JP5963231B2 - Manufacturing method of tissue paper products - Google Patents

Description

  The present invention relates to a method for manufacturing tissue paper products, and in particular, in a multi-stand type interfolder, the secondary continuous sheet is not unwound from a secondary raw roll obtained by winding a secondary continuous sheet coated with a chemical solution. The present invention relates to a method for supplying and manufacturing a tissue paper product to which a chemical solution is applied.

[Tissue paper products]
A bundle of tissue paper is stored in a storage box, and the tissue paper is sequentially pulled out from the outlet provided on one side of the storage box (also called a carton box or tissue carton). Tissue paper products are well known (a type in which when a sheet is taken out, the next sheet is continuously pulled out from the take-out port is also called a pop-up type).

In this tissue paper product, there are a chemical solution application type in which a tissue paper to be stored is applied with a chemical solution imparting moisture retention and flexibility, and a general-purpose product or general-purpose type in which no chemical solution is applied.
A tissue paper coated with a chemical is superior to a general-purpose product in terms of surface smoothness and softness.

  Demand for chemical-coated products tended to increase at times when the chances of biting increased, such as when hay fever and influenza are prevalent, but in recent years there have been advantages in terms of usability such as smoothness and softness of the surface. It has been evaluated and used regardless of season and time, and its demand is expanding.

[Types of chemicals used in chemical-coated products]
There are various types of chemicals used in chemical-coated products that have been applied with chemicals that impart moisturizing properties and flexibility, but most of them are water-based chemicals containing water and polyol (usually called “water-based lotion agents”). Are roughly classified into oil-based chemicals that contain water-insoluble wax and the like and are semi-solid at room temperature. Aqueous chemicals are characterized by excellent handling and low cost.

  In addition, when applied to a sheet, an aqueous chemical solution is excellent in affinity with pulp fibers constituting the sheet, impregnated in the sheet thickness direction (also referred to as Z direction), and modifies the entire sheet and its surface properties. Acts as follows. On the other hand, the oil-based chemical liquid mainly acts to coat the surface, and acts to improve the smoothness of the surface.

And since an aqueous | water-based chemical | medical solution impregnates a sheet | seat, the effect | action which extends the crepe coated on the sheet | seat after application | coating is large, but such an effect | action is small with an oil-type chemical | medical solution.
There are differences in problems such as manufacturing problems depending on the characteristics of both.
An aqueous chemical solution is suitable for low cost and mass production.

[Overview of conventional manufacturing methods for tissue paper products]
The manufacturing process of tissue paper products is as follows.
First, a thin paper (also referred to as crepe paper) having a crepe is made in a paper making facility, and this is wound up to produce a primary roll (generally also called a jumbo roll).

  Next, the required number of primary rolls are set in a ply machine, and a primary continuous sheet is fed out from each of the set primary rolls. 2) is produced.

  Next, the secondary web roll is transferred to a folding facility called an interfolder, secondary continuous sheets are fed out from the secondary web roll sequentially, the secondary continuous sheets are folded and sequentially laminated, and cut into tissue paper. Produce a bundle. Next, this tissue paper bundle is stored in a storage box to obtain a tissue paper product.

[Types of interfolders used to manufacture tissue paper products]
Here, in manufacturing tissue paper bundles used for tissue paper products, two types of multi-stand type (multiple type) interfolders (Patent Documents 1 and 2 below) and rotary interfolders (Patent Documents 3 and 4) are used. Inter folder is used.

  As shown in Patent Documents 1 and 2, the former multi-stand type interfolder has a large number of folding mechanism sections (usually 80 to 120 machines) arranged in the line flow direction. The secondary web roll is fixed to the secondary web roll support section corresponding to the above, and the secondary continuous sheet is unwound from the secondary web roll, and the secondary continuous sheet is supplied to the folding mechanism section. At that time, the multi-stand type interfolder arranges two sets of secondary rolls slit to the same width as the width of tissue paper for each folding mechanism part, and at the same time, the secondary continuous sheet is continuous from the secondary roll. The secondary continuous sheet is folded at each folding mechanism unit, and the second continuous sheet folded at the folding mechanism unit at the upstream side of the line is folded at the folding mechanism unit at the downstream side of the line. The folded secondary continuous sheets are sequentially laminated, and a continuous laminated sheet bundle in which the required number of sheets is laminated at the most downstream side is formed.

  Here, one machine of the folding mechanism unit is a unit of equipment that folds the secondary continuous sheet so as to be folded inward, and is a unit of the mechanism unit that is the basis of the multi-stand type interfolder.

  Here, since the multi-stand type interfolder has a large number of folding mechanisms, a large number of secondary web rolls are required. And, in order to reduce the complexity of the mounting, the secondary raw roll is obtained by winding a secondary continuous sheet slit to the same width as the width of the tissue paper adjacent to a plurality of tube axes. Often used. Usually, two sets of secondary web rolls wound around one tube shaft are used so that the supply to the folding mechanism can be suitably performed. In addition, the process of slitting to the width of tissue paper is performed immediately before the folding mechanism part of the multi-stand type interfolder, using a secondary raw roll obtained by winding a continuous sheet slit to about 2 to 10 times the width of the tissue paper. Sometimes it is done at

  On the other hand, the rotary interfolder cuts each secondary continuous sheet fed from a pair of secondary web rolls while folding them from the front end with a rotary folding plate, and from each of the cut secondary web rolls. Sheets are sequentially stacked to form a laminated sheet bundle.

In the rotary type interfolder, an original roll having a width of 5 times or more the tissue paper width is used.
Therefore, this rotary interfolder has an operation for obtaining a laminated sheet bundle by performing appropriate marking and manual division at a predetermined number of laminated sheets in a continuous operation, or automatic division at a predetermined number of laminated sheets. . And the laminated sheet bundle obtained is a comparatively short thing of the length substantially the same as the width length of a secondary original fabric roll. For this reason, it is inferior in productivity as compared with the multi-stand type interfolder.

  For example, in a rotary type interfolder, if a tissue paper bundle is produced at a processing speed of 100 m / min using an original roll having a width 5 times the width of the tissue paper, it takes about 25 bundles / minute. In contrast, the multi-stand type interfolder can produce 435 bundles / minute at a processing speed of 100 m / minute.

[Relationship between tissue paper product type and inter-folder type]
As mentioned above, the multi-stand type interfolder is used for the manufacture of general-purpose type products that require a large amount of production because of its high productivity. The rotary type inter-folder is produced in comparison with the general-purpose type. It is used for the manufacture of a chemical solution coating type with a small amount (for example, Patent Document 5 below).

