidation and a reduction in the quality of regenerated particles. Cause the problem of Therefore, by providing a stainless steel lifter in the second combustion furnace, a technology that can produce high-quality regenerated particles with uniform firing quality, such as no iron oxidation problem and no reduction in whiteness, is found. It was.

  As the structure of the second combustion furnace, either an external heat kiln furnace or an internal heat kiln furnace can be adopted as appropriate. However, in the external heat kiln furnace, the direct flame of the burner is not directly exposed to the raw material, so that the excessive combustion of the raw material can be prevented, the combustion product of the second combustion furnace can have a uniform firing quality, and high whiteness is achieved. There is an advantage that it can be obtained. On the other hand, the internal heat kiln furnace has an advantage that the refractory attached inside has heat insulation and at the same time emits far infrared rays and can be heated with a small amount of heat. Therefore, regarding the structure of the second combustion furnace, either an external heat kiln furnace or an internal heat kiln furnace can be appropriately selected in view of these conditions, but it is optimal to provide a lifter for any of the methods.

  More preferably, an internal heat source is used as the first first combustion furnace, and an external heat source is used as the second second combustion furnace. As these combustion furnaces, various conventionally used furnaces such as a stalker furnace (fixed bed), a fluidized bed furnace, a cyclone furnace, and a kiln furnace can be used. However, as these combustion furnaces have repeatedly studied the production of regenerated particles in the respective combustion furnaces, the following matters have become clear.

  In other words, for the stalker furnace (fixed bed), it is difficult to adjust the degree of combustion of the deinking floss, and the combustion products are not uniform. Not suitable because it occurs. Since air is blown up and burned under the combustion material through the grate, calcium carbonate or the like becomes fly ash and is sent to the exhaust gas facility together with the exhaust gas.

  As for the fluidized bed furnace, since a particulate fluid medium such as silica sand is used as the fluid medium in the furnace, there is a problem that the silica sand is mixed into the regenerated particles and the quality is deteriorated, and the silica sand is used in the present invention. Hardness is higher than regenerated particles, making it difficult to grind uniformly. After the cinnabar sand is mixed in the fluidized bed and burned, the cinnabar sand and the burned material are separated, and the cinnabar sand is returned to the combustion furnace, and only the burned material is taken out. Is difficult. In addition, since the regenerated particles are burned in a state of floating on the cinnabar sand, it is difficult to adjust the degree of combustion, and the quality of the obtained combustion product varies. Furthermore, since the combustion products are burned while passing through a stoker (stepped shape) of the combustion furnace with a predetermined width, the ash is not sufficiently stirred, and variation occurs in combustion in the width direction. Further, since silica sand has a high hardness, there is also a problem that the combustion products are pulverized by friction and collision, and fly ash is discharged out of the system, resulting in a decrease in yield.

  About a cyclone furnace, since a combustion thing passes the inside of a furnace instantly, the fixed carbon in a combustion substance cannot be burned enough, but it leads to the fall of the whiteness of a reproduction | regeneration particle | grain. Furthermore, since the fine particles are not separated by the cyclone and are sent to the exhaust gas treatment process together with the exhaust gas, the yield decreases.

  Therefore, as a result of considering the above problems of each furnace, the combustion furnace used for the production of regenerated particles used in the present invention includes kiln furnace, fluidized bed furnace, stalker furnace, cyclone furnace, semi-dry distillation and negative pressure combustion. Various known combustion furnaces such as a type furnace can be used, but it is particularly preferable to use a kiln furnace. Furthermore, a well-known combustion method such as an indirect heating type combustion furnace using heavy oil or the like as a heat source may be employed as the second external combustion furnace.

  More preferably, a method is used in which the drying step and the combustion step are performed in a series of steps after the raw material has undergone the dehydration step. In this method, as the first combustion furnace of the first combustion step, the combustion time (residence time) is 30 to 90 minutes, preferably 40 to 80 minutes, more preferably 50 to 70 minutes, preferably the main body is placed horizontally. Using an internal heat (direct heating) kiln furnace that rotates around the central axis, the raw material after the dehydration process is dried and the first combustion is performed. Also, as the second combustion furnace of the second combustion process, the combustion time ( Residence time) is 60 minutes or more, preferably 60 to 240 minutes, more preferably 90 to 150 minutes, particularly preferably 120 to 150 minutes, preferably external heat (indirect heating) in which the main body is placed horizontally and rotates around the central axis ) Using a kiln furnace, in particular, an external heat electric furnace whose combustion temperature can be easily adjusted, the combustion product obtained in the first combustion path is burned again.

  As described above, when an internal heat kiln furnace capable of performing drying and combustion in one furnace is used as the first combustion furnace, it is gradually and stably from the supply port to the discharge port of the first combustion furnace. In addition, drying and combustion proceed, and the pulverization of the combustion product can be suppressed. In addition, when an external heat kiln furnace capable of performing drying and combustion in one furnace is used as the second combustion furnace, the combustion product is discharged from the end of the second combustion furnace with a predetermined residence time and discharged at the other end. Since the heat can be discharged from the outlet and the uniform heat is applied to the combustion product by the external heat, the combustion becomes uniform and does not cause variations in combustion. Furthermore, since the combustion product is gently stirred by friction caused by the rotation of the inner wall of the kiln furnace, the pulverization of the combustion product can be further suppressed. As a result, the quality and shape of the final combustion product are stabilized. That is, as described above, the drying process and the combustion process are performed in two stages using at least two combustion furnaces, preferably using an internal heat kiln furnace and an external heat kiln furnace. High regenerated grains can be obtained.

