JP2008190080A - Lining paper for wallpaper - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide lining paper for wall paper, which is capable of being processed by preferably foaming a resin such as a vinyl chloride resin, having a high dimensional stability and concealing property, and also having a good removability of the wall paper in remodel. <P>SOLUTION: This lining paper for the wallpaper is obtained by using a Yankee paper machine equipped with a Yankee dryer, and contains 1-65 mass% mechanical pulp in pulp, regenerated particle aggregates as a filler, and 1-18 mass% ash measured in accordance with the JIS-P 8252. The filler consists mainly of clay and the regenerated particle aggregates at a blending ratio of the clay to the regenerated particle aggregates of (2/8) to (8/2). <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

  The present invention relates to a base paper (backing paper) such as vinyl wallpaper or paper wallpaper, and more particularly to a backing paper for wallpaper which is excellent in adhesion processability and workability with synthetic resins such as vinyl chloride resin and olefin resin.

  The wallpaper is made of a wallpaper backing paper and a synthetic resin such as vinyl chloride resin or olefin resin coated, dried and bonded to the wallpaper backing paper. For wallpaper backing paper used for wallpaper, in addition to dimensional stability and concealment, the synthetic resin applied to the wallpaper backing paper will foam well, and the wallpaper backing paper will re-peel well during renovation Etc. are required.

  The wallpaper is bonded to the wall with an aqueous paste such as starch or vinyl acetate. At that time, when the dimensional stability of the wallpaper backing paper is poor, the wallpaper backing paper contracts and an opening occurs at the joint portion of the wallpaper.

  Regarding the dimensional stability of backing paper for wallpaper, for example, as a method for preventing opening during wallpaper construction, JP 2005-82894 A uses a drying method with a Yankee dryer in the paper making process, A method is proposed in which is set to 10 to 2000 seconds. JP-A-2005-154968 discloses that pulp components are mixed with synthetic resin fibers such as vinyl chloride copolymer, vinyl acetate copolymer, acrylic, olefin, and polyester as synthetic resin components. A method of improving curling and underwater elongation due to the influence of glue or the like has been proposed from paper made of paper only.

  However, dimensional stability is certainly improved by controlling the sizing to a specific range or mixing synthetic resin fibers at the paper making stage, but in particular the latter requires expensive synthetic resin fibers to be mixed at the paper making stage. The cost of backing paper for wallpaper is high.

  In addition, these methods can solve the concealment problem, the foaming problem of the synthetic resin applied to the wallpaper backing paper, and the re-peelability problem during renovation, which are required for wallpaper backing paper. is not.

  In addition, the surface of the wallpaper is covered with a surface layer material such as vinyl chloride resin or olefin resin. However, due to environmental problems such as disposal of the removed wallpaper and resource saving, which occurs when the wallpaper is replaced by remodeling. In recent years, the thickness of the surface material, which is a synthetic resin, has been reduced, and in order to prevent the wall material from being transferred to the wallpaper surface, it is desired to improve the concealability of the backing paper.

  As a method for enhancing the concealing property, there is a method by blending a filler. In Japanese Patent No. 3715739, calcined clay having an average particle size of 3 μm or less or kaolin having an average particle size of 8 μm or less is used. JP-A-2004-353112 proposes a method of blending 5 to 50% by mass of kaolin having an average particle size of 3 μm or less as a filler type in paper.

  However, these are effective as a method for obtaining concealment, but are required for wallpaper backing paper, foaming problems of synthetic resin applied to wallpaper backing paper, problems of removability at the time of reforming Cannot be solved. Moreover, there is a problem that the strength of the backing paper for wallpaper is lowered, and problems such as tearing occur at the time of enforcement.

  Therefore, in addition to dimensional stability and concealability, there is a need to provide a wallpaper backing paper in which the synthetic resin applied to the wallpaper backing paper foams well and the wallpaper backing paper re-removes well during renovation. Is the actual situation.

JP 2005-82894 A JP 2005-154968 A Japanese Patent No. 3715739 JP 2004-353112 A

  Therefore, the main problem to be solved by the present invention is that the backing paper for wallpaper can be processed by foaming resin such as vinyl chloride resin, olefin resin, etc., and dimensional stability, concealment, work It is an object to provide a backing paper for wallpaper having a high property and having good removability of the wallpaper at the time of reforming.

  In order to solve the above problems, the present invention has the following configuration.

[Invention of Claim 1]
Using a Yankee paper machine equipped with a Yankee dryer, wallpaper backing paper with pulp and filler as main ingredients,
The pulp contains 1 to 65% by weight of mechanical pulp,
The filler contains recycled particle aggregates and is contained in the paper so that the ash content of the backing paper for wallpaper measured according to JIS-P 8252 is 1 to 18% by mass. Lined paper for wallpaper. The regenerated particle aggregate will be described later.

(Function and effect)
By including a filler so that mechanical pulp is 1 to 65% by mass in the total pulp and ash content is 1 to 18% by mass, voids are easily formed in the paper, and heat during coating of vinyl chloride resin, olefin resin, etc. Conduction and air flow can be generated to improve the foaming property of the resin, and troubles such as cracking of the resin layer during wallpaper construction due to poor foaming of the resin can be prevented.

  Unlike other kraft and synthetic pulps, mechanical pulp, in particular, is obtained by physical grinding from wood, so there is little fiber crushing, the fiber surface is finely fibrillated by grinding, and vinyl chloride. Resin, olefin resin, etc. are easy to blend in, the backing paper and the resin layer do not inadvertently peel off, and adequate voids are secured in the paper. Can be obtained, and the opening of the wallpaper joints is less likely to occur.

  Moreover, since the mechanical pulp and filler inhibit light transmission, the concealability of the wallpaper backing paper is improved, and the show-through of the wall material on the wallpaper surface can be prevented.

  By containing regenerated particle aggregates as the filler, the regenerated particle aggregates are produced by calcining and agglomerating deinked floss as the main raw material, thus having a porous and porous three-dimensional structure, and regenerated particles Because it shows cationicity due to the effect of aluminum in the constituent elements, unlike conventional fillers that exhibit anionic properties, it shows the effect of separating the raw fibers between the fibers of the raw pulp, and demonstrates the bulkiness of the paper be able to.

[Invention of Claim 2]
2. The backing paper for wallpaper according to claim 1, wherein the filler contains clay and regenerated particle aggregates as main components, and the blending ratio of clay and regenerated particle aggregates is 2/8 to 8/2. It is characterized by.

(Function and effect)
Furthermore, the filler used in the backing paper for wallpaper of the present invention contains clay and regenerated particle aggregates as main components, and the mixing ratio of clay and regenerated particle aggregates is from 2/8 to 8/2. .

  Clay has been widely used as a filler for paper, and is inexpensive and has a plate-like crystal structure. Therefore, it can contribute to improvement of the flatness and gloss of the paper surface. By using together with the agglomerates, it is possible to improve the surface flatness and gloss of the wallpaper backing paper while obtaining bulk.

[Invention of Claim 3]
The base paper is flattened by pressing the metal surface of the Yankee dryer with a roll without using a felt, and the glossy surface JIS-P 8119 that touches the metal surface of the Yankee dryer for wallpaper backing paper. The wallpaper backing paper according to claim 1 or 2, wherein the smoothness of the non-glossy surface that does not contact the metal surface of the Yankee dryer is 5 seconds or more according to the above. .

(Function and effect)
The backing paper for wallpaper of the present invention is different from a conventional drying method in which a Yankee dryer passes through a canvas and the wet paper comes into contact with the Yankee dryer. It is possible to reduce the difference in smoothness between the paper surface (glossy surface) in contact with the Yankee dryer and the paper surface (non-glossy surface) in contact with the roll, and the texture of the canvas (so-called Since there is no transfer of the canvas mark) to the non-glossy surface, it is a non-glossy surface, but the paper surface is flat. In construction, it becomes possible to peel off the wallpaper without detaching the wall paper and the wall base material (for example, gypsum board surface paper) without damaging it. Can.

[Invention of Claim 4]
The raw material contains a wet paper strength enhancer and a dry paper strength enhancer, and has a wet tensile strength (longitudinal) of 0.3 kN / m or more and 1.0 kN according to JIS-P 8135 for backing paper for wallpaper. The backing paper for wallpaper according to any one of claims 1 to 3, wherein the backing paper is / m or less.

(Function and effect)
More preferably, the backing paper for wallpaper of the present invention contains a wet paper strength enhancer and a dry paper strength enhancer in the paper. By using wet paper strength enhancer and dry paper strength enhancer, suitable paper quality strength is maintained when applying vinyl chloride resin, olefin resin, etc. (when dry) or when applying wallpaper (when wet). At the same time, dimensional stability can be achieved by bonding with a wet paper strength enhancer and a dry paper strength enhancer between the fibers.

  For conventional wallpaper, the glue is applied to the backing paper, and then the wallpaper is applied to the wall to start construction. The wallpaper using the wallpaper backing paper according to the present invention can maintain the paper quality of the wallpaper even before applying the glue, after applying the glue (after the wallpaper is wetted by the glue), when the wallpaper is applied to the wall, A wallpaper having excellent workability can be obtained.

