Patent Grant
11859348
The present application is based on, and claims priority from JP Application Serial Number 2021-106445, filed Jun. 28, 2021, the disclosure of which is hereby incorporated by reference herein in its entirety.
The present disclosure relates to a fiber body manufacturing method.
In the related art, as described in JP-A-2015-168904, a sheet manufacturing apparatus including a first transport section having a first transport belt for transporting a web containing fibers; a second transport section having a second transport belt for transporting the web while suctioning the web in a direction away from the first transport belt; a pressure roller arranged downstream of the second transport section in a web transport direction to pressurize the web; and a heating roller arranged downstream of a pressurizing section in the web transport direction to heat the web, is known.
Further, JP-A-2015-168904 discloses that the web is sprayed with water to which starch or PVA (polyvinyl alcohol) is added.
However, in the above-described apparatus, when the web is sprayed with water to which starch or PVA (polyvinyl alcohol) is added, there is a problem that the web sticks to the pressure roller or the like due to the binding force of the starch or the like.
When the web sticks to the pressure roller or the like, the web may be poorly transported or the web may be damaged.
According to an aspect of the present disclosure, there is provided a fiber body manufacturing method in a fiber body manufacturing apparatus including an accumulating section that forms a web on a first transport belt, a transport section having a second transport belt for transporting the web, a water-applying section that applies water to the web, and a heating section that heats the web to which the water is applied, the method including an accumulating step of forming the web by accumulating a material containing fibers and starch or dextrin on the first transport belt by a dry method; a transport step of transporting the web by peeling off a first surface of the web from the first transport belt, and by bringing a second surface of the web, which is a surface opposite to the first surface peeled off from the first transport belt, into contact with the second transport belt; a water-applying step of applying the water to the web which is in contact with the first transport belt or the second transport belt; and a heating step of heating the web by bringing the heating section into contact with the web peeled off from the second transport belt, and forming a fiber body by binding the fibers with the starch or dextrin, in which the web peeled off from the second transport belt is directly supplied to the heating section.
First, the configuration of a fiber body manufacturing apparatus 100 will be described, and then the fiber body manufacturing method will be described.
The fiber body manufacturing apparatus 100 is an apparatus for manufacturing a sheet-like fiber body S. As illustrated in
The supply section 10 supplies the raw material to the crushing section 12. The supply section 10 is, for example, an automatic charging section for continuously charging the raw material into the crushing section 12. The raw material supplied by the supply section 10 is a material containing various fibers.
The fiber is not particularly limited, and a wide range of fiber materials can be used. Examples of the fiber include natural fiber (animal fiber, plant fiber) and chemical fiber (organic fiber, inorganic fiber, organic-inorganic composite fiber). More specifically, the fiber includes fibers made of cellulose, silk, wool, cotton, cannabis, kenaf, flax, ramie, jute, Manila hemp, sisal, coniferous tree, broadleaf tree, and the like, and these may be used alone, may be appropriately mixed and used, or may be used as a purified regenerated fiber.
Examples of the raw material of the fiber include pulp, used paper, and used cloth. Further, the fiber may be subjected to various surface treatments. Further, the material of the fiber may be a pure substance or a material containing a plurality of components such as impurities and other components. Further, as the fiber, a defibrated product obtained by defibrating used paper, pulp sheet, or the like by a dry method may be used.
The length of the fiber is not particularly limited, but in a case of one independent fiber, the length along the longitudinal direction of the fiber is 1 μm or more and 5 mm or less, preferably 2 μm or more and 3 mm or less, and more preferably 3 μm or more and 2 mm or less.
In the fiber body manufacturing apparatus 100, water is applied in the water-applying section 79, and thus the mechanical strength of a formed fiber body S can be increased by using a fiber having the ability to form hydrogen bonds. Examples of such fibers include cellulose.
The fiber content in the fiber body S is, for example, 50% by mass or more and 99.9% by mass or less, preferably 60% by mass or more and 99% by mass or less, and more preferably 70% by mass or more and 99% by mass or less. Such a content can be obtained by performing mixing when forming the mixture.