  In addition, since an external heat kiln furnace becomes a structure which provided the heating equipment in the outer side of the kiln furnace, in order to dry and burn a combustion substance indirectly, a lot of heat sources are needed. Therefore, when an external heat kiln furnace is used as the first combustion furnace, the raw material after the dehydration step is in a high water content state as described above, and thus the drying / combustion efficiency is lowered. As a result, the productivity of the regenerated particles is deteriorated and the temperature is difficult to control, so that a large energy cost is required and the effect on the cost becomes extremely low.

  Further, when an internal heat kiln furnace is used as the second combustion furnace, the combustion heat is transferred to the internal heat kiln furnace unless a large amount of dilution air is introduced in the combustion of the remaining carbon of the combustion product obtained in the first combustion furnace. It is difficult to convey uniformly inside the furnace, and it is difficult to adjust the temperature in the furnace. The problem occurs. Furthermore, a heavy oil burner is usually used for heating the internal heat kiln furnace, but particles with low whiteness such as heavy oil combustion residual carbon and sulfur oxide are generated, resulting in a decrease in whiteness and variations in the resulting regenerated particles. And it becomes difficult to obtain uniform quality.

  Furthermore, the internal heat kiln furnace or the external heat kiln furnace used as the preferred first combustion furnace and the second combustion furnace is a hexagonal or octagonal internal refractory instead of a circumferential shape. Can be lifted and stirred without slipping. However, in reality, since the kiln furnace is cylindrical, it is optimal to provide a lifter for stirring the combusted material because the raw material can be uniformly burned and the quality can be made uniform. This is also considered to be related to intentionally burning the entire raw material at a low temperature of 300 to 500 ° C. in the first combustion furnace.

Next, an example of a method for producing regenerated particles used for the book paper will be described with reference to the drawings.
〔Overview〕
FIG. 1 is a manufacturing equipment flow diagram according to an embodiment of recycled particles internally added to the base paper of the book paper. As will be described below, the production process of the regenerated particles includes a dehydration process, a drying / combustion process, and a pulverization process. In addition to this, the deinking floss aggregation process or granulation process, and each process A classification step or the like may be provided between them. This equipment is equipped with various sensors, and controls the state of the combustibles and equipment, the processing speed, and the like.

  The deinking floss separated from the pulp fiber in the deinking process for producing the waste paper pulp not shown is subjected to various operations, and the moisture content is 40 to 90%, preferably 45 to 70 by a known dehydration equipment not shown. %, More preferably 50 to 60% high water content. Furthermore, it is desirable that the raw material 10 after such dehydration is pulverized by a pulverizer (or pulverizer) (not shown) so as to have a particle diameter of 40 mm or less.

  The raw material 10 is cut out from the storage tank 12, and is charged from the first combustion furnace 14 from one side of the first combustion furnace 14 which is an internal heat kiln furnace in which the main body is placed horizontally and rotates around the central axis by the charging machine 15. Is charged. Further, an exhaust gas chamber 16 is provided on one side of the first combustion furnace 14, and an exhaust chamber 18 is provided on the other side. The hot air passes through the discharge chamber 18, is blown from the other side of the first combustion furnace 14, is charged from the one side, and is sequentially transferred to the other side as the first combustion furnace 14 rotates. Drying and burning are performed.

  Here, it is desirable that the hot air blown into the first combustion furnace 14 has an oxygen concentration of 0.2 to 20%. The furnace temperature is 300 to 500 ° C, preferably 400 to 500 ° C, more preferably 400 to 450 ° C. Hot air is blown from a hot air generating furnace 20 provided with a burner 20A.

  From the exhaust gas chamber 16, exhaust gas subjected to drying and combustion is sent into the recombustion chamber 22. The fine powder of the combustion material contained in the exhaust gas is discharged from the lower part of the exhaust gas chamber 16 and reused. The exhaust gas is recombusted by the burner in the recombustion chamber 22, precooled by the precooler 24, passed through the heat exchanger 26, and discharged from the chimney 30 by the induction fan 28. Here, after raising the temperature of the outside air, the heat exchanger 26 is sent to the hot air generating furnace 20 and used for the hot air blown from the first combustion furnace 14 to recover the heat of the exhaust gas from the exhaust gas chamber 16. It is like that. The treatment of exhaust gas is effective for removing harmful substances contained in the exhaust gas.

  Combustion products that have undergone drying and combustion treatment in the first combustion furnace 14 are charged into a second combustion furnace 32 that is an external heat kiln furnace in which the main body is placed horizontally and rotates around the central axis. The particle size of the combusted material to be charged is preferably 40 mm or less. As a heat source in the second combustion furnace 32, it is preferable to use an electric adjustment that allows easy temperature control in the second combustion furnace 32 and easy temperature control in the longitudinal direction. Therefore, it is desirable to be an external heating type combustion furnace in which the combustion product obtained from the first combustion furnace 14 indirectly is burned again by an electric heater.