  Next, an embodiment of the present invention will be described.

  The wallpaper backing paper of the present invention can be produced with a paper machine comprising a normal long mesh, circular mesh, short mesh, slanted wire part, etc., with a slurry containing pulp and filler as main raw materials and the necessary chemicals. The machine is not particularly limited. In addition, the drying process uses a Yankee dryer, so that the drying process can be performed without applying much tension to the wet paper as compared with the drying method using a multi-cylinder dryer, so that it is possible to obtain a backing paper for wallpaper having excellent dimensional stability. This is preferable. The drying method using a Yankee dryer is different from the drying method using a general multi-cylinder dryer, and wet paper is attached to the cylinder surface for drying. This reduces paper shrinkage during drying and is used as wallpaper backing paper. When the water-based paste is applied to the wall, the paper is less stretched, has excellent dimensional stability, and can be particularly suitable for wallpaper backing paper. In addition, an ordinary multi-cylinder dryer or the like can be used in combination.

  As the mechanical pulp used in the present invention, GP (Grandwood pulp), PGW (Pressurized Grandwood pulp), TMP (Thermomechanical pulp) and the like can be used, and the mechanical pulp is not bleached depending on the application. Bleached pulp may be used, and for example, BCTMP or the like that has been subjected to a bleaching treatment can also be suitably used.

  As other pulps, kraft pulp, semi-chemical pulp and the like can be used.

  As raw materials for obtaining pulp, in addition to wood raw materials such as conifers and broad-leaved trees, non-wood raw materials such as hulls, hemp and kenaf can be used.

  Further, recycled pulp derived from waste paper containing or not containing mechanical pulp can also be used.

  Moreover, the number average fiber length of the disaggregated pulp of the wallpaper backing paper disaggregated according to JIS-P8220 is set to 0.8 to 2.0 mm, the initial dehydration in the paper machine wire part is increased, and the conifer pulp is increased. By such a method, strain between fibers can be reduced and high dimensional stability can be obtained.

  The blending ratio of mechanical pulp is 1 to 65% by mass in the total pulp for obtaining desired concealability. Furthermore, it is preferable to make it contain 20-50 mass% from the point etc. which prevent the generation | occurrence | production of the blister of the coated resin at the time of removability of the backing paper for wallpaper at the time of renovation, and make it contain 30-50 mass% More preferred.

  If the mechanical pulp is less than 1% by mass, the opacity of the backing paper for wallpaper will decrease, and the problem of reflection of the wall material on the wallpaper surface and the interlayer strength (internal bond) of the backing paper for wallpaper will increase. Sometimes a problem occurs that the resin layer or the gypsum board surface paper is damaged.

  In general paper such as printing paper and paperboard, it is required that the interlayer strength is high. However, in the backing paper for wallpaper in the present invention, if the interlayer strength is high, it is peeled off at the time of reform after being bonded to the wall. The work efficiency is reduced. That is, in the application of the present invention product, it is necessary to adjust the interlayer strength within a certain range so that the wallpaper can be easily peeled off when the wallpaper is peeled off at the time of remodeling. When the backing paper has a high interlayer strength, not only does it require a strong force to peel off the wallpaper during renovation, but part of the backing paper remains on the wallpaper side, part of the backing paper remains on the wall side, and on the wall surface. Since unevenness is generated or only the resin layer is peeled off, the wallpaper to be bonded next cannot be applied neatly.

  On the other hand, if the content of mechanical pulp exceeds 65% by mass, the interlaminar strength becomes too low, and unintentional peeling may occur. Moreover, in order to adjust the interlaminar strength, a strength auxiliary agent such as excessive addition of a paper strength enhancer is required, which not only increases the cost, but also increases the cost by the resin component (lignin) in the system. Dirt is likely to occur, resulting in a decrease in operability.

  In addition, the tensile strength may be reduced and a problem may occur. That is, when a wallpaper is pasted on a colonnade of a building, the wallpaper having a length of 4 to 5 m is used, but the wallpaper may be broken by a slight external force and the weight of the wallpaper.

  The backing paper for wallpaper of the present invention contains 1 to 65% by mass of mechanical pulp to obtain a desired concealing property, and further has an interlaminar strength (internal bond) of 70 to 120 mJ which is excellent in wallpaper peelability at the time of reforming. It is easy to adjust to the range, more preferably, the interlayer strength is more preferably 90 to 110 mJ from the viewpoint of workability.

A suitable basis weight of the backing paper for wallpaper obtained in the present invention is 40 to 150 g / m ² . If the basis weight is less than 40 g / m ² , it is difficult to obtain the rigidity, strength, and concealment required for wallpaper, while if the basis weight exceeds 150 g / m ² , the rigidity, strength, and concealment are excellent. On the other hand, the weight of the wallpaper increases, and the worker who pastes the wallpaper on the wall or ceiling is burdensome. Moreover, since rigidity becomes high too much, the bonding suitability at the time of sticking a wallpaper to the corner part etc. of a room falls.

  In the present invention, recycled particle aggregates are used as a filler for wallpaper backing paper. A method for producing regenerated aggregates from raw materials for obtaining regenerated particle aggregates used in the present invention will be described in detail below.

〔material〕
In the used paper pulp manufacturing process, for the purpose of continuously producing used paper pulp with stable quality, used paper is selected and selected and used with a certain quality.

  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 unburned substances in the recycled particle agglomerate production method, are contained in the waste paper, these foreign substances are used in the deinking process to obtain deinking floss. It can be removed at the previous stage. Accordingly, the deinking floss is a raw material for producing regenerated particle aggregates having extremely stable quality as compared with papermaking sludge generated in other processes such as a factory drainage process and a papermaking raw material adjustment process.

  The deinking floss referred to in the present invention refers to what is separated from the pulp fiber in the deinking process for removing the 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 in the present embodiment, the deinking floss is dehydrated by separating water from the deinking floss by a screen serving as a dewatering unit. 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 50% or less.

  If the moisture content exceeds 50%, the temperature of the drying / combustion process in the first combustion furnace is lowered, energy loss due to heating increases, and uneven combustion of the raw material is likely to occur, thereby promoting uniform combustion. I want to. 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. In addition, although lowering the moisture content of the raw material facilitates uniform combustion, dehydrating the moisture content of the raw material to less than 25% increases the size of the dehydration equipment and significantly increases the energy of dehydration treatment. Have the problem.

  As described above, if the deinking floss is dehydrated in a multi-stage process and abrupt dehydration is avoided, the outflow of the inorganic substance can be suppressed and there is no possibility that the deinking floss floc 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 particle aggregate due to oxidation of iron.

  The deinking process of deinking floss is preferably adjacent to the manufacturing process of the regenerated particle aggregate used in the present invention in terms of production efficiency, but the equipment was previously provided adjacent to the waste paper pulp manufacturing process and dewatered. It is also possible to convey the object, and it is conveyed to a fixed quantity feeder by a conveying means such as a truck or a belt conveyor, and supplied to the drying / combustion process from this fixed quantity feeder.

  In the operation of supplying the raw material after dehydration to the first combustion furnace, it is desirable that the raw material is desirably aligned with a particle size of 40 mm or less by a pulverizer (or a pulverizer), and more preferably the average particle size is 3 It is preferable to adjust so that the average particle size is in the range of ˜30 mm, more preferably in the range of 5 to 25 mm, and preferably the pulverization is performed so that the proportion of the particle size of 50 mm or less is 70% by weight or more. Is more preferable. 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 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 an average particle size exceeding 50 has a problem that it is difficult to uniformly burn the raw material core.

  The ratio between the average particle size and the particle size in the present invention was measured using a sample solution sufficiently dispersed by a stirring type disperser.

  The particle diameter in each combustion stroke was measured with a metal plate sieve based on JIS Z8801-2: 2000.

[First combustion process] (Drying and combustion process)
Such raw material is cut out from the storage tank and supplied to the first combustion furnace. The first combustion furnace is preferably an internal heat kiln furnace system in which the main body is placed horizontally and rotates around the central axis, and is charged from one side of the internal heat kiln furnace by a charging machine. 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 so as to counter-flow with the flow of the dehydrated product. An exhaust gas chamber is provided on one side of the internal heat kiln furnace, and an exhaust chamber is provided on the other side. Drying and burning of the raw material that passes through the discharge chamber, hot air is blown from the other side of the internal heat kiln furnace, charged from the one side, and sequentially transferred to the other side as the internal heat kiln furnace rotates. Is supposed to do.

  That is, in this drying / combustion process, the dehydrated product is dried and burned by a tangible means such as an internal heat kiln furnace in which the main body is placed horizontally and rotates around the central axis, thereby reaching the discharge port from the supply port. Until then, drying and combustion of organic components can be performed gently, pulverization of the combusted matter can be suppressed, and the degree of combustion and particle size of the dehydrated product having various properties such as hard and soft can be controlled stably. Further, 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 preferably has an oxygen concentration of 0.2 to 20%, more preferably 1 to 15%, and most preferably 5 to 12%.