  Also, in the rotary type interfolder, a wide original roll is used and the operation speed is slow due to the folding mechanism, so that the chemical solution is applied online to the secondary continuous sheet unwound from the secondary original roll. In contrast, it is necessary to set a large number of secondary web rolls in a multi-stand type interfolder, so that chemical solution coating equipment is installed on each of the many secondary web rolls. The fact that it is complicated in terms of quality control, such as adjusting the coating amount of each raw roll, is difficult to perform online coating, which is also a factor that makes different types of tissue paper products manufactured in each inner folder.

  In addition, as for the manufacturing method of the conventional chemical | medical solution application type product, the manufacturing method and equipment are illustrated by the following patent documents 5-7.

  However, considering the increase in production due to the growing demand for chemical-coated tissue paper products as described above, it is desired to manufacture the chemical-coated tissue paper products in a multi-stand type interfolder.

  However, it has been difficult to manufacture chemical tissue-applied tissue paper products using a multi-stand type interfolder due to the following technical problems in addition to the application problems.

[Problems when manufacturing chemical application type products with a multi-stand type interfolder]
When manufacturing chemical solution-coated tissue paper with a multi-stand type interfolder, as described above, online application of chemical solution to the secondary material roll requires complexity, so a secondary continuous sheet pre-applied with chemical solution is used. It is convenient to prepare a wound secondary web roll. Such a secondary material roll is manufactured from a chemical material application facility such as a printer facility other than the multi-stand type interfolder, or a primary material roll which is a pre-stage facility of the multi-stand type interfolder. Manufacture is possible if a ply machine is provided with a printing machine to apply a chemical solution.

  However, in the multi-stand type interfolder, even if a secondary raw roll with a chemical solution applied (hereinafter also simply referred to as a secondary raw roll) is used, the secondary roll roll may be unrolled. It is difficult to increase productivity. This problem will be further described in detail.

  First, in the multi-stand type interfolder, it is necessary to supply a secondary continuous sheet having an extremely long tissue paper width to each folding mechanism as described above. In general, the secondary raw roll used is of a small width and a large diameter, and even a roll of continuous sheets having a width multiple of tissue paper width is smaller than that used for a rotary interfolder. Often used.

  The secondary continuous sheet constituting the secondary material roll to which the chemical solution is applied is not only the effect of the chemical solution itself, but also the crepe is extended by the chemical solution application, so that the friction resistance of the sheet surface is reduced to the secondary of the non-chemical solution application. It tends to be lower than the continuous sheet. In addition, in the multi-stand type interfolder, as described above, the chemical solution is applied by a facility different from the interfolder. Therefore, the chemical solution application secondary raw roll requires a predetermined time from manufacture to use, and the chemical solution between the sheets is used. The diffusion permeation time of water and the moisture absorption period of moisture in the air become longer, so that the decrease in the frictional resistance of the surface tends to increase. Furthermore, when the secondary continuous sheet is stretched due to moisture absorption or the like after the secondary raw roll is formed, the winding of the secondary raw roll itself is loosened. This becomes particularly remarkable in the above-described aqueous chemical solution.

  On the other hand, in the conventional multi-stand type interfolder, the secondary continuous sheet is unwound from the secondary raw roll having a small width and a large diameter, as shown in FIGS. The feeding belt 183 is driven by a driving source such as a motor and is ideally driven with a small acceleration so as to be always in contact with the surface at a holding angle ∠B of more than 0 ° to 20 °. By rotating the secondary web roll 100x at a stable speed, the secondary continuous sheet S104 is unwound from the outer peripheral side of the secondary web roll 100x. Here, as can be understood from FIG. 12 in particular, the feeding belt 183 is arranged so as to always contact the upper part of the outer peripheral surface of the secondary raw roll 100x. This is because when the secondary web roll 100x is reduced in diameter as the secondary continuous sheet S104 is fed, the feed belt 183 moves downward due to the weight of the apparatus, etc., and always on the outer peripheral surface of the secondary web roll 100x. This is to make contact. Further, as can be understood from FIG. 13, in the secondary web roll 100x in which the secondary continuous sheets S104 and S104 are wound in a plurality, the feeding belt 183 is provided between the winding portions of the secondary continuous sheets S104 and S104. And a plurality of secondary continuous sheets S104, S104 are effectively unwound from the secondary raw roll 100x.

  However, in the unwinding mode of the secondary continuous sheet from such a secondary raw roll, the factors caused by the above-mentioned chemical solution application and the shape of the small and large diameter are combined, and the outer peripheral side in contact with the feeding belt is Although it is pressed by the feeding belt and rotates at an appropriate speed according to its driving speed, the pressing by the feeding belt is not sufficiently transmitted to the winding core side of the secondary raw roll through the sheet layer, and the winding core side The rotational speed may be higher than that on the outer peripheral surface side, and this causes a so-called winding deviation in which the winding is shifted between the core side and the outer peripheral surface side. Note that although the principle of occurrence of winding deviation is not clear, it is also presumed to be due to a difference in inertia between the outer peripheral surface of the secondary raw roll and the tube shaft.

  When the winding deviation occurs in this way, the secondary continuous sheet unwound from the secondary material roll is supplied to the folding mechanism unit while being shifted left and right or back and forth with respect to the advancing direction. Problems such as wrinkling of tissue paper products or defective folding, and pop-up mechanisms becoming discontinuous due to defective folding occur.

  Here, the winding deviation is noticeably generated in the secondary raw roll having a small width and a large diameter, but may also occur in the secondary raw roll having a relatively wide width. And when winding deviation generate | occur | produces when using a comparatively wide secondary raw material roll, the problem that a malfunction generate | occur | produces in the slit process performed before a folding mechanism part arises.

  In addition, the multi-stand type inner folder is a folding mechanism that forms a laminated continuous sheet bundle together with secondary continuous sheets wound from a number of other secondary raw rolls regardless of the width of the secondary raw roll. Therefore, when a winding deviation occurs in a certain secondary web roll, even if the secondary continuous sheet unwound from the other secondary web roll is normally unwound, a problematic continuous laminated sheet bundle is formed. Will be formed. That is, all of the secondary continuous sheets that are normally unwound from the other secondary raw rolls are wasted.

  Further, in the multi-stand type interfolder, the secondary continuous sheet unwound from the secondary raw roll is wound around an appropriate roll by the folding mechanism unit, and its folding direction is changed and folded by the folding plate. A laminated continuous sheet bundle is formed, and the laminated continuous sheet bundle is conveyed by a pull roll. Therefore, when the conveyance of the secondary continuous sheet shifts from side to side or back and forth due to winding deviation, it is wound on the roll and the folding plate is dropped or wrinkled when the traveling direction is changed. To form a defective laminated continuous sheet bundle.