  In the second combustion furnace 32, the oxygen concentration is 5 to 20%, preferably 10 to 20%, more preferably 10 to 15% by an air or oxygen supply mechanism (not shown) for adjusting the oxygen concentration. To burn. As temperature, it is 550-780 degreeC, Preferably it is 600-750 degreeC. The residence time in the second combustion furnace 32 is 60 minutes or longer, preferably 60 to 240 minutes, more preferably 90 to 150 minutes, and particularly preferably 120 to 150 minutes, in order to completely burn the remaining carbon. .

  The combusted material that has been burned is cooled by a cooler 34, and then sorted by a particle size sorter 36 such as a vibration sieve, and adjusted to a target particle size in a grinding process using a wet grinding machine or the like. The burned product is temporarily stored in the combusted product silo 38 and is sent to the application destination of the pigment and filler.

  In addition, although the case where deinking floss was used as a raw material was illustrated, the combustion material which used as a raw material what mixed papermaking sludges, such as papermaking sludge in a papermaking process, with deinking floss as a main raw material may be sufficient. .

As mentioned above, although the outline | summary of the manufacturing process of regenerated particle was demonstrated, the detail and an application example are demonstrated below.
〔material〕
In the used paper pulp manufacturing process, in order to continuously produce used paper pulp of stable quality, used paper is selected and selected, and used paper of a certain quality is used. For this reason, the types, ratios, and amounts of inorganic substances brought into the used paper pulp manufacturing process are basically constant. Moreover, even when plastics such as vinyl and film, which cause fluctuations in unburned materials in the method for producing regenerated particles, are contained in the waste paper, these foreign matters are not before the deinking process to obtain deinking floss. Can be removed in stages. Accordingly, the deinking floss is a raw material for producing regenerated particles having extremely stable quality as compared with paper sludge generated in other processes such as a factory drainage process and a papermaking raw material preparation process.

  The deinking floss referred to in the present specification refers to what is separated from the pulp fiber in the deinking process for removing ink adhering to the used paper in the used paper processing process for producing the used paper pulp.

[Dehydration process]
For further dehydration of the deinking floss, known dehydration means can be used as appropriate. In one example of this embodiment, the deinking floss is dehydrated by separating water from the deinking floss by a dehydrating means such as a screen. In the screen, it is preferable that the deinking floss dehydrated to 90 to 97% is sent to, for example, a screw press and further dehydrated to a predetermined moisture.

  If the moisture content of the raw material 10 after dehydration exceeds 70%, the temperature of the drying / combustion treatment in the first combustion furnace 14 will be lowered, the energy loss for heating will be great, and the non-uniform combustion of the raw material 10 will occur. It becomes easy and it becomes difficult to advance uniform combustion. Further, there are problems that the moisture in the exhaust gas to be discharged increases, the recombustion treatment efficiency is reduced in dioxin countermeasures, and the load on the exhaust gas treatment facility is increased. Moreover, when the moisture content of the raw material 10 after dehydration is as low as less than 40%, it causes excessive combustion of the deinking floss.

  As has been clarified in the above description, if dewatering of the deinking floss is performed in a multi-stage process and abrupt dewatering is avoided, the outflow of inorganic substances can be suppressed and there is no possibility that the deinking floss flock becomes too hard. In the dehydration treatment, an auxiliary agent for improving the dehydration efficiency such as an aggregating agent for aggregating the deinking floss may be added, but it is preferable to use an aggregating agent that does not contain iron. When iron is contained, it causes a problem of lowering the whiteness of the regenerated particles due to oxidation of iron.

  The deinking process of deinking floss is preferably adjacent to the manufacturing process of regenerated particles used in this book paper in terms of production efficiency. It is also possible to transport the liquid to the fixed quantity feeder by means of conveyance such as a truck or a belt conveyor, and supply it to the drying / combustion process from this constant quantity feeder.

  In the operation of supplying the raw material 10 after dehydration to the first combustion furnace 14, the average particle diameter is reduced to 40 mm or less, preferably 3 to 30 mm, more preferably 5 to 20 mm by a pulverizer (or pulverizer). To be adjusted. Furthermore, it is more preferable to grind so that the ratio of an average particle diameter of 50 mm or less may be 70% by weight or more. In order to achieve a combustion treatment that does not cause a heat change of the calcium carbonate contained in the deinking floss, it is preferable that the average particle diameter of the raw material is uniform. However, if the average particle diameter is less than 3 mm, overcombustion tends to occur. This is because if it exceeds 40 mm, there is a problem that it is difficult to uniformly burn the raw material core.

  The ratio between the average particle size and the particle size was measured using a sample solution sufficiently dispersed by a stirring type disperser. The particle diameter in each combustion process was measured with a metal plate sieve based on JIS Z8801-2: 2000.

[First combustion process] (Drying and combustion process)
The raw material 10 is cut out from the storage tank 12 and supplied to the first combustion furnace. The first combustion furnace has an internal heat kiln furnace system in which a main body is placed horizontally and rotates around a central axis, and is charged from one side of the internal heat kiln furnace 14 by a charging machine 15. The internal heat kiln furnace heating means feeds hot air generated in the hot air generation furnace from the discharge port side of the internal heat kiln furnace 14 so as to counter-flow with the flow of the dehydrated product. An exhaust gas chamber 16 is provided on one side of the internal heat kiln furnace 14, and an exhaust chamber 18 is provided on the other side. Hot air is blown from the other side of the internal heat kiln furnace 14 through the discharge chamber 18, charged from the one side, and sequentially transferred to the other side as the internal heat kiln furnace 14 rotates. It is designed to dry and burn.