The crushing section 12 cuts the raw material supplied by the supply section 10 into strips in the air such as the atmosphere. The shape and size of the strips are, for example, several centimeter square. In the illustrated example, the crushing section 12 has a crushing blade 14, and the charged raw material can be cut by the crushing blade 14. As the crushing section 12, for example, a shredder is used. The raw material cut by the crushing section 12 is received by a hopper 1 and then transferred to the defibration section 20 through a pipe 2.
The defibration section 20 defibrates the raw material cut by the crushing section 12. Here, “defibrating” means unraveling a raw material obtained by binding a plurality of fibers into each fiber. The defibration section 20 also has a function of separating substances such as resin particles, ink, toner, and a blot inhibitor adhering to the raw material from the fibers.
A product that passed through the defibration section 20 is referred to as “defibrated product”. In addition to the unraveled defibrated fiber, the “defibrated product” may include resin particles separated from the fiber when the fiber is unraveled, coloring agents such as ink and toner, or additives such as blot inhibitors and paper strength enhancers. The shape of the unraveled defibrated product is a shape of a string. The unraveled defibrated product may exist in a state of not being entangled with other unraveled fibers, that is, in an independent state, or may exist in a state of being entangled with other unraveled defibrated products to form a mass shape, that is, in a state where a lump is formed.
The defibration section 20 performs defibration by a dry method. Here, the treatment of defibrating or the like in the air such as the atmosphere, not in the liquid, is referred to as a dry method. As the defibration section 20, for example, an impeller mill is used. The defibration section 20 has a function of suctioning the raw material and generating an airflow that discharges the defibrated product. Accordingly, the defibration section 20 can suction the raw material together with the airflow from an introduction port 22 by the airflow generated by itself, perform the defibration treatment, and transport the defibrated product to a discharge port 24. The defibrated product that passed through the defibration section 20 is transferred to the sorting section 40 through the pipe 3. As the airflow for transporting the defibrated product from the defibration section 20 to the sorting section 40, the airflow generated by the defibration section 20 may be used, or an airflow generating apparatus such as a blower may be provided to use this airflow.
The sorting section 40 introduces the defibrated product defibrated by the defibration section 20 from the introduction port 42 and sorts the defibrated product according to the length of the fibers. The sorting section 40 has, for example, a drum section 41 and a housing section 43 that accommodates the drum section 41 therein. As the drum section 41, for example, a sieve is used. The drum section 41 has a net, and can sort out fibers or particles smaller than the size of the mesh opening of the net, that is, a first sorted product passing through the net, and fibers, undefibrated pieces, and lumps larger than the size of the mesh opening of the net, that is, a second sorted product that does not pass through the net. For example, the first sorted product is transferred to the accumulating section 60 through a pipe 7. The second sorted product is returned from the discharge port 44 to the defibration section 20 through a pipe 8. Specifically, the drum section 41 is a cylindrical sieve that is rotationally driven by a motor. As the net of the drum section 41, for example, a wire net, an expanded metal obtained by stretching a metal plate having a cut, or a punching metal in which a hole is formed in the metal plate by a press machine or the like is used.
The first web forming section 45 transports the first sorted product that passed through the sorting section 40 to the pipe 7. The first web forming section 45 includes, for example, a mesh belt 46, a stretching roller 47, and a suction mechanism 48.
The suction mechanism 48 can suction the first sorted product dispersed in the air through the opening of the sorting section 40 onto the mesh belt 46. The first sorted product is accumulated on the moving mesh belt 46 to form a web V.
Passing products that passed through the opening of the sorting section 40 are accumulated on the mesh belt 46. The mesh belt 46 is stretched by the stretching roller 47, and is configured such that the passing products are unlikely to pass therethrough and air is allowed to pass therethrough. The mesh belt 46 moves as the stretching roller 47 revolves. While the mesh belt 46 moves continuously, the passing products that passed through the sorting section 40 are continuously piled up, and accordingly, the web V is formed on the mesh belt 46.
The suction mechanism 48 is provided below the mesh belt 46. The suction mechanism 48 can generate a downward airflow. By the suction mechanism 48, the passing products dispersed in the air by the sorting section 40 can be suctioned onto the mesh belt 46. Accordingly, the discharge speed from the sorting section 40 can be increased.