  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 less than 0.2%, 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.

  As temperature of a 1st combustion furnace, 500 to 650 degreeC, More preferably, 510 to 620 degreeC, Especially preferably, 530 to 600 degreeC is desirable. In the first combustion furnace, it is preferable that the easily combustible organic matter is gradually burned and burned in a temperature range of 500 ° C. to 650 ° C., and below 500 ° C., the combustion of the organic matter is insufficient. When it exceeds ° C., overcombustion occurs, and calcium oxide is easily generated due to decomposition of calcium carbonate. Further, when the temperature of the hot air exceeds 650 ° C., the drying and combustion progress locally faster than the particle alignment of the burned material having various properties such as hard and soft, so that the unburned particles on the particle surface and inside are not burned. It becomes difficult to make the difference in rate small and uniform.

  Hot air is blown from a hot air generator equipped with a burner.

  From the exhaust gas chamber, exhaust gas used for drying and combustion is fed into the recombustion chamber. The fine powder is discharged from the lower part of the exhaust gas chamber, and is mixed again with the raw material and reused.

  The exhaust gas is recombusted by a burner in a recombustion chamber, precooled by a precooler, passed through a heat exchanger, and discharged from a chimney by an induction fan. Here, the heat exchanger raises the outside air, and then is sent to the hot air generating furnace and used for hot air blown from the internal heat kiln furnace so as to recover the heat of the exhaust gas from the exhaust gas chamber 16. is there.

  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 substances contained in the deinking floss and suppress the formation of residual carbon. Is preferred. More preferably, 40 minutes to 80 minutes is preferable in terms of combustion of organic matter and production efficiency. Most preferably, a range of 50 minutes to 70 minutes is preferred in order to ensure 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 burning time exceeds 90 minutes, thermal decomposition of calcium carbonate occurs due to overburning of the raw material, and the resulting regenerated particle aggregate becomes extremely hard.

  In particular, it is preferable to dry and burn the unburned rate of the combustion product supplied in the second combustion step of the next step to 2 to 20% by mass, more preferably the unburned rate is set to 2 to 15% by mass. Preferably, the unburned rate is 2 to 10% by mass.

  By setting the unburned rate to 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 80 by stable heating in the external heating furnace. %, At least 70% or more of high whiteness combustion products can be obtained. If 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 material may be relatively high. There is a case where quality deterioration such as deterioration occurs.

[Second combustion process]
Combustion material that has undergone drying and combustion treatment in the internal heat kiln furnace is charged into an external heat kiln furnace corresponding to a second combustion furnace having an external heat jacket in which the main body is placed horizontally and rotates around the central axis through a transfer channel. .

  In this combustion furnace, the combustibles are heated with external heat and gently agitated by friction caused by rotation of the inner wall of the kiln furnace, thereby suppressing particle refinement and more uniformly suppressing the generation of hard substances. While burning the unburned matter.

  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. It is preferable to adjust the particle size of the burned product after the drying / combustion step so that the average particle size is 2 to 30 mm, and more preferably, the adjustment is performed so that the average particle size is 2 to 18 mm. It is particularly preferable to perform combustion aggregation so that the average particle diameter is 3 to 15 mm.

  If the average particle diameter at the entrance of the second combustion furnace is less than 2 mm, there is a risk of overcombustion, and if the average particle diameter exceeds 30 mm, it is difficult to burn the remaining carbon and combustion does not proceed to the core. This causes a problem that the whiteness of the regenerated particle aggregate 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 a particle size of 1 to 30 mm is 70% or more. Therefore, it is beneficial to the possibility of practical use in terms of making the quality of the regenerated particle aggregate obtained uniform. Furthermore, 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, an electric heating type electric kiln furnace in which temperature control in the external heat kiln furnace is easy and temperature control in the longitudinal direction is easy is suitable. Generation of hard substances due to combustion and melting of regenerated particle constituent substances can be suppressed.
Therefore, an external heat kiln furnace with an electric heater is most desirable.

  By using electricity for external heat, the temperature can be finely adjusted and the internal temperature can be controlled uniformly, and the control of the degree of burning of dehydrated products with various properties, such as hard and soft, and stable particle alignment are possible. It can be carried out.

  Furthermore, in the electric kiln furnace, by providing a plurality of electric heaters in the flow direction of the furnace, it is possible to arbitrarily provide a temperature gradient, and it is possible to maintain the temperature of the combustion product for a certain period of time, Residual organic content in the combustion product that has passed through the first combustion furnace, especially residual carbon, can be brought to zero as much as possible without causing uncombusted carbon dioxide decomposition in the second combustion furnace. High whiteness regenerated particle aggregates can be obtained.

  In an external heat kiln furnace, it is desirable that the oxygen concentration be 5 to 21%, more preferably 10 to 21%, and most preferably 15 to 21%.

  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.

  As temperature, 550 degreeC-750 degreeC, More preferably, 600 degreeC-725 degreeC, Especially preferably, 650-710 degreeC is desirable.

  As described above, the second combustion furnace is preferably burnt at a higher temperature than the first combustion furnace because it is necessary to burn residual organic matter, particularly residual carbon, that could not be burned in the first combustion furnace. When the combustion temperature is less than 550 ° C., it is difficult to sufficiently burn the residual organic matter, and when the combustion temperature exceeds 750 ° C., the oxidation of calcium carbonate in the combustion product proceeds and the particles become hard. Arise.

  The residence time is 10 to 60 minutes, more preferably 15 to 45 minutes, and particularly preferably 20 to 40 minutes. In particular, the remaining carbon must be burnt slowly at a high temperature that does not cause decomposition of calcium carbonate as much as possible. If the residence time is less than 10 minutes, the remaining carbon is burned in a short time and 60 minutes. If it exceeds 1, the problem of decomposition of calcium carbonate occurs.

  Furthermore, it is preferable that combustion be performed in a residence time of 10 minutes or more in order to prevent overcombustion and secure productivity in order to ensure stable production of combusted materials.

  The particle size of the combustion product discharged from the external heat kiln furnace 32 is preferably adjusted to 20 mm or less, more preferably the average particle size is 5 to 18 mm or less, and most preferably the average particle size is 8 to 15 mm. In addition, setting the ratio of the particle diameter of 20 mm or less to 65% or more is effective for impossibility of reducing the pulverization process as a post-worker.

  The regenerated particle agglomerates that have been combusted are cooled by a cooler and then temporarily stored in a combustion product silo by a particle size sorter such as a vibrating sieve to be used for pigments and fillers. Be directed.

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

[Crushing process]
The fired particles can be made into regenerated particle aggregates that can be used as a filler by finely pulverizing them to a necessary particle size in the pulverization step.

  For example, particles obtained by firing 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, and the desired regenerated particle aggregate It can be. When the regenerated particle aggregate is used as a filler for internal addition, it is preferable to adjust the average particle size by a Coulter counter method to 0.1 to 10 μm.

[Attached process]
In the case of seeking further stabilization of the quality of the regenerated particle aggregate, it is preferable to classify the particle size of the regenerated particle aggregate in each step, and coarse particles and fine particles are fed back to the previous step. It is desirable.

  In addition, it is preferable to granulate the deinked floss that has been subjected to dehydration in the previous stage of the drying process, more preferably to classify the granulated product uniformly, and coarse granulated particles. Further, the quality can be further stabilized by feeding back the fine granulated particles to the previous process. In addition, a well-known granulation equipment can be used for granulation, for example, rotation, a stirring type, an extrusion type, etc. are suitable.

  Further, it is preferable to remove foreign matters other than the regenerated particle aggregates. For example, in the manufacturing process of waste paper pulp, sand, plastic foreign matters, metals, etc. are removed with a pulper, screen, cleaner, etc. before the deinking step Is preferable in terms of removal efficiency. In particular, iron content may reduce the whiteness of the regenerated particle aggregate by oxidation, and therefore it is preferable to avoid iron content and selectively remove it. The equipment in each process is designed or lined with materials other than iron to prevent iron from being mixed into the system due to abrasion, etc., and high magnetic materials such as magnets are selectively installed in the drying / classifying equipment. It is preferable to remove iron.

In the drying step, the firing step, and, if necessary, the classification step, it is preferable that the particles having a particle size of 40 μm or less are preliminarily processed to 90% by mass or more before the pulverization step. 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, the pore volume of the regenerated particle aggregate is adjusted to 0.15 to 0.60 mL / g by adjusting calcium, silicon and aluminum in the deinking floss as the main raw material in advance, for example, to a mass ratio described later. The pore surface area may be 10 to 25 m ² / g, and the pore radius may be 30 to 100 nm.

  Thus, deinked floss discharged from the waste paper pulp manufacturing process is used as a main raw material, and the regenerated particle aggregate is obtained by subjecting the main raw material to a dehydration process, a drying process, a baking process, and a pulverization process. In the invention, as the regenerated particle aggregate, a silica-coated regenerated particle aggregate in which the surface of the particles obtained through the above-described steps is further coated with silica can be particularly preferably used.