  That is, in this drying / combustion process, the dehydrated product is dried and burned gently from the supply port to the discharge port by drying and burning in an internal heat kiln furnace in which the main body is placed horizontally and rotates around the central axis. Combustion of organic components can be performed, pulverization of combustibles can be suppressed, and the degree of combustion of dehydrated products having various properties such as formation of aggregates, hard and soft, and particle alignment can be stably performed. In addition, the drying can be divided into separate steps and a blow-up type dryer can be inserted.

  Here, the hot air blown into the internal heat kiln furnace 14 has an oxygen concentration of 0.2 to 20%, preferably 1 to 17%, more preferably 7 to 15%.

  Since the oxygen concentration is consumed by the combustion (oxidation) of the raw material, the oxygen concentration varies depending on the state of combustion. If the oxygen concentration is excessively low, it is difficult to achieve sufficient combustion. Oxygen in the combustion furnace is consumed due to the combustion of raw materials and the like, and the oxygen concentration decreases.However, the oxygen concentration is reduced by blowing or exhausting oxygen-containing gas such as air by a hot air generator for combustion. Further, the temperature in the combustion furnace can be finely adjusted by blowing or exhausting the oxygen-containing gas, and the raw material can be burned uniformly without unevenness.

  The furnace temperature of the first combustion furnace is 300 to 500 ° C, preferably 400 to 500 ° C, more preferably 400 to 450 ° C. In the first combustion furnace, it is preferable to combust at a combustion temperature range of 300 to 500 ° C. for the purpose of slowly burning an easily combustible organic substance and suppressing the formation of residual carbon that is difficult to burn. When the temperature is excessively low, the organic matter is not sufficiently combusted. When the temperature is excessively high, overcombustion occurs, and calcium oxide is easily generated due to decomposition of calcium carbonate. Furthermore, when the furnace temperature exceeds 500 ° C, the drying and combustion progress locally before the particle alignment of the combustibles with various properties such as hard and soft proceeds, so the unburned rate on the particle surface and inside It becomes difficult to make the difference between them small and uniform.

  Hot air is blown from a hot air generating furnace 20 provided with a burner 20A.

  From the exhaust gas chamber 16, exhaust gas subjected to drying and combustion is sent into the recombustion chamber 22. The fine powder is discharged from the lower part of the exhaust gas chamber 16 and is mixed with the raw material and reused.

  The exhaust gas is recombusted by the burner in the recombustion chamber 22, precooled by the precooler 24, passed through the heat exchanger 26, and discharged from the chimney 30 by the induction fan 28. Here, after raising the temperature of the outside air, the heat exchanger 26 is sent to the hot air generating furnace 20 and is used for hot air blown from the internal heat kiln furnace 14 to recover the heat of the exhaust gas from the exhaust gas chamber 16. It is like that.

  The first combustion furnace preferably burns with a residence time of 30 to 90 minutes under the above conditions in order to slowly burn the easily combusted organic matter contained in the deinking floss and suppress the formation of residual carbon. Is preferred. The range of 40 to 80 minutes is more preferable from the viewpoint of combustion of organic matter and production efficiency, and the range of 50 to 70 minutes is particularly preferable from the viewpoint of ensuring constant quality. If the combustion time is less than 30 minutes, sufficient combustion is not performed and the proportion of remaining carbon increases. When the combustion time exceeds 90 minutes, thermal decomposition of calcium carbonate occurs due to overcombustion of the raw material, and the obtained regenerated particles become extremely hard.

  In particular, it is dried and burned so that the unburned rate of the burned product supplied in the second combustion step of the next step is 2 to 20% by mass, preferably 5 to 17% by mass, more preferably 7 to 12% by mass. .

  By making the unburned rate 2 to 20% by mass, the combustion in the second combustion step can be efficiently performed in a short time, and the hardness is low and the whiteness is 75 to 75% by stable heating in the external heating furnace. 85% combustion can be obtained. By using regenerated particles having a whiteness of 75 to 85%, as described above, it becomes easier to set the product whiteness of the book paper to 60 to 75%. When the unburned material is less than 2% by mass, the energy cost in the first combustion furnace is high, and the hardness of the combustion product may be relatively high, and the white color at the outlet of the second combustion furnace. In some cases, the quality may deteriorate, such as a decrease in degree.

[Second combustion process]
Combustion products that have undergone drying and combustion treatment in the internal heat kiln furnace 14 are loaded into an external heat kiln furnace 32 that corresponds to a second combustion furnace having an external heat jacket 31 that rotates horizontally about the central axis through a transfer channel. Entered.

  In this combustion furnace, the combustion product is heated by external heat and controlled by the lifter provided on the inner wall of the kiln furnace to control the conveyance of the raw material in the combustion furnace and burn slowly. To burn.