  In the multi-stand type interfolder, since the continuous laminated sheet bundle is boxed and cut by the final stage cutter, it is difficult to remove only the problematic sheet bundle afterwards.

  As described above, in the multi-stand type interfolder, the winding deviation generated in one of the plurality of secondary raw rolls used becomes obvious as a manufacturing problem.

  In a rotary interfolder, a slight winding deviation may occur even when a wide secondary roll roll pre-impregnated with a chemical solution is used. However, in a rotary interfolder, a pair of secondary rolls Since each secondary continuous sheet unwound from the roll is supplied to the folding mechanism without changing its traveling direction and is alternately folded, there is a shift in the conveyance direction of the secondary continuous sheet due to winding deviation. Even in such a case, the deviation in the conveyance direction is easily corrected, and the deviation in the horizontal direction is corrected by the trim cutting process that is usually provided on the left and right edges, so that it is caused by the winding deviation before being supplied to the folding mechanism. The transport deviation of the secondary continuous sheet is corrected and does not manifest as a manufacturing problem.

  As described above, when producing a tissue paper product of a chemical solution application type in a multi-stand type interfolder, the problem of slippage of the secondary raw roll makes the production difficult.

  In addition, although the technique shown by the following patent documents 8-10 is disclosed regarding winding-up of roll paper, it prevents winding slip at the time of unwinding of the secondary continuous sheet from a secondary original fabric roll. It is not a thing.

US Patent No. 4052048 (Japanese Patent Publication No. 55-1215) JP 2006-240750 A JP 61-37668 A Japanese Patent Laid-Open No. 5-124770 Japanese Patent Application Laid-Open No. 2004-332034 Special table 2008-525103 gazette JP 2008-264564 A Japanese Patent Laid-Open No. 63-123743 JP 2009-220991 A JP 2007-106508 A JP 2011-136504 A JP 2011-156116 A

  Accordingly, the main problem of the present invention is to solve the problem of winding that has occurred in the production of a chemical-coated tissue paper product in a multi-stand type interfolder, and to efficiently manufacture a chemical-coated tissue paper product. Is to provide.

The present invention that has solved the above problems is as follows.
[Invention of Claim 1]
Tissue paper product having a step of feeding the secondary continuous sheet from a secondary web roll formed by winding a secondary continuous sheet coated with a chemical solution around a tube shaft and supplying the secondary continuous sheet to a folding mechanism of a multi-stand type interfolder A manufacturing method of
The secondary material roll is supported on a support member having an urging function in the ascending direction so as to be movable up and down,
A feeding belt is arranged below the outer peripheral surface of the secondary web roll so that the secondary web roll is always placed on the feeding belt via the outer circumferential surface, and is attached in the upward direction. In a state where the load applied to the feeding belt of the secondary raw roll is reduced by the support member having the urging function,
The secondary belt is rotated by driving the feeding belt, the secondary continuous sheet is fed from the outer peripheral surface of the secondary raw roll, and supplied to the folding mechanism.
A method for producing a tissue paper product.

[Invention of Claim 2]
The manufacturing method of the tissue paper product of Claim 1 which makes the holding angle with respect to the secondary raw material roll outer peripheral surface of a feeding belt 50-180 degrees.

[Invention of Claim 3]
When the secondary roll is a roll of a plurality of secondary continuous sheets wound around a tube axis, the feeding belt is a coaxial arrangement of separate belts in contact with each secondary continuous sheet, The manufacturing method of the tissue paper of Claim 1 or 2.

[Invention of Claim 4]
The method for producing a tissue paper product according to any one of claims 1 to 3, wherein a feeding direction of the secondary continuous sheet from the secondary web roll is a direction from the lower side to the upper side.

[Invention of Claim 5]
The feed belt is wound around a pair of rolls arranged before and after the secondary roll, and the secondary roll is placed on the feed belt between the pair of rolls. The manufacturing method of the tissue paper product of description.

(Function and effect)
As in the prior art, in the aspect in which the driving belt is arranged on the upper part of the secondary web roll, if the feeding belt is arranged along the peripheral surface of the secondary web roll and the holding angle is increased, the driving belt is placed on the upper side. Although it was difficult due to the increase in the scale and weight of the incidental device to be positioned and the holding angle was up to about 20 °, in the present invention, the secondary raw material roll was supported in a vertically movable manner instead of the driving belt, Since the feeding belt is arranged below the outer peripheral surface of the secondary web roll so that the secondary web roll is always placed on the feeding belt through the outer circumferential surface, the design flexibility of the feeding belt is increased. Improved and made it possible to increase the holding angle.

  In the present invention, since the holding angle can be increased in this way, the range in contact with the outer peripheral surface of the secondary original roll is widened, it is difficult to slip, and the rotation of the secondary original roll can be stably controlled. As a result, the difference between the feeding speed of the secondary continuous sheet (angular speed of the outer surface of the secondary web roll) and the rotational speed of the secondary web roll (angular speed on the center side from the outer surface of the secondary web roll) It can be made smaller and winding deviation can be improved.

  In addition, the winding deviation is likely to occur at the start of the rotation of the secondary web roll, but in the present invention, the holding angle can be increased. Occurrence can also be prevented. Furthermore, when the holding angle is large, the bounce of the secondary material roll is also prevented, so that the operation stability is improved.

  On the other hand, conventionally, in the feeding mode, the holding angle is small and the secondary web roll and the feeding belt are in contact with each other in a mode in which the feeding belt is placed on the upper part of the secondary web roll. The secondary roll may be deformed because it is intensively applied to the contact portion of the belt, and this causes the conveyor belt to bounce around the outer surface of the secondary roll, which also causes winding slippage. In the present invention, the holding angle can be increased as described above, the deformation of the secondary raw roll can be prevented, and the winding deviation caused by the deformation can also be prevented.

  Further, conventionally, in the feeding mode, even if the secondary continuous sheet is pulled out from the secondary web roll and the winding amount of the secondary web roll changes, the weight of the feeding belt does not change. Then, since it is a mode in which the secondary web roll is placed on the feeding belt, according to the reduction in the diameter and weight of the secondary web roll by feeding the secondary continuous sheet from the secondary web roll. Since the load becomes variable so that the load is reduced, stable feeding can be performed and winding deviation can be prevented very effectively.

  Here, the specific holding angle at which the effect of the present invention is remarkable is 50 to 180 °, and in the present invention, this range is desirable.

  Further, in the present invention, when the feed belt is wound around a pair of rolls arranged before and after the secondary roll, and the secondary roll is placed on the feed belt between the pair of rolls, It is possible to make the original roll roll stably placed on the feeding belt. Further, the followability of the feeding belt with respect to the outer peripheral surface of the secondary web roll is stabilized, and the effect of preventing the winding deviation is high.