The web V is formed in a soft and swollen state containing a large amount of air by passing through the sorting section 40 and the first web forming section 45. The web V accumulated on the mesh belt 46 is charged into the pipe 7 and transported to the accumulating section 60.
The rotating body 49 can cut the web V. In the illustrated example, the rotating body 49 has a base portion 49a and a protrusion portion 49b protruding from the base portion 49a. The protrusion portion 49b has, for example, a plate-like shape. In the illustrated example, four protrusion portions 49b are provided, and four protrusion portions 49b are provided at equal intervals. By rotating the base portion 49a in a direction R, the protrusion portion 49b can rotate around the base portion 49a as an axis. By cutting the web V by the rotating body 49, for example, the fluctuation of the amount of the defibrated product per unit time supplied to the accumulating section 60 can be reduced.
The rotating body 49 is provided in the vicinity of the first web forming section 45. In the illustrated example, the rotating body 49 is provided in the vicinity of the stretching roller 47a positioned downstream in the path of the web V. The rotating body 49 is provided at a position where the protrusion portion 49b can come into contact with the web V and does not come into contact with the mesh belt 46 on which the web V is accumulated. Accordingly, it is possible to suppress abrasion of the mesh belt 46 by the protrusion portion 49b. The shortest distance between the protrusion portion 49b and the mesh belt 46 is, for example, 0.05 mm or more and 0.5 mm or less. This is the distance at which the mesh belt 46 can cut the web V without being damaged.
The mixing section 50 mixes, for example, the first sorted product that passed through the sorting section 40 and the binder. The mixing section 50 has, for example, a binder supply section 52 that supplies the binder, a pipe 54 for transporting the first sorted product and the binder, and a blower 56. In the illustrated example, the binder is supplied from the binder supply section 52 to the pipe 54 through the hopper 9. The pipe 54 is continuous with the pipe 7.
In the mixing section 50, an airflow is generated by the blower 56, and the first sorted product and the binder can be transported while being mixed in the pipe 54. The mechanism for mixing the first sorted product and the binder is not particularly limited, and may be agitated by a blade that rotates at high speed, or may use rotation of a container such as a V-type mixer.
As the binder supply section 52, a screw feeder, a disc feeder, or the like is used.
The binder supplied from the binder supply section 52 is starch or dextrin. Starch is a polymer in which a plurality of α-glucose molecules are polymerized by glycosidic bonds. The starch may be linear or may contain branches.
As the starch, those derived from various plants can be used. Raw materials for starch include grains such as corn, wheat, and rice, beans such as broad beans, mung beans, and red beans, tubers such as potatoes, sweet potatoes, and tapioca, wild grasses such as Erythronium japonicum, bracken, and kudzu, and palms such as sago palm.
Further, processed starch or modified starch may be used as the starch. Examples of the processed starch include acetylated adipic acid cross-linked starch, acetylated starch, oxidized starch, octenyl succinate starch sodium, hydroxypropyl starch, hydroxypropylated phosphoric acid cross-linked starch, phosphorylated starch, phosphoric acid esterified phosphoric acid cross-linked starch, urea phosphorylated esterified starch, sodium starch glycolate, and high amylose corn starch. Further, as the dextrin that serves as the modified starch, those obtained by processing or modifying the starch can be preferably used.
In the fiber body manufacturing apparatus 100, by using starch or dextrin, at least one of gelatinization and hydrogen bonds between the fibers occurs by being pressurized and heated after water is applied, and the fiber body S can be given sufficient strength.
The content of starch or dextrin in the fiber body S is, for example, 0.1% by mass or more and 50% by mass or less, preferably 1% by mass or more and 40% by mass or less, and more preferably 1% by mass or more and 30% by mass or less. Such a content can be obtained by performing mixing when forming the mixture.
In addition, in the binder supply section 52, in addition to the binder, in accordance with the type of the fiber body S to be manufactured, a colorant for coloring the fibers, a coagulation inhibitor for suppressing coagulation of fibers or coagulation of binder, a flame retardant for making fibers and the like unlikely to burn, and the like, may be included. The mixture that passed through the mixing section 50 is transferred to the accumulating section 60 through the pipe 54.