  In the combustion in the second combustion furnace, the residual organic matter that could not be combusted in the first combustion furnace, such as residual carbon, is burned, so that the particle diameter is adjusted to be smaller than the particle diameter of the raw material supplied in the first combustion furnace. It is preferable to use a combustion product. The particle size of the burned product after the drying / combustion step is adjusted so that the average particle size is 10 mm or less, preferably 1 to 8 mm, more preferably 1 to 5 mm.

  If the average particle diameter at the entrance of the second combustion furnace is less than 1 mm, there is a risk of overcombustion, and if the average particle diameter exceeds 10 mm, the remaining carbon is difficult to burn and combustion may not proceed to the core. The problem is that the whiteness of the regenerated particles is reduced. In order to ensure stable production in the second combustion furnace, it is preferable to adjust the particle size so that the combustion product having an average particle size of 1 to 8 mm is 70% or more. Therefore, it is useful for practical application in terms of uniforming the quality of the regenerated particles obtained. Further, when the classification is performed after drying as in this embodiment, the combustion product of small-diameter particles can be surely removed, and the processing efficiency is improved.

  As an external heat source in the external heat kiln furnace 32, an electric heating type electric furnace in which temperature control in the external heat kiln furnace 32 is easy and temperature control in the longitudinal direction is easy is preferable. A kiln furnace 32 is desirable.

  By using electricity for the external heat, it becomes possible to finely adjust the temperature and control the internal temperature uniformly, control the degree of combustion of dehydrated products with various properties such as formation of aggregates, hard and soft, and granulation Alignment can be performed stably.

  Furthermore, the electric furnace can be provided with a temperature gradient arbitrarily by providing a plurality of electric heaters in the flow direction of the furnace, and can maintain the temperature of the combustion product for a certain period of time. Residual organic content in the combustion product that has passed through one combustion furnace, especially residual carbon, can be brought to zero as much as possible without causing decomposition of calcium carbonate in the second combustion furnace. Regenerated particles with whiteness can be obtained.

  In the external heat kiln furnace 32, the oxygen concentration is set to 5 to 20%, preferably 10 to 20%, more preferably 10 to 15%. The oxygen concentration can be controlled by controlling the amount of oxygen or air input to the second firing furnace by an appropriate means (illustration of a specific form is omitted). When the oxygen concentration in the external heat kiln furnace is less than 5%, there arises a problem that the remaining carbon that is difficult to burn does not burn. On the other hand, when the oxygen concentration exceeds 20%, the oxidation of calcium carbonate proceeds and tends to change to calcium oxide. For this reason, it becomes easy to elute in water, and there exists a possibility that scale dirt may generate | occur | produce in papermaking type | system | group.

  The combustion temperature of the second combustion furnace is 550 to 780 ° C, preferably 600 to 750 ° C. As described above, since the second combustion furnace needs to burn residual organic matter, particularly residual carbon, that could not be burned in the first combustion furnace 14, it can be burned at a higher temperature than the first combustion furnace 14. preferable. Therefore, if the combustion temperature of the second combustion furnace is less than 550 ° C., it is difficult to sufficiently burn the residual organic matter. On the other hand, if the combustion temperature exceeds 780 ° C., the oxidation of calcium carbonate in the combustion product Advances and the problem that the particles become hard arises.

  The residence time is 60 minutes to 240 minutes, preferably 90 minutes to 150 minutes, and more preferably 120 minutes to 150 minutes. That is, it is preferable that the residence time is 60 minutes or more from the viewpoint of stable production of combustion products, while the residence time is 240 minutes or less from the viewpoint of preventing overcombustion and ensuring production. In particular, the remaining carbon must be burnt slowly at a high temperature that does not cause the decomposition of calcium carbonate as much as possible. However, if the residence time is less than 60 minutes, the remaining carbon is burnt in a short time. On the other hand, when it exceeds 240 minutes, the problem that calcium carbonate decomposes occurs.

  The particle size of the combustion product discharged from the external heat kiln furnace 32 is adjusted to 10 mm or less, preferably the average particle size is 1 to 8 mm, more preferably 1 to 5 mm.

  The regenerated particles whose combustion has been completed are preferably aggregates (regenerated particle aggregates), and after being cooled by the cooler 34, those having a target particle size are combusted by a particle size sorter 36 such as a vibration sieve. It is temporarily stored in the silo 38 and sent to the application destination of the pigment and filler.

  In addition, although the case where the deinking froth was used as the raw material 10 was illustrated, it may be a combustion product obtained by appropriately mixing other papermaking sludge such as papermaking sludge in the papermaking process with the deinking floss as the main raw material.

[Crushing process]
In the method for producing regenerated particles based on the present embodiment, if necessary, a known dispersion / pulverization step is further provided, and a pigment for coating and a filler for internal addition are prepared by appropriately finely pulverizing to a necessary particle size. Can be used as

  In one example, the particles obtained after combustion are pulverized using 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. Regarding the optimum particle size for fillers, pigment applications, etc., the regenerated particles of this embodiment preferably have an average particle size of 2 to 5 μm.

  This is considered to be because the bulky effect is improved because the average particle size is larger than that of conventional calcium carbonate. Talc and clay have a larger average particle size than regenerated particles and can be expected to have a bulky effect. However, since they become acidic papermaking, they tend to yellow and are not practical.