  Further, when the secondary web roll is supported by a support member having an urging function in the upward direction so as to reduce the load on the feeding belt of the secondary web roll, the secondary web roll The entire weight is not loaded on the feeding belt, and can be set to an appropriate weight. Thereby, in addition to exhibiting the effect of preventing the winding slip, the paper thickness of the secondary continuous sheet is not crushed, and the product becomes more easily bulky.

  Here, as a form of the secondary web roll, when a plurality of secondary continuous sheets are wound around the tube shaft, conventionally, one feed belt is disposed so as to straddle each secondary web roll. In this mode, in combination with the weighting from above, as shown by the one-dot chain line arrow in FIG. 13, the original material escapes to both sides in the width direction of the secondary original material roll. The conveyance direction deviation of the secondary continuous sheet in the width direction also occurs.

  Therefore, in the present invention, when a plurality of secondary continuous sheets are wound around the tube shaft, it is desirable that the feeding belt is a coaxial belt with separate belts in contact with each secondary continuous sheet. . By doing in this way, the force by each belt comes to the width direction of each secondary continuous sheet. That is, since each secondary continuous sheet escapes in the width direction of the entire secondary web roll and the center direction, the winding deviation in the width direction is improved.

  Here, in the present invention, since the feeding belt is arranged at the lower part of the secondary web roll, when the feeding direction of the secondary continuous sheet from the secondary web roll is the direction from the bottom to the top, the secondary continuous roll This is desirable because the sheet can be pulled out smoothly.

  According to the present invention as described above, it is possible to solve the problem of winding slip that has occurred in the manufacture of a chemical-coated tissue paper product in a multi-stand type interfolder, and to efficiently manufacture a chemical-coated tissue paper product. become.

It is the schematic which shows the manufacturing equipment and manufacturing method of a primary web roll. It is the schematic which shows the manufacturing equipment (ply machine) and manufacturing method of a secondary web roll. It is the schematic of a multi stand type inter folder. It is a figure for demonstrating delivery of the secondary continuous sheet from the secondary fabric roll of this invention. It is another figure for demonstrating delivery of the secondary continuous sheet from the secondary fabric roll of this invention. It is a perspective view for demonstrating a folding mechanism part. It is a perspective view which shows how to fold a secondary continuous sheet. It is a perspective view which shows how to fold a secondary continuous sheet. It is a perspective view which shows how to fold a secondary continuous sheet. It is a bundle sectional view showing how to fold a secondary continuous sheet. It is explanatory drawing of a storage process. It is a figure for demonstrating delivery of the secondary continuous sheet from the conventional secondary fabric roll. It is another figure for demonstrating delivery of the secondary continuous sheet from the conventional secondary original fabric roll.

Hereinafter, a manufacturing mode example of a chemical-coated type tissue paper product according to the present invention and a chemical-coated secondary raw roll unit of the present invention will be described in detail with reference to the drawings.
[Paper making process [Production method and equipment for primary roll]]
In order to preferably produce the secondary raw roll to which the chemical solution used in the present invention is applied, the primary raw roll JR (also referred to as a jumbo roll) is made as follows according to the papermaking equipment example X1 shown in FIG. To manufacture.

  First, a paper stock prepared by adding an appropriate chemical to the pulp slurry from the head box 31 is supplied onto the wire 32w of the wire part 32 to form the wet paper W (forming process). After being transferred to the felt 34 of the press part 33, it is sandwiched and dehydrated by the paired dewatering rolls 34 and 35 (dewatering step).

  Next, the dehydrated wet paper is attached to the surface of the Yankee dryer 36 and dried, and then scraped off by the doctor blade 37 to obtain a dry base paper S1 (primary continuous sheet described later) having a crepe (drying step).

  The dry base paper S1 is wound by the winding means 38 having the winding drum 39 so that the back surface of the dry base paper S1 faces the axial side of the primary raw roll JR (so that it becomes the winding inner surface). Take the primary roll roll JR (primary roll take-up step).

  The primary web roll JR differs depending on the performance of the papermaking equipment X1, but generally has a diameter of 1000 to 5000 mm, a length (width) of 1500 to 9200 mm, and a winding length of 5000 to 80000 m.

  In addition, a calendar process (not shown) may be provided on the dry base paper S1 that has been scraped off by the doctor blade 37 before the primary web winding process to smooth the front and back surfaces.

  Here, the back surface of the dry base paper S1 means a surface opposite to the surface that is in contact with the cylinder of the Yankee dryer 36. Although depending on the presence or absence of the calendar process, the surface in contact with the mirror Yankee dryer is generally smoother and has better surface properties.

  The primary continuous sheet S1 has a crepe rate of 10 to 30%, preferably 12 to 25%, more preferably 13 to 20%. When the crepe rate is less than 10%, the paper is easy to break during subsequent processing, and the tissue paper does not stretch and has little elongation. On the other hand, if the crepe rate is more than 30%, it is difficult to control the tension of the sheet at the time of processing, and it becomes easy to break the paper.

  Moreover, in making the primary continuous sheet S1, the paper strength of the product can be adjusted by a known method so as to have an appropriate value. For example, a dry paper strength enhancer is internally added to the stock or wet paper, the freeness of the stock is reduced (for example, reduced by about 30 to 40 ml), and the NBKP blending ratio of the raw pulp is increased (for example, 50% or more). The known methods such as these can be combined as appropriate.

  As the dry paper strength agent, starch, polyacrylamide, CMC (carboxymethyl cellulose) or a salt thereof such as sodium carboxymethyl cellulose, carboxymethyl cellulose calcium, carboxymethyl cellulose zinc and the like can be used. As the wet paper strength agent, polyamide polyamine epichlorohydrin resin, urea resin, acid colloid / melamine resin, thermal crosslinkability imparting PAM and the like can be used.

  When the wet paper strength agent is internally added, the addition amount can be about 5 to 20 kg / t in weight ratio to the pulp slurry. In addition, when the dry paper strength agent is internally added, the addition amount can be about 0.5 to 1.0 kg / t by weight ratio to the pulp slurry.

[Production example of secondary roll with chemicals applied]
The secondary web roll according to the present invention transfers the primary web roll manufactured in the above-mentioned papermaking process to an appropriate chemical solution coating facility, where a chemical solution is applied to form a chemical solution coated primary raw roll, and this chemical solution The primary continuous sheet of the chemical solution is unwound from the primary roll of coating, and the secondary sheet is wound around several tube shafts as appropriate by slitting the tissue paper suitable for the multi-stand type interfolder to the same width or multiple times. It can be a raw fabric roll.