The accumulating section 60 introduces the mixture that passed through the mixing section 50 from an introduction port 62, unravels the entangled defibrated product, and disperses the unraveled defibrated product in the air to make the product fall. Accordingly, the accumulating section 60 can uniformly accumulate the mixture (a material containing the fibers and the binder) on the second web forming section 70.
The accumulating section 60 has, for example, a drum section 61 and a housing section 63 that accommodates the drum section 61 therein. As the drum section 61, a rotating cylindrical sieve is used. The drum section 61 has a net and makes fibers or particles smaller than the size of the mesh opening of the net, which are contained in the mixture that passed through the mixing section 50, fall. The configuration of the drum section 61 is, for example, the same as the configuration of the drum section 41.
The “sieve” of the drum section 61 may not have a function of sorting a specific object. In other words, the “sieve” used as the drum section 61 means a sieve provided with a net, and the drum section 61 may make all of the mixture introduced into the drum section 61 fall.
The second web forming section 70 accumulates the passing products that passed through the accumulating section 60 to form the web W. The second web forming section 70 includes, for example, a first mesh belt 72 that serves as a first transport belt, a stretching roller 74, and a suction mechanism 76.
Passing products that passed through the opening of the accumulating section 60 are accumulated on the first mesh belt 72. The first mesh belt 72 is stretched by the stretching roller 74, and is configured such that the passing products are unlikely to pass therethrough and air is allowed to pass therethrough. The first mesh belt 72 moves as the stretching roller 74 revolves. While the first mesh belt 72 moves continuously, the passing products that passed through the accumulating section 60 are continuously piled up, and accordingly, the web W is formed on the first mesh belt 72.
The suction mechanism 76 is provided below the first mesh belt 72. The suction mechanism 76 can generate a downward airflow. By the suction mechanism 76, the mixture dispersed in the air by the accumulating section 60 can be suctioned onto the first mesh belt 72. Accordingly, the discharge speed from the accumulating section 60 can be increased. Furthermore, the suction mechanism 76 can form a downflow in the falling path of the mixture, and can prevent the defibrated product and the binder from being entangled during the fall.
As described above, the web W in a soft and swollen state containing a large amount of air is formed by passing through the accumulating section 60 and the second web forming section 70.
The transport section 78 is arranged downstream of the first mesh belt 72 in the transport direction of the web W. The transport section 78 peels off the web W on the first mesh belt 72 from the first mesh belt 72 and transports the web W toward the heating section 80. As illustrated in
Accordingly, a first surface Wa of the web W is peeled off from the first mesh belt 72, and a second surface Wb which is a surface opposite to the first surface Wa peeled off from the first mesh belt 72 can be adsorbed to the second mesh belt 78a. The web W adsorbed to the second mesh belt 78a is transported in a state of being in contact with the second mesh belt 78a.
The water-applying section 79 is arranged downstream of the accumulating section 60. The water-applying section 79 applies water to the web W which is in contact with the first mesh belt 72 or the second mesh belt 78a.
The water-applying section 79 of the present embodiment is arranged below the transport section 78, and applies water to the web W which is in contact with the second mesh belt 78a. Specifically, the water-applying section 79 applies water toward the first surface Wa of the web W which is in contact with the second mesh belt 78a. In other words, in the present embodiment, water is applied from below the web W toward the first surface Wa. In the water-applying section 79, as the water, for example, water vapor or mist is applied to the web W. Accordingly, water can be uniformly applied to the web W.
The water-applying section 79 of the present embodiment includes a container 79a capable of storing water and a piezoelectric vibrator 79b arranged at the bottom portion of the container 79a. The upper portion of the container 79a is opened, and the container 79a is arranged such that the opening faces the first surface Wa side of the web W. By driving the piezoelectric vibrator 79b, ultrasonic waves are generated in the water and mist is generated in the container 79a. The generated mist is supplied to the web W through the opening of the container 79a. By applying water from below the web W, water droplets do not fall on the web W even when dew condensation is generated in the water-applying section 79 or in the vicinity thereof.