  The particle size of the regenerated particles after the pulverization step was measured by a volume average particle size using a particle size distribution measuring device (laser type microtrack particle size analyzer: manufactured by Nikkiso Co., Ltd.).

[Attached process]
In this production facility, in order to obtain more stable quality, it is preferable to classify the particle size of the regenerated particles uniformly in each step, and feed back coarse and fine particles to the previous step. The quality can be further stabilized.

  In addition, it is preferable to granulate the deinked floss that has been subjected to dehydration in the previous stage of the drying process, and it is more preferable to classify the granulated product so that the particle diameter is uniform, The quality can be further stabilized by feeding back the fine granulated particles to the previous process. In granulation, a known granulation facility can be used, and facilities such as a rotary type, a stirring type and an extrusion type are suitable.

  As the raw material 10 of this manufacturing method, it is preferable to remove in advance other than the raw material of the regenerated particles. That is, for example, it is preferable in terms of removal efficiency to remove sand, plastic foreign matters, metals, and the like with a pulper, screen, cleaner, etc., before the deinking process of the used paper pulp manufacturing process. In particular, the iron content is a causative substance that lowers the whiteness of the fine particles due to oxidation of the iron content. Therefore, it is recommended to selectively remove iron to avoid iron contamination. For this reason, each process is designed or lined with a material other than iron to prevent iron from being mixed into the system due to wear, etc., and a high magnetic material such as a magnet is installed in the drying / classifying equipment. It is preferable to remove iron.

  Furthermore, the regenerated particles produced by the method for producing regenerated particles according to the present embodiment have a ratio of calcium, silica and aluminum of 30 to 82: 9 to 35: 9 in terms of oxides in the elemental analysis of fine particles using an X-ray microanalyzer. To 35, preferably 40 to 82: 9 to 30: 9 to 30, more preferably 60 to 82: 9 to 20: 9 to 20.

  By including calcium, silica, and aluminum in a mass ratio of 30 to 82: 9 to 35: 9 to 35 in terms of oxides, the specific gravity is light and excessive aqueous solution absorption can be suppressed. The ratio of unburned matter in the drying / combustion process and the possibility of excessive curing due to sintering in the combustion process can be reduced.

  As a method for adjusting the ratio of the present embodiment, the main point is to adjust the raw material composition in the deinking floss, but in the drying / combustion process and the combustion process, the coating floss and preparation process with a clear origin It is also possible to adjust by means of containing floss in the process by spraying or the like, or means of containing incinerator scrubber lime.

  For example, using deinked floss as the main raw material, neutral papermaking wastewater sludge and coated paper manufacturing wastewater sludge are used to adjust calcium in the recycled particles, and white carbon is used as an opacity improver to adjust silica. Wastewater sludge from the newsprint manufacturing system to which a large amount of is added, and the drainage sludge from the papermaking system that uses sulfuric acid bands such as acidic papermaking system to adjust the aluminum, and the wastewater from the high quality papermaking process that often uses clay Sludge can be used.

In addition, the regenerated particles obtained by the production method as described above have a weight loss (rate) in decomposition (change to calcium oxide) of calcium carbonate that occurs in the vicinity of 700 ° C. in differential thermal analysis using a differential thermothermal gravimetric simultaneous measurement apparatus. By controlling combustion of the deinking froth based on the present embodiment so as to be 50% or more, it is preferable because the progress of oxidation of the calcium component can be suppressed more accurately and the particles can be prevented from becoming hard. .
[About the lifter of the second combustion furnace (external heat kiln furnace)]
As described above together with the reason for adoption, the spiral lifter and / or the parallel lifter parallel to the axial center is formed on the inner wall of the second combustion furnace (external heat kiln furnace) 32 from one end side to the other end side. It is possible to achieve uniform combustion of the raw material 10 and uniform quality.

  For this second combustion furnace (external heat kiln furnace) 32, a known rotary combustion apparatus as shown in FIG. 2 (a) with its internal structure and FIG. Used.

  That is, the second combustion furnace (external heat kiln furnace) 32 is configured to be rotationally driven by a rotational drive means (not shown), and has a charging part 32a at one end and a discharge part ( A combustion burner 20A (not shown) for introducing combustion gas into the cylindrical main body 32b is disposed at the other end. The inner surface of the fireproof wall 32c on the side of the insertion portion 32a of the cylindrical main body 32b has a plurality of spirals (eight in the illustrated example) that are inclined at an inclination angle of 45 ° to 70 ° with respect to the axis of the cylindrical main body 32b. A cylindrical lifter 32d protrudes at equal intervals through a bracket 32e, and a parallel lifter 32f of an appropriate length parallel to the axial center of the cylindrical main body 32b is provided at the other end side in the circumferential direction. A plurality (eight in the illustrated example) are provided at intervals, and a plurality of rows (eight in the illustrated example) bracket 32g are provided in the axial direction.

  The fireproof wall 32c is preferably made of fireproof castable or fireproof brick, and the helical lifter 32d and the parallel lifter 32f are made of metal such as a stainless steel plate having heat resistance, for example. Therefore, durability and strength can be sufficiently secured without using an expensive heat-resistant material, and heat transfer efficiency is higher than that of a refractory lifter, so that the heat efficiency can be further improved. In particular, it is desirable that the spiral lifter 32d and the parallel lifter 32f are arranged in this order from the combusted material input portion 32a side to the discharge side as described above.