  Also, without producing the chemical primary roll, the primary continuous sheet is unwound from the primary roll, the chemical is applied to the primary continuous sheet, and slit into a width suitable for a multi-stand type interfolder. A secondary material roll can be obtained by winding it around several tube shafts.

  Furthermore, before winding on a primary web roll in the above-mentioned papermaking process, a chemical solution may be applied, and this may be slit to form a secondary web roll without going through the primary web roll.

  As described above, the chemical solution-coated secondary raw roll in the present invention is formed by winding a continuous sheet coated with a chemical solution to a width suitable for a multi-stand type interfolder and winding it around one tube shaft. Means things.

  For the application of the chemical solution, known chemical solution application means such as flexographic printing, spray coating, and ink jet printing can be employed. Flexographic printing is suitable because of requirements such as flexibility of printing plates, high-speed compatibility, prevention of chemical solution scattering, and ease of adjustment of coating amount. Furthermore, since the press roll or the like is not brought into contact with the paper surface, the reduction in the paper thickness is not caused. Therefore, the spray coating, which is a non-contact type application form that directly applies the chemical solution to the paper surface without using the press plate roll or the like. Work and ink jet printing are suitable.

  Here, tissue paper products usually have a structure in which a plurality of crepe papers such as 2 plies and 3 plies are laminated to each other, and after the primary continuous sheet is unwound from a plurality of primary raw rolls and laminated. In general, the laminated continuous sheet is wound into a secondary raw roll. And the process of slitting to the width suitable for such laminating processing and multi-stand type interfolder, and the process of winding around the tube shaft with the appropriate number of sheets are generally carried out with equipment called a ply machine. .

  In addition, the ply machine is originally a facility that can move at high speeds and can produce multiple secondary rolls for multi-stand type interfolders at the same time, thus meeting the production speed of highly productive multi-stand type interfolders. It is extremely useful in terms of productivity to produce a secondary liquid roll that can produce a secondary raw roll, and to apply a chemical with a ply machine.

  Therefore, it is particularly preferable in the present invention to produce a secondary raw roll coated with a chemical solution by a ply machine. This production example will be described in detail below.

[Production example of secondary material roll coated with chemicals in ply machine]
In the ply machine X2, as shown in FIG. 2, the required number (two in FIG. 2) of the primary rolls JR produced in the paper making process is set, and the primary continuous rolls fed out from the primary rolls JR and JR. Process for laminating sheets (S11, S12 in the illustrated example), chemical liquid application process for applying chemical liquid, calendar process for calendering, contact embossing process for integrating laminated sheets, tissue paper width suitable for multi-stand type interfolder A slit process for slitting the sheet and a winding process for winding the slit sheet around the tube shaft in an appropriate number of sheets are continuously performed. The calendar process and the contact embossing process are not essential.

  The step of laminating the primary continuous sheet is performed by an overlapping portion 51 such as a known nip roll. That is, each primary continuous sheet S11, S12 unwound from each primary raw roll JR, JR is superposed along the continuous direction and then nipped in a laminated state.

  Here, in the illustrated example, the surfaces of the primary continuous sheets S11 and S12 fed out from the primary raw rolls JR and JR are respectively the surfaces of the laminated continuous sheets S3 after being overlaid (here, “surface” of the laminated continuous sheets). Is the front and back surfaces that are the outer surfaces of the stack). You may comprise so that the back surface of primary continuous sheet S11, S12 may become the surface of lamination | stacking continuous sheet S3, respectively, either one back surface of primary continuous sheet S11, S12 may become the surface of lamination | stacking continuous sheet S3, and the other surface May be the surface of the laminated continuous sheet S3, but the surface of the primary raw sheet S11, S12 is in contact with the surface of the Yankee dryer during drying, so there is less fuzz compared to the back surface and it is smooth and soft to the touch Therefore, it is desirable that the surface of the primary continuous sheet (dry base paper S1) forms the front and back surfaces of the laminated continuous sheet S3.

  The chemical solution application step can be performed at an appropriate position of the ply machine X2, but preferably, a chemical solution application means 53 is provided after the overlapping portion 51 to continuously apply the chemical solution to the laminated continuous sheet S3. . This is the form in the illustrated example. As described above, the chemical solution can be applied by using known chemical solution application means such as flexographic printing, spray coating, and ink jet printing. One or a plurality of chemical solution applying means 53 can be installed, and in the case of installing a plurality of chemical solution applying means 53, they may be arranged in parallel in the horizontal direction, the up-down direction, or the oblique direction, and are arranged by combining these installation directions including the horizontal direction. You may do it. Since the holding angle can be reduced by arranging them in the horizontal direction, the processing speed can be increased, and when they are arranged in the vertical direction, the installation space in the horizontal direction can be reduced. In the illustrated example, two doctor chamber type flexographic printing machines 53A and 53B are provided in order to apply a chemical solution to both surfaces of the laminated continuous sheet S3.

  The calendering process improves the surface smoothness by known calendering means. In the illustrated example, two calendar means 52, 52 are provided. Note that calendar processing is not necessarily performed.

  The contact embossing step is a step of applying contact embossing so as to make it difficult to separate the plies of the two primary continuous sheets S11 and S12 constituting the laminated continuous sheet S3. The contact embossing means is indicated by reference numeral 54 in FIG.

  The slitting process is a process of slitting the laminated continuous sheet S3 in the continuous direction to make the width of the tissue paper product. The slit processing can be performed by the slit means 55 including a plurality of roll cutters and receiving portions arranged side by side with a width of the tissue paper in the width direction (direction perpendicular to the flow direction) of the laminated continuous sheet S3.

  At the subsequent stage of the chemical solution applying means 53, there is provided a winding means 56 for winding the laminated continuous sheet S3 into the chemical solution applying secondary raw roll 100. The winding means 56 has a pair of winding drums for winding the laminated continuous sheet S3 coated with a chemical solution around the tube shaft while guiding the continuous sheet S3 to the winding means 56. These two winding drums 56A, 56A are in contact with the outer peripheral surface of the chemical solution-coated secondary raw roll R and guide the laminated continuous sheet S3 coated with the chemical solution, and assist the winding of the tube shaft.

  In the manufacturing equipment X2 or the manufacturing method of the secondary web roll 100 according to this embodiment, the processing speed is 100 to 1100 m / min, preferably 350 to 1050 m / min, more preferably 450 to 1000 m / min. Due to the relationship with the productivity of the multi-stand type interfolder, if it is less than 100 m / min, it cannot be said that the productivity is sufficient and it is difficult to obtain the effect of the present invention. On the other hand, if it exceeds 1100 m / min, stable production becomes difficult.