Further, the suction mechanism 78c of the transport section 78 is arranged at a position facing the water-applying section 79 with the second mesh belt 78a interposed therebetween. Accordingly, the airflow containing water generated in the water-applying section 79 by the suction mechanism 78c can pass through the inside of the web W and apply water to the inside of the web W. In other words, the suction mechanism 78c is arranged so as to face a part of the first mesh belt 72 of the second web forming section 70 and the container 79a of the water-applying section 79. Accordingly, the common suction mechanism 78c has a function of peeling off the web W from the first mesh belt 72 and adsorbing the web W to the second mesh belt 78a and a function of applying water to the inside of the web W. Therefore, the configuration of the fiber body manufacturing apparatus 100 can be simplified.
In the present embodiment, water is applied from the first surface Wa side opposite to the second surface Wb of the web W which is in contact with the second mesh belt 78a, and thus the second surface Wb side can be transported with a weaker adhesive force than the first surface Wa side. Therefore, it is possible to suppress the sticking of the web W, to which the water is applied, to the second mesh belt 78a.
Further, the water applied from the water-applying section 79 does not contain starch or dextrin. Therefore, the web W can be transported in a state where the binding force of starch or the like is not sufficiently expressed, and the sticking of the web W to a member such as the second mesh belt 78a can be suppressed.
The water content of the web W to which water was applied in the water-applying section 79 is 12% by mass or more and 40% by mass or less. With the specified web water content, hydrogen bonds between fibers can be effectively formed and the strength of the fiber body S can be increased. Further, the specified web water content can suppress the sticking of the web W to the second mesh belt 78a. Further, by specifying the water content of the web W to be 40% by mass or less, the amount of water used can be reduced.
Furthermore, even in a case of the web W containing a binder (starch or dextrin), the sticking to the second mesh belt 78a is suppressed, the binding force between the fibers is increased, and the strength of the fiber body S can be increased.
The heating section 80 is arranged downstream of the transport section 78 and the water-applying section 79. The web W to which the water is applied is transported to the heating section 80.
The heating section 80 heats the web W to which the water is applied and which is peeled off from the second mesh belt 78a. The heating section 80 of the present embodiment simultaneously pressurizes and heats the web W to which water is applied. Accordingly, the water contained in the web W evaporates after the temperature rises, and the thickness of the web W becomes thin to increase the fiber density. The temperature of the water and the binder (starch or dextrin) rises due to heat, the fiber density increases due to the pressure, and accordingly, the binder is gelatinized, and then the water evaporates to bind the plurality of fibers to each other through the gelatinized binder. Furthermore, the water evaporates due to heat and the fiber density increases due to pressure, and accordingly, the plurality of fibers are bound to each other by hydrogen bonds. Accordingly, it is possible to form the sheet-like fiber body S having better mechanical strength. Further, since the fiber body S formed by evaporation of water has a weaker adhesive force than the web W before heating, it is possible to suppress the sticking of the fiber body S to the heating section 80.
The heating section 80 of the present embodiment has a pressurizing heating section 84 that pressurizes and heats the web W. The pressurizing heating section 84 can be configured by using, for example, a heating roller or a heat press molding machine. In the illustrated example, the pressurizing heating section 84 is a pair of heating rollers 86. The number of heating rollers 86 is not particularly limited. The pressurizing heating section 84 can simultaneously pressurize and heat the web W. Further, the configuration of the fiber body manufacturing apparatus 100 can be simplified.
As illustrated in
As a result, a single-cut fiber body S having a predetermined size is molded. The cut single-cut fiber body S is discharged to a discharge receiving section 96.
Next, a fiber body manufacturing method will be described.
In the present embodiment, a method for manufacturing the fiber body S in the fiber body manufacturing apparatus 100 will be described.
As illustrated in
Specifically, a mixture containing defibrated fibers and a binder (starch or dextrin) is accumulated by a dry method to form the web W. The fiber is a defibrated product defibrated by the defibration section 20, the binder is supplied from the binder supply section 52, and the mixture is formed by the mixing section 50. Then, the accumulating section 60 and the second web forming section 70 accumulate the mixture by a dry method to form the web W.