  According to the second combustion furnace (external heat kiln furnace) 32 configured as described above, the content charged from the charging portion 32a is firstly fed in an appropriate amount toward the other end side by the spiral lifter 32d. While being lifted and dropped while being fed, the organic components resulting from the raw material 10 efficiently come into contact with the combustion gas (combustible gas) generated by gasification, and subsequently lifted and dropped by the parallel lifter 32f. By repeating the operation, the contents can be efficiently contacted with the combustion gas (combustible gas), so that the contents can be combusted efficiently. In particular, by controlling the amount of the content fed into the parallel lifter 32f by the spiral lifter 32d, the content can be properly lifted and dropped at the parallel lifter 32f, and the content can be burned uniformly and efficiently. Can be done automatically. Further, since there is no fear of damage to the refractory, there is no decrease in the purity of the fired product, and its production capacity can be improved. In the above-described embodiment, the spiral lifter 32d and the parallel lifter 32f are provided side by side, but only one of them may be provided as necessary.

  The regenerated particles obtained as described above have a high whiteness of 75 to 85%, preferably 80 to 85%, and little variation in whiteness. Further, when the regenerated particles obtained by the production method described above are used for the base paper of the present coated paperboard, the whiteness is lower than that in the case of using conventionally known regenerated particles and calcium carbonate which is a commercially available filler. The coated paperboard which is high and bulky and does not peel off during printing can be obtained.

  The regenerated particles obtained by the above-described production method have an average particle size larger than that of conventionally known calcium carbonate (1 to 2 μm), and the regenerated particles are fixed between the fibers, so that the bulk effect is improved. In addition, since the aluminum of the regenerated particles is cationic, the fixing property to the fiber is strong, and since the blending amount can be reduced more than calcium carbonate, the ash content can be lowered, the bulk effect and the surface strength are improved, As a result, it is considered that paper peeling during printing can be reduced.

  It is desirable that the book paper has a content of aluminum oxide of 10 to 35% by mass, preferably 15 to 25% by mass, of all inorganics including the inorganics brought in from the recycled particles. When the content of aluminum oxide is less than 10%, the effect of improving fixability is reduced. On the other hand, when the content of aluminum oxide exceeds 35%, the cationicity becomes too strong and reacts with the papermaking chemicals to generate aggregates or black foreign matters such as pitch.

In the present embodiment, the regenerated particles as described above can be used alone, or such regenerated particles and heavy calcium carbonate, light calcium carbonate, talc, clay, kaolin, ordinarily used as an internal filler. One or more fillers selected from inorganic fillers such as titanium dioxide, synthetic silica and aluminum hydroxide, and synthetic polymer fine particles such as polystyrene resin and urea formaldehyde resin can be used in combination.

  In order to confirm the effect of the book paper according to the present invention, the following various samples were prepared, and a test for evaluating the quality of each sample was performed. In addition, in a present Example, the numerical value which shows a mixing | blending, a density | concentration, etc. is a numerical value of the solid content or the mass reference | standard of an active ingredient. Moreover, since the pulp, chemical | medical agent, etc. which are shown in a present Example are only examples, it cannot be overemphasized that this invention is not restrict | limited by these Examples, and can be selected suitably.

15 types of book papers (referred to as “Example 1” to “Example 15 ”) according to the present invention and 12 types of book papers for comparison with Examples 1 to 15 (This is referred to as “Comparative Example 1” to “Comparative Example 12”.) Was prepared in the configuration shown in Table 1.

[Example 1]
Raw material pulp containing 30% by mass of mechanical pulp and 70% by mass of hardwood bleached kraft pulp (LBKP) as a filler, low-temperature regenerated particles are 12% of the book paper ash content with respect to the weight of the raw pulp 200 ppm of cationic polyacrylamide (manufactured by Eka Chemicals, model number: PL2615H) is added as a cationic coagulant, and colloidal silica (manufactured by Eka Chemicals, model number NP: 443) is added as an anionic flocculant. ) (In the table, "Colloidal silica A") is added at 100 ppm, and a sulfuric acid band is added at 1.0% by mass in solid content with respect to the raw material pulp to obtain a raw material pulp slurry. A base paper was obtained using a paper machine.
In addition, with a gate roll coater, oxidized starch was applied to both sides of the base paper at 0.5 g / m ² per side to obtain a book paper (Example 1) having a rice basis weight of 70 g / m ² . Various evaluations were performed as follows.

  In addition, Examples 2 to 15 and Comparative Examples 1 to 12 were prepared in the same manner as Example 1 except for the conditions shown in Table 1, and each sample as a book paper was produced. In addition, model number "Tama Pearl TP-121-6S" manufactured by Okutama Kogyo Co., Ltd. was used as the low temperature regenerated particles used in Comparative Examples in Table 1. Moreover, as the calcium carbonate described in the column of regenerated particles in Comparative Example 3, the trade name “TP-123CS” manufactured by Okutama Kogyo Co., Ltd. was used, and the high temperature regenerated particles of Comparative Example 5 were used as the firing temperature in the first firing furnace. The product name “Nanoace D1000” manufactured by Nippon Talc Co., Ltd. having an average particle size of 1.0 μm was used as the talc. In addition, as a cationic ammonium acrylate salt of the cationic coagulant in Table 1, a model number “Himolock NR-783” manufactured by Hymo Co., Ltd. is used, and a model number “SC924” manufactured by Hymo Corporation is used as a polyethyleneimine. Model number “FA-230” manufactured by Hymo Co., Ltd. was used as the anionic acrylamide. Moreover, the colloidal silica BG of the column of an anionic flocculant used the prototype which adjusted the amount of anions, and used the model number "FA-230" by Hymo Corporation as anionic acrylamide.