  Silica is further precipitated on the surface of the regenerated particle aggregate to form a silica-coated regenerated particle agglomerate, which is used for paper making as a buffering agent or a bleaching aid by reacting with sodium hydroxide in the used paper processing step in circulation use. This can contribute to the recycling of raw materials and inorganic particles.

  In addition, the deinking floss discharged from the used paper processing step used in the present invention has a tendency to increase the content of calcium carbonate with the recent neutral paper making, and the amount of calcium in the regenerated particle aggregate obtained is increased. The ratio also tends to be high. Thus, when the regenerated particle aggregate having a high calcium ratio is internally added to the pulp, the opacity of the paper may be slightly lowered. However, the silica-coated regenerated particle aggregate having silica deposited on the surface is used for papermaking. The function as a regenerated particle aggregate is very high, and the opacity of the backing paper for wallpaper obtained by internally adding the silica-coated regenerated particle aggregate to pulp is 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 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, which impairs the porosity of the regenerated particle aggregate and improves opacity. In order to eliminate the possibility that the effect is insufficient, the silicic acid content (in terms of SiO ₂ ) is preferably 10% by mass or less.

  The regenerated particle aggregate thus obtained contains calcium, silicon and aluminum as particle constituents, and these calcium, silicon and aluminum form a composite in the particles. The mass ratio of these calcium, silicon and aluminum in the regenerated particle aggregate (calcium: silicon: aluminum) is determined by X-ray microanalyzer (model number: E-MAX S-2150, Hitachi, Ltd./Horiba, Ltd.). In the elemental analysis using the product, 30 to 82: 9 to 35: 9 to 35, preferably 40 to 82: 9 to 30: 9 to 30, particularly preferably 60 to 82: 9 to 30 in terms of oxide. 20: 9-20. In particular, when the regenerated particle aggregate is a silica-coated regenerated particle aggregate, the mass ratio of calcium, silicon, and aluminum (calcium: silicon: aluminum) is determined by elemental analysis using the X-ray microanalyzer. In terms of oxide, it is 30 to 62:29 to 55: 9 to 35, preferably 30 to 50:35 to 55:15 to 30. At the same time, the total content of calcium, silicon and aluminum in the particle constituents is 90% by mass or more, preferably 94% by mass or more in terms of oxides in the same elemental analysis as described above.

  Thus, since the regenerated particle aggregate contains calcium, silicon, and aluminum as the particle constituents in terms of oxides in the mass ratio, the specific gravity is light and excessive aqueous solution absorption is suppressed, Dehydration in the dehydration process is good and moisture adjustment in the drying process is easy, as well as reducing the proportion of unburned material in the firing process and reducing the risk of excessive hardness due to sintering. it can.

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

  For example, to adjust the calcium content in recycled particle aggregates, neutral papermaking wastewater sludge and wastewater sludge from the coated paper manufacturing process, to adjust the silicon content, increase opacity. To adjust the aluminum content of newsprint manufacturing wastewater sludge, which is added in large quantities as an additive, a large amount of papermaking wastewater sludge using acid band such as acid papermaking and clay is used. The drainage sludge from the fine paper making process can be used as appropriate.

  Moreover, in order to adjust the total content ratio of calcium, silicon and aluminum to 90% by mass or more in terms of oxide, for example, means for using a flocculant containing no iron in the agglomeration treatment of drainage sludge, Designing or lining the manufacturing equipment process with materials other than iron to prevent iron from entering the system due to wear, etc.Furthermore, high magnetic materials such as magnets are installed in the drying / classifying equipment to reduce the iron content. It is possible to adopt a means for removing. In particular, iron 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. Therefore, the calcium contributes to the quality stability of the regenerated particle aggregate itself, and the regenerated particle aggregate is an agglomerate composed of particles in which different components such as calcium, silicon and aluminum are combined, Shows stable properties.

  In addition, the regenerated particle aggregate contains silicon as a particle component, but the silica particles composed of the silicon are fine, so that the optical refractive index is high. By using such a regenerated particle aggregate containing 9 mass% or more of silicon in terms of oxide as a filler, the opacity of the resulting wallpaper backing paper is further improved.

  That is, the regenerated particle agglomerates thus obtained have one characteristic in that they are composed of agglomerates in which different components such as calcium, silicon and aluminum are agglomerated, because they have a small specific heat, and are excellent in opacity and water absorption. When it is contained in the backing paper for wallpaper, it is possible to obtain a backing paper for wallpaper that is particularly excellent in resin foaming, dimensional stability, and concealment, and excellent in workability at the time of wallpaper removal at the time of reforming.

  As other fillers that can be contained in the backing paper for wallpaper of the present invention, it is particularly preferable to use clay, from the viewpoint of obtaining good resin foaming properties, but appropriately known talc, calcium carbonate, titanium oxide, white carbon, etc. Inorganic particles can also be used.

  Further, the disintegrated pulp slurry of wallpaper backing paper disaggregated according to JIS-P 8220 is filtered through a 440 mesh (mesh 32 μm) circular standard sieve, and 90% or more of the filler contained in the filtrate is 0.1 μm. To 15 μm, a bulky low air permeability can be obtained from the base paper by a synergistic effect of mechanical pulp and bulky regenerated particle aggregates.

  In making paper backing paper, the filler added internally at the raw material adjustment stage is washed away with dehydration at the paper making stage and remains in the paper at a particle size different from the internal addition stage to the raw material. It is necessary to adjust the properties of the filler remaining in the filter, and in the study by the inventors, 90% or more of the filler contained in the filtrate contains 0.1 to 15 μm. With the particle size range of, the paper quality strength due to the fine filler is reduced too much, and the occurrence of coating defects due to the presence of excessive filler, such as vinyl chloride resin and olefin resin, is suppressed, and the backing for wallpaper It is possible to make foamability uniform when resin such as vinyl chloride resin and olefin resin is applied to paper, improve releasability during re-peeling, and improve dimensional stability.

  In the backing paper for wallpaper of the present invention, the filler is contained in an amount of 1 to 18% by mass as ash, and preferably, the paper is dried by using a Yankee dryer, so that the J · TAPPI-No27-28A method is used. It is preferable that the elongation in water in the transverse direction (paper machine width direction) of the specified paper is 0.8 to 1.5%, more preferably the elongation in water is 0.8 to 1.2%. Opening after bonding to the wall can be prevented and dimensional stability can be improved.

  In addition, when the underwater elongation in the lateral direction of the paper exceeds 1.5%, not only troubles such as opening of the paper will occur after the wallpaper construction, but also problems such as curling will occur at the time of construction, leading to a decrease in workability. This causes a problem. Also, in order to reduce the lateral water elongation of the paper to less than 0.8%, it is necessary to take excessive measures such as adding synthetic fibers and hardening the paper layer with resin, resulting in lower operability and higher costs. In addition, the quality is excessive as a general wallpaper backing paper, which is not economical.

  Furthermore, as a preferable configuration of the backing paper for wallpaper of the present invention, as a filler, a ratio of 2/8 to 8/2 is a blending ratio of clay and recycled particle aggregates as a main component and clay and recycled particle aggregates. The disaggregated pulp slurry of the backing paper for wallpaper, which has been disaggregated according to JIS-P 8220, is filtered through a 440 mesh (mesh 32 μm) circular standard sieve and the volume average particle diameter of the filler contained in the filtrate is It is preferable to be in the range of 0.1 μm to 15 μm.

  If the blending ratio of clay and regenerated particle aggregate is out of the range of 2/8 to 8/2, the effect of clay and regenerated particle agglomerates will be biased, the flatness of the paper surface will be reduced, and the density The problem that becomes high appears.

  As a filler for wallpaper, clay has a plate-like crystal structure, so it has the effect of improving the flatness and glossiness of the paper surface at a low cost. Recycled particle aggregates have been conventionally discarded and landfilled and effectively used as resources. Deinking floss that was not used is the main raw material, which is preferable in terms of environmental protection and resource saving, as well as porosity as agglomerates of regenerated particles, cushioning workability as wallpaper, glue and backing paper Or affinity with resin, such as a vinyl chloride resin and an olefin resin, improves, and the effect that peeling of an inadvertent resin layer and peeling from a paste surface hardly arises is expressed.

  As the regenerated particle aggregate, the particle constituents contain calcium, silicon, and aluminum in a mass ratio of 30 to 82: 9 to 35: 9 to 35 in terms of oxides, and particles of the regenerated particle aggregate Among the constituent components, a regenerated particle aggregate in which the total content ratio of the calcium, the silicon, and the aluminum is 90% by mass or more in the regenerated particle aggregate constituent component can be used.

  In a preferred configuration of the wallpaper backing paper of the present invention, it is recommended that the paper contains a wet paper strength enhancer and a dry paper strength enhancer.