Next, in the transport step (step S12), the first surface Wa of the web W is peeled off from the first mesh belt 72, and the second surface Wb of the web W, which is a surface opposite to the first surface Wa peeled off from the first mesh belt 72, is brought into contact with the second mesh belt 78a that serves as a second transport belt to transport the web W.
Specifically, the suction mechanism 78c of the transport section 78 generates an upward airflow in the second mesh belt 78a to suction the web W. Accordingly, the first surface Wa of the web W is peeled off from the first mesh belt 72, and the web W is transported in a state where the second surface Wb is in contact with the second mesh belt 78a.
In the water-applying step (step S13), water is applied toward the first surface Wa of the web W which is in contact with the second mesh belt 78a. In other words, in the present embodiment, water is applied to the web W during the period in which the web W is being transported in the transport step.
Specifically, water is supplied from the water-applying section 79. In this step, as the water, water vapor or mist is applied to the web W. By doing so, it is possible to more uniformly apply water to the web W, and the fiber body S can be manufactured with a simpler apparatus configuration. In addition, the water applied to the web W does not contain starch or dextrin. The amount of water applied in the water-applying step can be managed by, for example, the water content of the web W. The water content of the web W to which water was applied in the water-applying step is preferably 12% by mass or more and 40% by mass or less. When the amount of water applied is approximately this level, it is possible to manufacture the fiber body S having higher strength while suppressing the amount of energy such as electric power required for heating and drying the web W.
Further, by applying water toward the first surface Wa of the web W, the second surface Wb side can be transported in a state where the adhesive force is weaker than that of the first surface Wa side. Therefore, it is possible to suppress the sticking of the web W, to which the water is applied, to the second mesh belt 78a.
Furthermore, by applying water to the web W formed by accumulating a material containing starch or dextrin, for example, as compared with a case where water containing starch or dextrin is applied to the web, the web W can be transported in a state where the binding force of the starch or the like is not sufficiently expressed, and the sticking of the web W to members such as the first mesh belt 72 and the second mesh belt 78a can be suppressed. In particular, when water is applied such that the water content of the web W is 12% by mass or more, this effect becomes even more remarkable.
Furthermore, by applying water toward the first surface Wa side of the web W which is in contact with the second mesh belt 78a, the second surface Wb side has a weaker adhesive force than the first surface Wa side, and thus it is possible to suppress the sticking of the web W, to which the water is applied, to the second mesh belt 78a.
Further, in the present embodiment, water is applied to the web W which is in contact with the second mesh belt 78a. Meanwhile, for example, when water is applied to the web W in a state of not being in contact with the second mesh belt 78a or the like, there is a concern that the web W is torn off as the amount of water contained in the web W increases. However, in the present embodiment, since water is applied to the web W in a state of being supported by the second mesh belt 78a, the tearing of the web W due to an increase in the amount of water contained in the web W can be suppressed.
Next, in the heating step (step S14), the heating section 80 (heating roller 86) is brought into contact with the web W peeled off from the second mesh belt 78a to heat the web W, and the fibers are bound to each other by starch or dextrin to form the fiber body S. In the heating step, the web W is simultaneously heated and pressurized. Accordingly, the manufacturing man-hours can be reduced.
Specifically, a pair of heating rollers 86 of the heating section 80 applies pressure to the web W to thin the web and increase the fiber density in the web W. The pressure applied to the web W is preferably 0.1 MPa or more and 15 MPa or less, more preferably 0.2 MPa or more and 10 MPa or less, and further preferably 0.4 MPa or more and 8 MPa or less. When the pressure applied to the web W in the heating step is within such a range, the deterioration of the fiber can be suppressed, and the fiber body S having good strength can be manufactured again using the defibrated product obtained by defibrating the manufactured fiber body S as a raw material.
Further, in the heating step, heat is applied to the web W to evaporate the water contained in the web W. In the heating step, the web W is heated so as to have a temperature of 60° C. or higher and 100° C. or lower. Accordingly, the binding force of starch or dextrin can be sufficiently expressed. Furthermore, the time required for the heating step can be reduced, and the fiber body S can be manufactured with lower energy.