[Configuration of secondary roll and secondary continuous sheet]
Here, when this invention is a secondary original fabric roll and a secondary continuous sheet shown below, the remarkable winding-up prevention effect is exhibited.
The secondary web roll in which the effect of the present invention is remarkable is a roll of secondary continuous sheet of 10,000 to 25000 m, a diameter of 900 to 25000 mm, and a tube shaft diameter of 50 to 300 mm. The width is not limited in the present invention because it depends on the number of secondary continuous sheets wound around one tube shaft.

The basis weight of each successive sheet constituting the secondary continuous sheet has a basis weight by JIS P 8124 is, 10 to 25 g / m ^2, preferably 11~20g / m ^2, more preferably 12~16g / m ² It is. The secondary continuous sheet according to the present invention is processed into tissue paper later, and has a basis weight equivalent to that of the tissue paper constituting the final product. When the basis weight is less than 10 g / m ² , it is preferable in terms of the softness of the tissue paper, but it is difficult to ensure an appropriate strength. On the other hand, if the basis weight exceeds 25 g / m ² , the tissue paper becomes too hard and the touch is deteriorated. The paper thickness (measured with a Peacock manufactured by Ozaki Seisakusho) is 80 to 250 μm, preferably 100 to 200 μm, more preferably 130 to 180 μm.

  The secondary continuous sheet has a dry tensile strength (hereinafter also referred to as dry paper strength) defined in JIS P 8113 having a longitudinal direction of 200 to 700 cN / 25 mm, preferably 250 to 600 cN / 25 mm with 2 plies. The lateral direction is preferably 300 to 600 cN / 25 mm, and the lateral direction is 100 to 300 cN / 25 mm, preferably 130 to 270 cN / 25 mm, particularly preferably 150 to 250 cN / 25 mm. If the dry tensile strength is too low, troubles such as paper breakage and elongation at the time of production and use are likely to occur, and if it is too high, the touch becomes stiff during use.

The secondary continuous sheet has a chemical coating amount of 0.3 to 5.0 g / m ² , preferably 1.0 to 4.0 g / m ² . Note that if it exceeds 3.9 g / m ² , there may be a case where the paper is cut or the sticky feeling is too high due to a decrease in paper strength or elongation. If it is less than 0.3 g / m ² , the quality difference from the uncoated product such as smoothness and moistness cannot be felt. Moreover, when it is in this range, the effect of preventing winding deviation becomes remarkable.

  In the secondary continuous sheet, the applied chemical solution is an aqueous lotion agent, particularly contains a polyol, more preferably contains 70 to 90% polyol and 1 to 15% moisture, particularly preferably further contains It contains 0.01 to 22% of functional chemicals. Such an aqueous chemical solution has an action of extending the crepe, and the effect of the present invention becomes remarkable.

  The polyol includes polyhydric alcohols such as glycerin, diglycerin, propylene glycol, 1,3-butylene glycol, polyethylene glycol, and derivatives thereof, and saccharides such as sorbitol, glucose, xylitol, maltose, maltitol, mannitol, and trehalose. .

  Functional agents include softeners, surfactants, inorganic and organic fine particle powders, oily components, and the like. Softeners and surfactants have the effect of imparting flexibility to the tissue and smoothing the surface, and anionic surfactants, cationic surfactants and zwitterionic surfactants are applied. Inorganic and organic fine particle powders have a smooth surface. The oil component has a function of improving lubricity, and higher alcohols such as liquid paraffin, cetanol, stearyl alcohol, and oleyl alcohol can be used.

  In addition, as a functional agent, one or more of a hydrophilic polymer gelling agent, collagen, hydrolyzed collagen, hydrolyzed keratin, hydrolyzed silk, hyaluronic acid or a salt thereof, ceramide, etc. are optionally selected as agents that maintain the moisture retention of polyol. A moisturizer such as a combination of the above can be added.

  Deodorants such as flavors, emollients such as various natural extracts, vitamins, emulsifiers that stabilize compounding ingredients, antifoaming agents, antifungal agents, organic acids, etc. An agent can be appropriately blended. Furthermore, you may contain the antioxidant of vitamin C and vitamin E.

  Among the above components, when the main component is a polyhydric alcohol such as glycerin or propylene glycol, it is preferable from the viewpoint of application in terms of stabilizing the viscosity and application amount of the chemical solution.

  On the other hand, the secondary continuous sheet has pulp paper as a main material. The pulp fiber type is not particularly limited, and an appropriate raw material pulp used for this type of tissue paper can be selected and used. Specific examples include wood pulp, non-wood pulp, synthetic pulp, waste paper pulp, and more specifically, ground wood pulp (GP), stone ground pulp (SGP), refiner ground pulp (RGP), pressurized ground wood pulp. (PGW), thermomechanical pulp (TMP), chemithermomechanical pulp (CTMP), bleached chemithermomechanical pulp (BCTMP) and other mechanical pulp (MP), chemical mechanical pulp (CGP), semi-chemical pulp (SCP) Kraft pulp (KP) such as hardwood bleached kraft pulp (LBKP), softwood bleached kraft pulp (NBKP), chemical pulp (CP) such as soda pulp (AP), sulfite pulp (SP), dissolved pulp (DP) , Nylon, rayon, polyester, polyvinyl alcohol (PVA) Synthetic pulp made from coconut, deinked pulp (DIP), waste paper pulp such as waist pulp (WP), ground pulp (TP), cotton, flax, hemp, jute, manila hemp, ramie etc. One or several kinds of pulp, esparto pulp, bagasse pulp, bamboo pulp, sesame pulp such as kenaf pulp, auxiliary pulp such as bast pulp, and the like can be appropriately selected and used.

  In particular, the pulp fiber is preferably composed of NBKP and LBKP. Waste paper pulp may be blended as appropriate, but it is compatible with aqueous chemicals, desirable in the production method of the present invention that is folded after application, and desirable in terms of the texture of the tissue paper to be obtained. It is preferable that it is composed only of LBKP. In this case, the blending ratio (JIS P 8120) is preferably NBKP: LBKP = 20: 80 to 80:20, and particularly preferably NBKP: LBKP = 30: 70 to 60:40.

[Support of secondary web roll and delivery of secondary continuous sheet]
As shown in FIGS. 3 to 8 and the like, the secondary fabric roll 100 to which the chemical solution manufactured by the above manufacturing example is applied flows through the folding mechanism unit 70 having a pair of folding plates 72 and 72. A multi-stand type interfolder X3 having a structure in which a large number (usually 80 to 120 groups) are juxtaposed in the direction is moved, and is rotatably attached to the original roll support portion 71 corresponding to each folding mechanism portion. Secondary continuous sheets S4a and S4b are fed out from the secondary web roll 100.