  The backing paper for wallpaper of the present invention has a smoothness according to JIS-P 8119 of the surface of the Yankee dryer that contacts the metal surface (glossy surface) for at least 20 seconds, and does not contact the metal surface of the Yankee dryer (non-glossy). Surface) smoothness of 5 seconds or more, and preferably, the smoothness according to JIS-P 8119 of the glossy surface on the side in contact with the metal surface of the Yankee dryer is 30 to 42 seconds, and does not contact the metal surface of the Yankee dryer. The smoothness of the glossy surface is preferably 11 to 15 seconds or more.

  By using a roll, preferably a resin roll, the flatness of the paper surface can be ensured without applying excessive pressure to the paper, and the glossy surface on the side in contact with the metal surface of the Yankee dryer is smooth according to JIS-P 8119. When the degree is less than 20 seconds, the flatness of the coated surface is impaired during coating of vinyl chloride resin, olefin resin, etc., and the unsatisfactory after coating is reduced, and the workability during coating of resin, etc. is also lowered.

  In addition, if the smoothness of the non-glossy surface on the side pressed by a roll, particularly a resin roll, is less than 5 seconds, the amount of glue at the time of wallpaper application is likely to be uneven, and the surface of the wallpaper after inadvertent peeling or application Problems that cause undulations and irregularities appear.

  Resin rolls that can be suitably used to adjust the front and back surfaces of wallpaper backing paper to a desired smoothness are those having a rubber hardness of 90 to 95 degrees in “durometer hardness” in accordance with JIS K 6253. The Yankee dryer can be pressed on the surface without applying excessive linear pressure, and is suitable for ensuring flatness. When the rubber hardness is higher than 95 degrees or a metal roll, it is not preferable because pressure is applied by a line rather than a surface, and the density tends to be excessively high. Also, if the angle is less than 90 degrees, the contribution to the flatness of the non-glossy surface is low, and the pressure on the glossy surface is dispersed, resulting in low glossiness. Vinyl chloride resin, olefin resin There arises a problem that the covering property by the synthetic resin is inferior.

  In the backing paper for wallpaper of the present invention, the wet tensile strength (longitudinal) according to JIS-P 8135 is preferably 0.3 kN / m or more and 1.0 kN / m or less, more preferably 0.5 to The range is 0.9 kN / m. If the wet tensile strength (longitudinal) is less than 0.3 kN / m, it will be difficult to maintain a sufficient paper strength even after applying glue at the time of wallpaper construction. When the wallpaper is peeled off, there are problems such as damage to the adhesive material typified by gypsum board, cost increase due to the use of expensive chemicals, and dirt in the paper machine system.

  The wet paper strength enhancer that can be particularly preferably used is a dry paper strength using one or more resins selected from polyurethane resins, polyamide epoxy resins, melamine resins, urea resins, and silicon resins. As the enhancer, one or more selected from starch, vegetable gum, semi-synthetic polymer or synthetic polymer can be suitably used, and the mixing ratio of dry paper strength enhancer and wet paper strength enhancer Is preferably dry paper strength enhancer: wet paper strength enhancer = 1: 4 to 4: 1.

  If the ratio of the dry paper strength enhancer is excessive, it is difficult to adjust the texture, causing a problem of soiling in the paper machine system, and if the wet strength enhancer is added excessively, the waste paper can be reused. Not only is it difficult, but there is a problem that the gypsum board is damaged when sticking to the surface of the Yankee dryer or peeling the wallpaper.

[Wet paper strength enhancer]
Examples of the wet paper strength enhancer suitably used for the wallpaper backing paper of the present invention include epoxidized polyamide resin, acrylate ester, dialdehyde starch, melamine resin, urea resin, polyethyleneimine, and polyamide / epichloropyrroline resin. Examples include wet paper strength enhancers including Although there is no limitation in particular about the usage-amount of a wet paper strength enhancer, it is preferable to make it adhere 0.015-0.3g per square meter of paper obtained from a pulp. When the amount of the wet paper strength enhancer used is less than 0.015 g / m ² , it is not possible to sufficiently impart water resistance to the backing paper for wallpaper, and workability after applying glue to the backing paper for wallpaper. Decreases. When the amount of the water-resistant agent used exceeds 0.3 g / m ² , the resulting paper becomes hard, and the effect of improving the water resistance according to the amount of the wet paper strength enhancer cannot be obtained.

[Dry paper strength enhancer]
The dry paper strength enhancer suitably used for the wallpaper backing paper of the present invention is an acrylamide-based dry paper strength enhancer.

  Examples of acrylamide-based dry paper strength enhancers include acrylamide and aminomethylacrylamide copolymer salts or quaternary ammonium salts, acrylamide and quaternary ammonium base-containing alkyl (meth) acrylate copolymers, acrylamide, and the like. And a polyacrylamide-based dry paper strength enhancer having a molecular weight of about 500,000 to 1,500,000, such as sodium acrylate copolymer.

  As the dry paper strength enhancer, in addition to the acrylamide-based dry paper strength enhancer, a dry paper strength enhancer such as raw starch, processed starch, and vegetable gum can be used in combination as appropriate. Polyacrylamide-based dry paper strength enhancers are particularly excellent. The addition amount of the dry paper strength enhancer is adjusted to about 0.2 to 1.5% by mass with respect to the absolutely dry pulp. Incidentally, if it is less than 0.2% by mass, it is difficult to obtain the heat resistance desired by the present invention. On the other hand, if it exceeds 1.5% by mass, its action and effect are saturated, which is not desirable from an economic viewpoint.

  The backing paper for wallpaper of the present invention has an ash content of 1 to 18% by mass measured according to JIS-P8252 in order to obtain good resin foamability, strength, wallpaper peelability, dimensional stability, and concealment. Thus, it is more preferable to make it contain so that it may become 5-15 mass%. When the ash content is less than 1% by mass, it becomes difficult to adjust the thermal conductivity of the resulting backing paper for wallpaper to a predetermined range, and the resin tends to cause poor foaming when processed into wallpaper. Moreover, in addition to being inferior in concealability, the interlayer strength tends to be high, leading to a problem that the peeling work efficiency at the time of reforming is lowered.

  Furthermore, it becomes difficult to obtain the dimensional stability necessary for wallpaper backing paper.

  Furthermore, the present inventors applied a synthetic resin such as vinyl chloride resin or olefin resin to wallpaper backing paper at the time of wallpaper production, pre-dried at about 160 ° C, and then applied the resin in a heating furnace at about 230 ° C. In the step of foaming, it has been found that the resin foamability is greatly influenced by the thermal conductivity of the backing paper.

  As a more preferable structure of the backing paper for wallpaper of the present invention, the thermal conductivity is preferably 0.2 to 0.5 W / (m · K), and 0.3 to 0.5 W / (m · K). More preferably. In order to set the thermal conductivity of the backing paper for wallpaper to 0.2 to 0.5 W / (m · K), the specific heat of the filler at a temperature of about 230 ° C. for drying and foaming the wallpaper resin is 1.2 J / g. It is preferable to use inorganic particles of / deg or less, and it is more preferable to use inorganic particles of 1.1 J / g / deg or less. If the specific heat at 230 ° C of the filler used is higher than 1.2 J / g / deg, it becomes difficult to set the thermal conductivity of the backing paper for wallpaper to 0.2 to 0.5 W / (m · K). Since the heat for foaming and drying the resin is hindered by the backing paper, it is difficult to be transmitted to the resin and the temperature rise of the resin is hindered, so it is not possible to obtain good foamability of resins such as vinyl chloride resin and olefin resin It is.

  About the backing paper by the above manufacturing method, by making the content ratio of mechanical pulp and filler content within a certain range, while obtaining the required dimensional stability, concealment, and peeling workability at the time of renovation, Furthermore, the thermal conductivity can be adjusted to 0.2 to 0.5 W / (m · K), and the foaming property of the resin is improved by increasing the thermal conductivity of the backing paper to a certain range.

  In addition, the clay and the regenerated particle aggregate that can be suitably used in the present invention preferably have an average particle size of 15 μm or less by the Coulter counter method from the viewpoint of concealment. When the average particle diameter exceeds 15 μm, the opacity decreases and it becomes difficult to obtain a desired concealing property.

  Moreover, it becomes easy to adjust the said interlayer intensity | strength (internal bond) to 70-120 mJ by the mixing | blending of these fillers. If the internal bond is lower than 70 mJ, peeling work at the time of renovation becomes easy, but there is a possibility that delamination may occur due to an unintentional external force at the time of wallpaper bonding work, making it difficult to obtain the desired strength as wallpaper. Moreover, when it exceeds 120 mJ, the peeling work efficiency of the wallpaper at the time of remodeling falls.

  In the present invention, the wallpaper backing paper contains inorganic particles in an amount of 5 to 18% by mass, preferably by using clay or recycled particle aggregates as the inorganic particles, thereby improving the dimensional stability of the wallpaper backing paper, By setting the opacity according to JIS 8138 to 85 to 90%, and more preferably by setting the opacity to 90 to 92%, it is possible to obtain a backing paper with high concealment. If the filler content (ash content) is less than 1% by mass, it is difficult to obtain the desired concealment. Conversely, if the filler content exceeds 18% by mass, the rigidity and strength required for the backing paper for wallpaper are required. It becomes difficult to get.