  The “anion amount (meq / g)” in Table 1 is the anion amount of the anionic flocculant and is a value measured using a cation demand measuring device (model number PCD03) manufactured by mutek.

  Table 1 shows the results of quality evaluation for all of these Examples and Comparative Examples. This quality evaluation test was performed under environmental conditions of temperature 23 ± 2 ° C. and humidity 50 ± 2% in accordance with JIS-P8111.

  In Table 1, “product whiteness (%)” is the whiteness of the book paper as each sample, and is a value measured according to JIS-P8148 (2001).

  The “ash content (%)” is the ash content of the base paper of the book paper that is each sample, and is a value measured according to JIS-P8251 (2003).

In addition, “density (g / cm ³ )” refers to the basis weight of the base paper of each sample and “paper and board-test method for thickness and density” described in JIS-P8118 (1998). It is a value calculated from the measured thickness of the base paper.

In addition, the “black defect” is prepared by cutting 4 pieces of each sample into a size of 50 cm × 50 cm, and referring to the contaminant measurement chart of JIS-P8208 (1998), the thickness is 1.0 mm ² or more. This is an evaluation of the number of black defects. The evaluation criteria were as follows.
A: There are 3 or less black spot defects per sample.
(Triangle | delta): There are 4-9 black spot defects per sample.
X: There are 10 or more black spot defects per sample.

Furthermore, “back-through” means that the obtained sample is cut into a flat size, and is printed at 10,000 at a printing speed of 7,000 sheets / min. The sheet was printed, and the degree of the back-through was evaluated by looking at the black solid print portion from the back side. The evaluation criteria were as follows.
○: There is almost no show-through.
Δ: There is some back-throw, but there is no practical problem.
X: The showthrough is conspicuous and cannot be used.

  From Table 1, when it is the book paper which concerns on this invention, ie, the book paper which concerns on Example 1- Example 15, it is excellent in any evaluation of product whiteness, a black defect, and a back-through, and does not use a bulking agent. The book paper which is the object of the present invention, is bulky, has no black defect, and has high whiteness can be obtained.

10 Material 12 Reservoir 14 First Combustion Furnace (Internal Heat Kiln Furnace)
15 Charging machine 16 Exhaust gas chamber 18 Exhaust chamber 20 Hot air generating furnace 22 Recombustion chamber 24 Precooler 26 Heat exchanger 31 External heat jacket 32 Second combustion furnace (external heat kiln furnace)
32b Tubular body 32c Fire wall 32d Spiral lifter 32f Parallel lifter 34 Cooler 36 Particle size sorter 38 Combustion furnace silo

Claims (4)

The mechanical pulp blending ratio measured in accordance with JIS P8120 (1998) is 30 to 80% by mass, and has a base paper with a filler internally added,
As the filler, containing regenerated particles, a cationic coagulant, and an anionic flocculant,
The regenerated particles are mainly made of deinked floss separated from pulp fibers in a deinking process of a used paper processing facility for producing used paper pulp, and include a dehydration process, a drying process, at least a first combustion process, and a second combustion process. After the main raw material is dehydrated to a moisture content of 40 to 90% in the dehydration process and dried and burned at 300 to 500 ° C. in the first combustion furnace of the first combustion process. The second combustion furnace of the second combustion step is obtained through a combustion step of recombusting the main raw material burned in the first combustion step and a pulverization step. Book paper. The regenerated particles have a whiteness of 75 to 85%,
The base paper has an ash content measured in accordance with JIS P8251 (2003) of 5 to 20% by mass,
The book paper according to claim 1, wherein the book paper has a density of 0.4 to 0.6 g / cm ³ and a whiteness of 60 to 75% in accordance with JIS P8148 (2001). The book paper according to claim 1 or 2, wherein the anionic flocculant has an anion amount of 0.5 to 6.0 meq / g. A book paper manufacturing method comprising a base paper in which a filler is internally added to a raw pulp in which mechanical pulp is blended so that the blending ratio of mechanical pulp measured in accordance with JIS P8120 (1998) is 30 to 80% by mass. In addition, regenerated particles as the filler, a cationic coagulant, and an anionic flocculant are added,
A method for producing a book paper, wherein the regenerated particles are produced by a production process comprising the following (a) to (d).
(I) a dehydration step in which the deinking floss separated from the pulp fiber in the deinking step of the used paper processing facility for producing the used paper pulp is used as a main raw material, and the main raw material is dehydrated to a moisture content of 40 to 90%;
(B) Drying and first combustion stroke in which the main raw material is dried and burned at 300 to 500 ° C. in a first combustion furnace;
(C) a second combustion step in which the main raw material burned in the first combustion step is burned again in a second combustion furnace;
(D) After the second combustion step, regenerated particles are obtained by pulverization in a pulverization step.

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