  In this embodiment, the original fabric roll support portion 71 is at the tip of an arm-shaped support member 80 as shown in FIG. 4 and the like, and the secondary original fabric roll 100 is a known jig 150 also called a core plug. Can be pivotally attached. The support member 80 is configured such that a tip end side of the support portion of the secondary raw roll 100 is vertically swung with a predetermined position as a fulcrum, and the secondary raw roll 100 attached along with the swing is provided. Go up and down.

  On the other hand, a plurality of rotatable rotating rolls 81 </ b> A to 81 </ b> D having the same axial direction as that of the secondary raw roll 100 are arranged at a lower position of the secondary raw roll 100 of the support member 80. A feeding belt 83 which is an endless belt is wound around the belt. The secondary roll 100 is lowered by the swing mechanism of the support member 80 due to its weight and the like while being attached to the support member 80, and is always placed on the feeding belt 83 via the outer peripheral surface 100A. Is done.

  In the form shown in the figure, the feeding belt 83 is one 81 </ b> A at the front (feeding direction side) of the secondary web roll 100, and one at the rear of the secondary web roll 100 with the axis of the secondary web roll 100 interposed therebetween. 81B has a portion that is cross-linked to the rotating rolls 81A and 81B in two places in total, and the secondary original roll 100 fits between the rotating rolls 81A and 81B so that a large predetermined amount is provided on the feeding belt 83. It is placed with a hugging angle. Here, the holding angle ∠A in this embodiment is 50 to 180 °, and it is preferable to be within this range. More preferably, it is 70-160 degrees.

  On the other hand, in this embodiment, as a preferred embodiment, an urging cylinder 85 such as a hydraulic or pneumatic cylinder is connected to the base end side of the support member 83, and the secondary raw material roll 100 is operated by this cylinder 85. A force is applied in the direction of lifting the front end side of the support member 83 to which is attached. As a result, the load applied to the feeding belt 83 by the secondary material roll 100 is reduced. The degree of urging can be appropriately changed according to the size and weight of the secondary raw roll 100, the weight of the support member, and the like. Of course, it should not be an excessive urging force that prevents the secondary raw roll from being raised and placed on the feeding belt 83 with the secondary original roll 100 attached.

  On the other hand, the secondary web roll 100 according to the present embodiment is obtained by winding two secondary continuous sheets S4a and S4b around one tube shaft, which is also referred to as 2 wide, and the feeding belt 83 includes In order to correspond, as understood from FIG. 5 which is also a view taken in the direction of the arrow V in FIG. 4, as an aspect in which separate belts 83 a and 83 b are arranged so as to be in contact with the peripheral surfaces of the respective secondary continuous sheets S4 a and S4 b. Yes. These belts 83a and 83b are wound around rotating rollers 81A to 81D having the same rotating shaft as can be understood from the figure, and are simultaneously moved along with the rotation of the rotating rollers 81A to 81D. There is no difference between the feeding speeds of the secondary continuous sheets S4a and S4b. Further, the belts 83a and 83b are spaced apart from each other between the secondary continuous sheets S4a and S4b, and as a result, the secondary belts 83a and 83b that are not in direct contact with each other as shown by the dotted arrows in FIG. The side portions of the continuous sheets 4Sa and 4Sb have substantially the same direction of force escape, so that each secondary continuous sheet is continuously applied with a force in the constant direction in the width direction so that it does not move.

  In addition, when the width of the feeding belt 83 (83a, 83b) is about 40 to 80% of the width (tissue paper product width) of the secondary continuous sheet S4a (S4b), the secondary original fabric is coupled with the holding angle. The contact area with the roll outer peripheral surface 100A is in a suitable range, and the effect of preventing winding is ensured.

  In the present embodiment, the secondary continuous sheets S4a and S4b are unwound from the secondary original roll 100 under such a characteristic support manner of the secondary original roll 100. The feeding is performed by transporting the feeding belt 83 by rotational driving of the rotary rolls 81A to 81D by a driving source (not shown).

  The conveying speed of the feeding belt 83 is a speed corresponding to the conveying speed of the subsequent continuous sheet bundle 10C of the folding mechanism sections 70, 70. The conveying speed of the continuous sheet bundle 10C is 50 to 120 m / min.

[Folding process in multi-stand type inter folder]
Next, folding of the secondary continuous sheets S4a and S4b unwound from the secondary raw roll 100 will be described. The secondary continuous sheets S4a and S4b having two tissue paper widths unwound from the secondary raw roll 100 are supplied to the folding mechanism unit 70 and folded. Folding at the folding mechanism is understood in particular from FIGS. 3, 4, and 9 to 14. The folding mechanism unit 70 includes a pair of folding plates 72, and secondary continuous sheets S <b> 4 a and S <b> 4 b are sent to the folding plates 72 and 72 via the guide roller 74 and the guide round bar member 75. Below each folding plate 72, 72 is located a continuous tissue paper bundle 10C that is stacked while being folded by a folding mechanism portion 70 on the upstream side of the folding plate 72, and the folding tissue portion 10C is placed on the continuous tissue paper bundle 10C. The chemical solution application secondary continuous sheets S4a and S4b folded at 70 are associated and stacked. These continuous tissue paper bundles 10C are configured to be sequentially sent downstream by a conveyor. That is, the number of continuous tissue paper bundles 10C is increased as the folding mechanism unit 70 located upstream is moved to the folding mechanism unit 70 located downstream. In addition, the folding mechanism part 70 using this kind of folding plate 72,72 ... is a mechanism well-known by US Patent 4052048 patent specification etc., for example.

  Further, the folding in the folding mechanism unit 70 will be described in detail. The secondary continuous sheets S4a and S4b supplied to the folding mechanism unit 70 are folded in a Z shape and are adjacent to the adjacent secondary continuous sheets S4a and S4b. Stack the side edges together. At this time, in the folding mechanism portion 70, the secondary continuous sheets S4a and S4b are guided to the respective folding plates 72 and 72. At this time, the secondary continuous sheets S4a and S4b are guided round bar members 75 and 75, respectively. Therefore, the side end portions are guided while being shifted in position so as not to overlap each other.

  A continuous secondary continuous sheet that overlaps the lower side when guided to the folding plates 72, 72 is a first secondary continuous sheet S4a, and a secondary continuous sheet that overlaps the upper side is a second secondary continuous sheet. Assuming that the sheet S4b, these secondary continuous sheets have a side end e1 that does not overlap the second secondary continuous sheet S4b of the first secondary continuous sheet S4a by the side plate 72e of the folding plate 72, and the second secondary continuous sheet S4b. A side end e2 of the second secondary continuous sheet S4b that does not overlap with the first secondary continuous sheet S4a is folded from the slit 72s of the folding plate 72 below the folded plate while being folded back to the upper side of the secondary continuous sheet S4b. It is folded back as if it was pulled in.