  Therefore, in this invention, 1-65 mass% of mechanical pulp is contained in the pulp, and the thermal conductivity of the backing paper for wallpaper is 0.2 by including the filler so that the ash content is 1-18 mass%. It is one of the embodiments to set it to -0.5W / (m * K). Furthermore, it is one of the more preferable embodiments to use specific inorganic particles, specific specific heat, and inorganic particles having a particle size.

[Example]
Next, specific examples of the present invention will be described.

Common Items in Examples 1 to 15 and Comparative Examples 1 to 10 In order to confirm the effect of the backing paper for wallpaper according to the present invention, various samples as described below were prepared, and tests for evaluating the quality of these samples were performed. Went. 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, chemicals, and the like shown in this embodiment are merely examples, it goes without saying that the present invention is not limited by these embodiments and can be appropriately selected.

  15 types of paper according to the embodiments of the present invention (referred to as “Example 1” to “Example 15”) and 10 types of paper for comparison with these Examples 1 to 15 (This is referred to as “Comparative Example 1” to “Comparative Example 10”) was fabricated with the configuration shown in Table 1.

  The regenerated particle aggregate used in this example was prepared by the following method.

<Regenerated particle aggregate>
(1) A deinked floss was used as a raw material, and after the dehydration step, the raw material was dried so that the water content was 40% and the dry matter water content was 5% to obtain a raw material having an average particle diameter of 1000 μm.

  (2) In the firing step, the primary firing temperature is 520 ° C., the oxygen concentration is 7.00% in the upper part of the primary firing furnace, the unburned rate after the primary firing furnace is 25.9%, the secondary firing temperature is 510 ° C., the secondary As a result of firing under the condition that the oxygen concentration in the firing furnace is 20.0%, the obtained regenerated particles have a whiteness of 80.7%, and the ratios in terms of oxides of calcium, silica, and aluminum are calcium. 30%, silica 35%, and aluminum 35%, and the proportion of calcium, silica, and aluminum in the constituent components was 87% of the total composition of the regenerated particles.

  (3) The obtained regenerated particle agglomerates were pulverized by a wet pulverizer and used for Examples of the present invention.

<Silica-coated regenerated particle aggregate>
(4) Further, the regenerated particle aggregate obtained in (3) is subjected to a silica coating treatment at a liquid temperature of 100 ° C. and a pH in the final reaction of 8.0 in a silica treatment step, and volume average particles after silica coating. A silica-coated regenerated particle having a diameter of 7.0 μm was obtained and used for the examples of the present invention.

  (5) The silica-coated regenerated particles described in (4) are calcium, silica, and aluminum in terms of oxide equivalents of 10% calcium, 80% silica, and 10% aluminum, and 95% in the constituent components. Yes, it was confirmed that the ratio of the particle diameter of 0.1 to 10 μm was 80% or more.

[Example 1]
As a raw material for wallpaper backing paper, after blending 40% by weight of softwood bleached kraft pulp (NBKP), 20% by weight of hardwood bleached kraft pulp (LBKP) and 40% by weight of mechanical pulp (BTMP), as a filler for internal addition , Clay was added so that the ash content of the resulting paper backing paper was 10% by mass, the sulfuric acid band was 2.5% by mass, and the sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) was solid. 1.0% by mass conversion, dry paper strength enhancer (trade name: DS-4360, produced by Seiko PMC Co., Ltd.) 0.8% by mass in terms of solid content, wet paper strength enhancer (WS4024, Seiko PMC shares) The raw material slurry was prepared by adding 1.2% by mass in terms of solid content. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When the backing paper for wallpaper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 2.0 mm.

[Example 2]
As a raw material for wallpaper backing paper, after blending 40% by weight of softwood bleached kraft pulp (NBKP), 59% by weight of hardwood bleached kraft pulp (LBKP) and 1% by weight of mechanical pulp (BTMP), as a filler for internal addition , Clay was added so that the ash content of the resulting paper backing paper was 10% by mass, the sulfuric acid band was 2.5% by mass, and the sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) was solid. 1.0% by mass conversion, dry paper strength enhancer (trade name: DS-4360, produced by Seiko PMC Co., Ltd.) 0.8% by mass in terms of solid content, wet paper strength enhancer (WS4024, Seiko PMC shares) The raw material slurry was prepared by adding 1.2% by mass in terms of solid content. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When this wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 0.8 mm.

[Example 3]
As a raw material for wallpaper backing paper, after blending 40% by weight of softwood bleached kraft pulp (NBKP), 40% by weight of hardwood bleached kraft pulp (LBKP) and 20% by weight of mechanical pulp (BTMP), as an internal filler , Clay was added so that the ash content of the resulting paper backing paper was 10% by mass, the sulfuric acid band was 2.5% by mass, and the sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) was solid. 1.0% by mass conversion, dry paper strength enhancer (trade name: DS-4360, produced by Seiko PMC Co., Ltd.) 0.8% by mass in terms of solid content, wet paper strength enhancer (WS4024, Seiko PMC shares) A raw material slurry was prepared by adding 1.5% by mass in terms of solid content. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When the wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 0.9 mm.

[Example 4]
As a raw material for wallpaper backing paper, after blending 40% by weight of softwood bleached kraft pulp (NBKP), 30% by weight of hardwood bleached kraft pulp (LBKP) and 30% by weight of mechanical pulp (BTMP), as a filler for internal addition , Clay was added so that the ash content of the resulting paper backing paper was 10% by mass, the sulfuric acid band was 2.5% by mass, and the sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) was solid. 1.0% by weight in terms of minute, 2.0% by weight of dry paper strength enhancer (trade name: DS-4360, manufactured by Seiko PMC Co., Ltd.), wet paper strength enhancer (WS4024, Starlight PMC stock) The raw material slurry was prepared by adding 2.5% by mass of epichlorohydrin manufactured by the company) in terms of solid content. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When the wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 1.0 mm.

[Example 5]
As a raw material for wallpaper backing paper, after blending 40% by weight of softwood bleached kraft pulp (NBKP), 10% by weight of hardwood bleached kraft pulp (LBKP) and 50% by weight of mechanical pulp (BTMP), as a filler for internal addition , Clay was added so that the resulting paper backing paper had an ash content of 12% by mass, a sulfuric acid band was added by 2.5% by mass, and a sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) was solidified. 1.0% by weight in terms of minute, dry paper strength enhancer (trade name: DS-4360, manufactured by Seiko PMC Co., Ltd.) 1.5% by weight in terms of solid content, wet paper strength enhancer (WS4024, Starlight PMC shares) The material slurry was prepared by adding 1.0% by mass in terms of solid content of epichlorohydrin manufactured by the company. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When this wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 1.8 mm.

[Example 6]
After blending 40% by weight of softwood bleached kraft pulp (NBKP) and 60% by weight of mechanical pulp (BTMP) as a pulp raw material for wallpaper backing paper, clay is used as an internal filler, and ash content of the resulting wallpaper backing paper is obtained. Is 10 mass%, the sulfuric acid band is 2.5 mass%, the sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) is 1.0 mass% in terms of solid content, and dry paper strength. 1.0% by mass of an enhancer (trade name: DS-4360, manufactured by Seiko PMC Co., Ltd.) and a wet paper strength enhancer (WS4024, epichlorohydrin manufactured by Seiko PMC Co., Ltd.) are converted into solids. The raw material slurry was adjusted by adding 1.8% by mass. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When this wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 1.9 mm.

[Example 7]
As a raw material for wallpaper backing paper, after blending 30% by weight of softwood bleached kraft pulp (NBKP), 5% by weight of hardwood bleached kraft pulp (LBKP) and 65% by weight of mechanical pulp (BTMP), as a filler for internal addition , Clay was added so that the resulting paper backing paper had an ash content of 12% by mass, a sulfuric acid band was added by 2.5% by mass, and a sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) was solidified. 1.0% by weight in terms of minute, dry paper strength enhancer (trade name: DS-4360, manufactured by Seiko PMC Co., Ltd.) 1.0% by weight in terms of solid content, wet paper strength enhancer (WS4024, Starlight PMC shares) The raw material slurry was prepared by adding 1.8% by mass of epichlorohydrin (manufactured by company) in terms of solid content. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When this wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 1.9 mm.

[Example 8]
As a raw material for wallpaper backing paper, after blending 40% by weight of softwood bleached kraft pulp (NBKP), 20% by weight of hardwood bleached kraft pulp (LBKP) and 40% by weight of mechanical pulp (BTMP), as a filler for internal addition , Clay was added so that the resulting paper backing paper had an ash content of 1% by mass, a sulfuric acid band was added by 2.5% by mass, and a sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) was solidified. 1.0% by weight in terms of minute, dry paper strength enhancer (trade name: DS-4360, manufactured by Seiko PMC Co., Ltd.) 1.5% by weight in terms of solid content, wet paper strength enhancer (WS4024, Starlight PMC shares) A raw material slurry was prepared by adding 1.5% by mass in terms of solid content. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When this wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 1.8 mm.