Here, in the fiber body manufacturing method of the present embodiment, the web W peeled off from the second mesh belt 78a is directly supplied to the heating section 80 (heating roller 86). “Directly supplied” means that the web W peeled off from the second mesh belt 78a is supplied without coming into contact with other members. In other words, in the fiber body manufacturing method of the present embodiment, the web W peeled off from the second mesh belt 78a is not brought into contact with a member other than the heating section 80 (heating roller 86) before the heating step. In other words, the web W peeled off from the second mesh belt 78a is charged into the heating roller 86 without coming into contact with a member such as a transport roller or a guide.
Therefore, the web W to which water is applied becomes more adhesive, but by charging the web W peeled off from the second mesh belt 78a into the heating section 80 (heating roller 86) without touching anything, it is possible to prevent the web W from sticking to a member such as a transport member before heating.
Further, since the web W peeled off from the second mesh belt 78a is heated, it is possible to prevent the web W from sticking to the second mesh belt 78a during heating.
In addition, in the heating step, since a relatively low pressure is applied to the web W, a small manufacturing apparatus can be used, and since the damage to the fiber is relatively small, the fiber body S is defibrated again to make it easy to manufacture a new fiber body S.
Further, in the heating step, since the web W is heated to a relatively low temperature, it is easy to form hydrogen bonds between the fibers and it is easy to secure the strength of the fiber body S. Further, since the binder can be gelatinized, the fibers can be bound to each other by the binder, and the strength of the fiber body S can be obtained.
Next, a second embodiment will be described.
The same configurations as those in the first embodiment will be given the same reference numerals, and repeating description will be omitted.
In the water-applying step of the above-described first embodiment, the configuration that applies water to the web W which is in contact with the second mesh belt 78a is adopted, but the present disclosure is not limited thereto.
In the water-applying step in the present embodiment, water is applied to the web W which is in contact with the first mesh belt 72.
In this case, for example, the water-applying section 79 is arranged below the (accumulated) web W supported by the first mesh belt 72. Then, water is applied from below the web W toward the first surface Wa. Accordingly, water can be applied to the web W which is in contact with the first mesh belt 72.
Further, as illustrated in
Even in this manner, the web W can be transported in a state where the binding force of starch or the like is not sufficiently expressed, and by charging the web W peeled off from the second mesh belt 78a into the heating section 80 (heating roller 86) without touching anything, it is possible to prevent the web W from sticking to a member such as a transport member before heating.
Next, a third embodiment will be described.
The same configurations as those in the first embodiment will be given the same reference numerals, and repeating description will be omitted.
In the first and second embodiments, the configuration that applies water from below the web W which is in contact with the first mesh belt 72 or the second mesh belt 78a is adopted, but the present disclosure is not limited thereto.
For example, a configuration that applies water from above the web W which is in contact with the first mesh belt 72 or the second mesh belt 78a may be adopted.
In this case, for example, the opening of the container 79a of the water-applying section 79 is configured to face the second surface Wb side of the web W. Accordingly, water vapor or mist can be applied to the second surface Wb of the web W.
Even in this manner, the web W can be transported in a state where the binding force of starch or the like is not sufficiently expressed, and by charging the web W peeled off from the second mesh belt 78a into the heating section 80 (heating roller 86) without touching anything, it is possible to prevent the web W from sticking to a member such as a transport member before heating.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2021-106445 | Jun 2021 | JP | national |
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| 20150252530 | Higuchi et al. | Sep 2015 | A1 |
| 20200141059 | Inaba et al. | May 2020 | A1 |
| 20200385924 | Aoyama et al. | Dec 2020 | A1 |
| 20210206019 | Miyazawa et al. | Jul 2021 | A1 |
| Number | Date | Country |
|---|---|---|
| 3 418 435 | Dec 2018 | EP |
| 2015-168904 | Sep 2015 | JP |
| 2020-076168 | May 2020 | JP |
| Number | Date | Country | |
|---|---|---|---|
| 20220412012 A1 | Dec 2022 | US |