  At this time, the side end e3 (e1) of the secondary continuous sheet S4a stacked while being folded on the upstream folding plate is guided between the folded portions of the second secondary continuous sheet from the slit of the folding plate.

  In this way, each secondary continuous sheet is folded into a Z-shape and the side ends of adjacent secondary continuous sheets are overlapped with each other.

  As described above, the chemical-containing continuous tissue paper bundle 10C formed by being folded and folded by the respective folding plate mechanism portions 70, 70... Is a rear stage cutter of the most downstream folding plate mechanism portion 70 as shown in FIG. In the section 160, the tissue paper bundle 10 is cut (cut) at a predetermined interval in the flow direction. Here, the processing speed in the cutter unit 160 is 50 to 120 m / min, and in the present invention, the secondary continuous sheet from the secondary original roll 100 set on the original roll support 71 by the processing speed of the cutter concerned. The feeding speed of S4a and S4b is determined. And this speed is slow compared with the above-mentioned papermaking equipment X1 and ply machine X2. And even if it is late, it exhibits sufficiently high productivity.

  This is because the multi-stand type interfolder X3 usually has 80 to 120 folding mechanisms, and the total width of the secondary roll used here is made by the paper making equipment X1 or the ply machine X2. -It is because it becomes about 10 to 30 times the processed secondary raw roll. That is, in the multi-stand type interfolder X3, the consumption speed of the secondary material roll is high even if the processing speed is low.

[Storing tissue paper bundles in storage boxes]
Next, an example of storing the tissue paper bundle 10 formed in the multi-stand type interfolder X3 in the storage box 2 will be described. The method for storing the tissue paper bundle 10 in the storage box is not limited to this example, and a known method can be adopted.

  The tissue paper bundle 10 cut and formed by the cutting step is stored in the storage box 2 as shown in FIGS. 3 and 11 in a storage facility continuing to the rear stage of the multi-stand type interfolder X3.

  Specifically, a storage box having the above-described top surface, bottom surface and side surfaces connecting these, and bottom surface side end surface pieces 23B, side surface end surface pieces 23S, and top surface side end surface pieces 23U connected to both side edges in the longitudinal direction of each surface. Is assembled in a semi-finished state in which the bottom end piece 23B, the side end piece 23S, and the top end piece 23U are open, that is, the end face is opened, and is multi-stand type so as to face the opening. The cut surface of the tissue paper bundle 10 sent from the interfolder X3 is attached.

And if it attaches together, the tissue paper bundle 10 will be pushed in in a storage box by a push rod etc. When the tissue paper bundle 10 is pushed into the storage box, the side surface end piece 23S is folded back to the inner surface side of the box, and then the upper surface side end surface piece 23U and the bottom surface side end surface piece 23B are folded to overlap each other. The contact portion is bonded with a hot melt adhesive or the like.
This bonding completes the production of the tissue paper product of the present invention.

  In the multi-stand type interfolder X3, the continuous tissue paper bundle 10C has a flow direction in the vertical direction (MD direction) and a horizontal direction (CD direction) along a direction orthogonal to the flow direction. For this reason, the direction of the paper of the tissue paper constituting the tissue paper bundle 10 obtained by cutting the continuous tissue paper bundle 10C into a predetermined length is along the extending direction of the folded portion of the tissue paper as shown in the drawing. The vertical direction (MD direction) and the horizontal direction (CD direction) along the direction perpendicular to the extending direction of the folded portion of the tissue paper.

  Therefore, when the tissue paper product manufactured by the present invention stored in the storage box as described above is pulled out from the storage box, the pull-out direction is along the lateral direction (CD direction) of the tissue paper. It has become.

  X1 ... papermaking equipment, JR ... primary web roll (jumbo roll), W ... wet paper, S1 ... dry base paper (primary continuous sheet), 31 ... head box, 32 ... wire part, 32w ... wire, 333 ... press part, 33F ... felt, 34, 35 ... dewatering roll, 36 ... Yankee dryer, 36C ... Yankee dryer hood, 37 ... doctor blade, 38 ... winding means, 39 ... winding drum, X2 ... ply machine, S11, S12 ... primary continuous sheet , S3 ... laminated continuous sheet, 51 ... overlapped portion, 53 ... chemical solution applying means, 54 ... contact embossing means, 55 ... slitting means, 56 ... winding means, 100 ... secondary raw roll, 100A ... outer peripheral surface, 150 ... Core plug, X3 ... Multi-stand type interfolder, S4a, S4b ... Secondary ream Sheet 70: Folding mechanism part 71 ... Original fabric roll support part 72 ... Folding plate 73, 74 ... Guide roller 75 ... Guide round bar member 10C ... Continuous tissue paper bundle 80 ... Support member 81A-81D ... Rotating roller, 83, 83a, 83b ... Feeding belt.

Claims (5)

Tissue paper product having a step of feeding the secondary continuous sheet from a secondary web roll formed by winding a secondary continuous sheet coated with a chemical solution around a tube shaft and supplying the secondary continuous sheet to a folding mechanism of a multi-stand type interfolder A manufacturing method of
The secondary material roll is supported on a support member having an urging function in the ascending direction so as to be movable up and down,
A feeding belt is arranged below the outer peripheral surface of the secondary web roll so that the secondary web roll is always placed on the feeding belt via the outer circumferential surface, and is attached in the upward direction. In a state where the load applied to the feeding belt of the secondary raw roll is reduced by the support member having the urging function,
The secondary belt is rotated by driving the feeding belt, the secondary continuous sheet is fed from the outer peripheral surface of the secondary raw roll, and supplied to the folding mechanism.
A method for producing a tissue paper product.   The manufacturing method of the tissue paper product of Claim 1 which makes the holding angle with respect to the secondary raw material roll outer peripheral surface of a feeding belt 50-180 degrees.   When the secondary roll is a roll of a plurality of secondary continuous sheets wound around a tube axis, the feeding belt is a coaxial arrangement of separate belts in contact with each secondary continuous sheet, The manufacturing method of the tissue paper of Claim 1 or 2.   The method for producing a tissue paper product according to any one of claims 1 to 3, wherein a feeding direction of the secondary continuous sheet from the secondary web roll is a direction from the lower side to the upper side.   The feed belt is wound around the pair of rolls arranged before and after the secondary roll with tension, and the secondary roll is placed on the feed belt between the pair of rolls. The manufacturing method of the tissue paper product of description.

Images