[Example 9]
As a raw material for wallpaper backing paper, after blending 40% by weight of softwood bleached kraft pulp (NBKP), 20% by weight of hardwood bleached kraft pulp (LBKP) and 40% by weight of mechanical pulp (BTMP), as a filler for internal addition , Clay was added so that the ash content of the resulting paper backing paper was 4% by mass, the sulfuric acid band was 2.5% by mass, and the sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) was solid. 1.0% by weight in terms of minute, dry paper strength enhancer (trade name: DS-4360, manufactured by Seiko PMC Co., Ltd.) 1.5% by weight in terms of solid content, wet paper strength enhancer (WS4024, Starlight PMC shares) A raw material slurry was prepared by adding 1.5% by mass in terms of solid content. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When this wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 1.7 mm.

[Example 10]
As a raw material for wallpaper backing paper, after blending 40% by weight of softwood bleached kraft pulp (NBKP), 20% by weight of hardwood bleached kraft pulp (LBKP) and 40% by weight of mechanical pulp (BTMP), as a filler for internal addition , Clay was added so that the ash content of the resulting paper backing paper was 10% by mass, the sulfuric acid band was 2.5% by mass, and the sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) was solid. 1.0% by mass conversion, dry paper strength enhancer (trade name: DS-4360, produced by Seiko PMC Co., Ltd.) 0.8% by mass in terms of solid content, wet paper strength enhancer (WS4024, Seiko PMC shares) A raw material slurry was prepared by adding 1.5% by mass in terms of solid content. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When this wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 1.7 mm.

[Example 11]
As a raw material for wallpaper backing paper, after blending 40% by weight of softwood bleached kraft pulp (NBKP), 20% by weight of hardwood bleached kraft pulp (LBKP) and 40% by weight of mechanical pulp (BTMP), as a filler for internal addition , Clay was added so that the ash content of the resulting paper backing paper was 18% by mass, the sulfuric acid band was 2.5% by mass, and the sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) was solid. 1.0% by weight in terms of minute, dry paper strength enhancer (trade name: DS-4360, manufactured by Seiko PMC Co., Ltd.) 1.5% by weight in terms of solid content, wet paper strength enhancer (WS4024, Starlight PMC shares) A raw material slurry was prepared by adding 1.5% by mass in terms of solid content. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When this wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 1.6 mm.

[Example 12]
As a raw material for wallpaper backing paper, after blending 40% by weight of softwood bleached kraft pulp (NBKP), 20% by weight of hardwood bleached kraft pulp (LBKP) and 40% by weight of mechanical pulp (BTMP), as a filler for internal addition , Clay was added so that the ash content of the resulting paper backing paper was 15% by mass, 2.5% by mass of sulfuric acid band, and sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) were solidified. 1.0% by weight in terms of minute, dry paper strength enhancer (trade name: DS-4360, manufactured by Seiko PMC Co., Ltd.) 1.5% by weight in terms of solid content, wet paper strength enhancer (WS4024, Starlight PMC shares) The raw material slurry was prepared by adding 0.5% by mass in terms of solid content. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When this wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 1.6 mm.

[Example 13]
As a raw material for wallpaper backing paper, after blending 40% by weight of softwood bleached kraft pulp (NBKP), 20% by weight of hardwood bleached kraft pulp (LBKP) and 40% by weight of mechanical pulp (BTMP), as a filler for internal addition , Clay was added so that the ash content of the resulting paper backing paper was 18% by mass, the sulfuric acid band was 2.5% by mass, and the sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) was solid. 1.0% by weight in terms of minute, dry paper strength enhancer (trade name: DS-4360, manufactured by Seiko PMC Co., Ltd.) 1.5% by weight in terms of solid content, wet paper strength enhancer (WS4024, Starlight PMC shares) The material slurry was prepared by adding 2.0% by mass in terms of solid content. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When this wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 1.7 mm.

[Example 14]
As a raw material for wallpaper backing paper, after blending 40% by weight of softwood bleached kraft pulp (NBKP), 20% by weight of hardwood bleached kraft pulp (LBKP) and 40% by weight of mechanical pulp (BTMP), as a filler for internal addition , Clay was added so that the ash content of the resulting paper backing paper was 10% by mass, the sulfuric acid band was 2.5% by mass, and the sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) was solid. 1.0% by weight in terms of minute, dry paper strength enhancer (trade name: DS-4360, manufactured by Seiko PMC Co., Ltd.) 1.5% by weight in terms of solid content, wet paper strength enhancer (WS4024, Starlight PMC shares) A raw material slurry was prepared by adding 1.5% by mass in terms of solid content. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When this wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 1.7 mm.

[Example 15]
As a raw material for wallpaper backing paper, after blending 40% by weight of softwood bleached kraft pulp (NBKP), 20% by weight of hardwood bleached kraft pulp (LBKP) and 40% by weight of mechanical pulp (BTMP), as a filler for internal addition , Clay was added so that the ash content of the resulting paper backing paper was 6% by mass, the sulfuric acid band was 2.5% by mass, and the sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) was solid. 1.0% by mass conversion, dry paper strength enhancer (trade name: DS-4360, produced by Seiko PMC Co., Ltd.) 0.2% by mass in terms of solid content, wet paper strength enhancer (WS4024, Seiko PMC shares) The material slurry was prepared by adding 1.0% by mass in terms of solid content of epichlorohydrin manufactured by the company. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When this wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 1.7 mm.

[Comparative Example 1]
After blending 40% by weight of softwood bleached kraft pulp (NBKP) and 60% by weight of hardwood bleached kraft pulp (LBKP) as a pulp raw material for wallpaper backing paper, clay is obtained as a filler for internal use. Added so that the ash content is 8% by mass, the sulfuric acid band is 2.5% by mass, the sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) is 1.0% by mass in terms of solid content, and is dried. Paper strength enhancer (trade name: DS-4360, manufactured by Seiko PMC Co., Ltd.) is 0.8 mass% in terms of solid content, and wet paper strength enhancer (WS4024, manufactured by Seiko PMC Co., Ltd., epichlorohydrin) is used as solid content. The raw material slurry was adjusted by adding 1.2% by mass in terms of conversion. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When the wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 0.5 mm.

[Comparative Example 2]
As a raw material for wallpaper backing paper, after blending 10% by weight of softwood bleached kraft pulp (NBKP), 20% by weight of hardwood bleached kraft pulp (LBKP) and 70% by weight of mechanical pulp (BTMP), as an internal filler , Clay was added so that the ash content of the resulting paper backing paper was 8% by mass, the sulfuric acid band was 2.5% by mass, and the sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) was solid. 1.0% by mass conversion, dry paper strength enhancer (trade name: DS-4360, produced by Seiko PMC Co., Ltd.) 0.8% by mass in terms of solid content, wet paper strength enhancer (WS4024, Seiko PMC shares) The raw material slurry was prepared by adding 1.2% by mass in terms of solid content. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When this wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 1.6 mm.

[Comparative Example 3]
As a raw material for wallpaper backing paper, after blending 40% by weight of softwood bleached kraft pulp (NBKP), 20% by weight of hardwood bleached kraft pulp (LBKP) and 40% by weight of mechanical pulp (BTMP), as a filler for internal addition , Clay was added so that the ash content of the resulting paper backing paper was 2% by mass, the sulfuric acid band was 2.5% by mass, and the sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) was solid. 1.0% by mass conversion, dry paper strength enhancer (trade name: DS-4360, manufactured by Seiko PMC Co., Ltd.) 1.2% by mass in terms of solid content, wet paper strength enhancer (WS4024, Seiko PMC shares) The raw material slurry was prepared by adding 1.4% by mass (in terms of solid content) of epichlorohydrin manufactured by the company. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When this wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 1.6 mm.

[Comparative Example 4]
As a raw material for wallpaper backing paper, after blending 40% by weight of softwood bleached kraft pulp (NBKP), 20% by weight of hardwood bleached kraft pulp (LBKP) and 40% by weight of mechanical pulp (BTMP), as a filler for internal addition , Clay was added so that the ash content of the resulting paper backing paper was 20% by mass, the sulfuric acid band was 2.5% by mass, and the sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) was solid. 1.0% by weight in terms of minute, dry paper strength enhancer (trade name: DS-4360, manufactured by Seiko PMC Co., Ltd.) 1.0% by weight in terms of solid content, wet paper strength enhancer (WS4024, Starlight PMC shares) The material slurry was prepared by adding 1.0% by mass in terms of solid content of epichlorohydrin manufactured by the company. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When this wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 1.6 mm.

[Comparative Example 5]
As a raw material for wallpaper backing paper, after blending 40% by weight of softwood bleached kraft pulp (NBKP), 20% by weight of hardwood bleached kraft pulp (LBKP) and 40% by weight of mechanical pulp (BTMP), as a filler for internal addition , Clay was added so that the ash content of the resulting paper backing paper was 10% by mass, the sulfuric acid band was 2.5% by mass, and the sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) was solid. 1.0% by mass conversion, dry paper strength enhancer (trade name: DS-4360, manufactured by Seiko PMC Co., Ltd.) 1.2% by mass in terms of solid content, wet paper strength enhancer (WS4024, Seiko PMC shares) The raw material slurry was prepared by adding 1.4% by mass (in terms of solid content) of epichlorohydrin manufactured by the company. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When this wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 1.7 mm.

[Comparative Example 6]
As a raw material for wallpaper backing paper, after blending 40% by weight of softwood bleached kraft pulp (NBKP), 20% by weight of hardwood bleached kraft pulp (LBKP) and 40% by weight of mechanical pulp (BTMP), as a filler for internal addition , Clay was added so that the ash content of the resulting paper backing paper was 6% by mass, the sulfuric acid band was 2.5% by mass, and the sizing agent (trade name: E-3600, manufactured by Modern Chemical Co., Ltd.) was solid. A raw material slurry was prepared by adding 1.0% by mass in terms of minutes and adding 0.4% by mass of wet paper strength enhancer (WS4024, manufactured by Seiko PMC Co., Ltd., epichlorohydrin) in terms of solids. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When this wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 1.7 mm.

[Comparative Example 7]
A wallpaper backing paper obtained in the same manner as in Example 1 except that a multi-cylinder dryer was used instead of a paper machine equipped with a Yankee dryer. A paper machine equipped with a multi-cylinder dryer was used.

[Comparative Example 8]
As a raw material for wallpaper backing paper, after blending 40% by weight of softwood bleached kraft pulp (NBKP), 20% by weight of hardwood bleached kraft pulp (LBKP) and 40% by weight of mechanical pulp (BTMP), as a filler for internal addition , Clay was added so that the ash content of the resulting paper backing paper was 5% by mass (no recycled particle aggregate was used), 2.5% by mass of sulfuric acid band, sizing agent (trade name: E-3600) , Modern Chemical Co., Ltd.) 1.0% by mass in terms of solid content, and 0.8% by mass of dry paper strength enhancer (trade name: DS-4360, manufactured by Seiko PMC Co., Ltd.) in terms of solid content. The raw material slurry was adjusted. This raw material slurry was paper-made with a long paper machine equipped with a Yankee dryer, and a backing paper for wallpaper having a basis weight of 65 g / m ² was obtained.

  When this wallpaper backing paper was disaggregated according to JIS-P8220, the number average fiber length of the disaggregated pulp was 1.7 mm.

[Comparative Example 9]
Evaluation was conducted in the same manner as in the Examples with respect to 60 g / m ² of general bleached glazed kraft paper commercially available.

[Comparative Example 10]
Evaluation was made in the same manner as in the example with respect to a commercially available general copy paper of 64 g / m ² .

  “Specific heat (230 ° C. specific heat: J / g / deg)” in Table 1 is 100 to 100 in differential scanning calorimetry (DSC) using a thermal analyzer manufactured by Seiko Instruments Inc. according to JIS-K7123. It is a value of 230 ° C. in which the specific heat change amount is measured in the range of 250 ° C.

  The “ash content (%)” is a value obtained by measuring the ash content when combusted at 525 ° C. according to JIS-P8252.

  “Thermal conductivity (W / (m · K))” is a value measured by a heat flow meter method using a thermal conductivity meter manufactured by Kyoto Electronics Industry Co., Ltd. according to JIS-A1412-2. . The measurement was performed under the condition of a temperature of 20 ° C.

  “Polyvinyl chloride resin foaming” means that a vinyl chloride paste is applied to a thickness of 100 μm with a table blade coater, pre-dried at 160 ° C., and then foamed in a heating furnace at 230 ° C. to obtain a prototype vinyl wallpaper. The foamability was evaluated. “◎” indicates that foamability is very good, “◯” indicates that there is no problem, “Δ” indicates that foamability is slightly poor, and “×” indicates that foamability is poor and cannot be used as a backing paper.

  “Tensile strength (longitudinal) (kN / m)” is a value in the longitudinal direction (flow direction) measured by “Testing method of paper and paperboard—tensile properties” defined in JIS-P8113.

  “Wet tensile strength (longitudinal) (kN / m)” is a value in the longitudinal direction (flow direction) measured by “paper and paperboard—wet tensile strength test method” defined in JIS-P8135.

  “Interlaminar strength (mJ)” refers to JAPAN TAPPI No. It is a value measured by the internal bond tester method specified in 18-2.

  “Wallpaper peelability” refers to a prototype vinyl wallpaper in which vinyl chloride paste is applied to wallpaper backing paper, starch paste is applied to the backing paper surface, and then applied to a plywood board for 3 days at 23 ° C., 50% R / After standing under the condition of H, the delamination property when peeled from the plywood board and the remaining way of the backing paper for wallpaper remaining on the plywood board were observed. “◎” indicates that the release peels uniformly between the paper layers, “○” indicates that the release does not occur without problem, and part of the backing paper remains on the resin side, and part of the backing paper remains on the plywood side, and peels unevenly. It was set as “x”.

  “Elongation in water (lateral)” is a value measured according to the J · TAPPI-No. 27-28A method.

  “Wall paper opening” means that a trial vinyl wallpaper coated with vinyl chloride paste is cut into a rectangle with the long (flowing) direction of the backing paper as the long side, and starch paste is applied to the surface of the backing paper. The two papers are pasted on a plywood board so that the long sides do not overlap each other and do not overlap, and then left for 3 days at 23 ° C. and 50% R / H. The presence or absence was confirmed. “◎” indicates that there is no opening, “◯” indicates that there is no problem, and “×” indicates that the opening is large.

  “Opacity (%)” is a value measured by “paper and paperboard—opacity test method (backing of paper) —diffuse illumination method” defined in JIS-P8149.

  “Concealment” refers to a prototype vinyl wallpaper in which vinyl chloride paste is applied to wallpaper backing paper, starch paste is applied to the backing paper surface, and then applied to a plywood board for 3 days at 23 ° C., 50% R / H. Then, the wallpaper was visually evaluated for the concealment property of the wallpaper. Those with excellent concealment were marked with “◎”, those with no problem were marked with “◯”, and those with poor concealment and impaired commercial value were marked with “X”.

Evaluation The backing paper for wallpaper of the present invention, as shown in claim 1, is a backing paper for wallpaper using a Yankee paper machine equipped with a Yankee dryer and using pulp and filler as main materials as raw materials,
The pulp contains 1 to 65% by weight of mechanical pulp,
The filler contains clay and regenerated particle aggregates as main components, and preferably contains a mixture ratio of clay and regenerated particle aggregates in a ratio of 2/8 to 8/2. The wallpaper backing paper of Examples 1 to 15 satisfying all of these conditions, although it is a wallpaper backing paper contained in the paper so that the ash content of the wallpaper backing paper measured in accordance with 1 to 18% by mass. The paper had excellent evaluation (◎ or ○ evaluation) in various physical properties such as PVC resin foaming property, wallpaper peeling property, wallpaper opening, and concealing property. On the other hand, the backing paper for wallpaper of Comparative Example 1 having a mechanical pulp content lower than the conditions in claim 1 is inferior in wallpaper peelability and hiding properties (x evaluation), and the mechanical pulp content in claim 1 The backing paper for wallpaper of Comparative Example 2, which has more conditions than the above, was inferior in PVC resin foamability and wallpaper opening (x evaluation).

  In addition, as a comparative example 9, a commercially available bleached piece glossy kraft paper was evaluated as a reference, but the results were inferior in PVC resin foaming property, wallpaper peelability, and wallpaper opening (× evaluation), and the difference from the present invention product was clear Met.

  In addition, commercially available high-quality paper was evaluated as Comparative Example 10 for reference, but the results were inferior in wallpaper peelability and wallpaper opening (× evaluation), the difference from the product of the present invention was clear, and the backing for wallpaper It was not usable as paper.

Claims (4)

Using a Yankee paper machine equipped with a Yankee dryer, wallpaper backing paper with pulp and filler as main ingredients,
The pulp contains 1 to 65% by weight of mechanical pulp,
Recycled particle aggregates are contained as the filler, and the ash content of the backing paper for wallpaper measured according to JIS-P 8252 is contained in the paper so as to be 1 to 18% by mass. Lined paper for wallpaper.   2. The filler according to claim 1, wherein the blending ratio of clay and regenerated particle agglomerates is 2/8 to 8/2 based on clay and regenerated particle agglomerates as main components. Lined paper for wallpaper.   The base paper is flattened by pressing the metal surface of the Yankee dryer with a roll without using a felt, and the glossy surface JIS-P 8119 that touches the metal surface of the Yankee dryer for wallpaper backing paper. The wallpaper backing paper according to claim 1 or 2, wherein the smoothness of the non-glossy surface that does not contact the metal surface of the Yankee dryer is 5 seconds or more according to the above. .   The raw material contains a wet paper strength enhancer and a dry paper strength enhancer, and has a wet tensile strength (longitudinal) of 0.3 kN / m or more and 1.0 kN according to JIS-P 8135 for backing paper for wallpaper. The backing paper for wallpaper according to any one of claims 1 to 3, wherein the backing paper is / m or less.