JP2008105747A - Paper-made container and its manufacturing method - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a paper-made container which is evenly foamed, and has excellent heat-insulating properties. <P>SOLUTION: The paper-made container comprises a barrel member and a bottom member, wherein the barrel member comprises a paper substrate and a foamed thermoplastic resin layer formed thereon. The foamed thermoplastic resin layer is characterized in that it is obtained by forming a thermoplastic resin layer on at least one side of the paper substrate by extrusion laminating under so that the time required for the thermoplastic resin in a molten state extruded from a T-die to reach the paper substrate is 0.11-0.33 sec while the water content in the paper substrate is thermally evaporated to thereby allow the foaming of the thermoplastic resin layer. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

  The present invention relates to a paper container requiring heat insulation and a raw material sheet for the container. More specifically, a cup for filling hot coffee or the like used in vending machines, a so-called instant food container that makes it possible to eat and drink the contents by injecting hot water, and a microwave oven The present invention relates to a disposable container having heat insulation used for a cooking container or the like.

Insulated containers are generally used when fast drinks such as coffee or soup are provided to buyers in fast food stores such as hamburger shops, trains, vending machines, and instant ramen in cups. .
Conventionally, as a container used for such a use, what has the heat insulation property made from expanded polystyrene (EPS) is known. This is manufactured by adding a foaming agent to polystyrene, then casting this material into a mold, then applying heat and pressure to foam the raw material, and removing the molding container from the mold. The heat insulating container thus obtained is very excellent in terms of heat insulating properties. However, this container is bulky because the entire plastic is foamed, and the amount of dust increases. And, when incinerated as garbage after use, the incinerator is easily damaged because it emits high heat and it is required to be reviewed from the viewpoint of saving petroleum resources. In addition, there are concerns about adverse effects on the human body as environmental hormones. Furthermore, since the outer surface of expanded polystyrene has many minute irregularities, even if patterns, letters, symbols, etc. are printed on the outer surface, they are not clearly expressed. In addition, the thickness of the container is weaker than that of a paper cup, and in the case of a relatively large container such as instant noodles, the container may be broken during transportation.

On the other hand, in addition to the above-mentioned foamed plastic container, for example, Patent Document 1 (Japanese Patent Laid-Open No. 57-110439) discloses a paper container composed of a container body member and a bottom plate member on the outer wall surface of the container body member. A technique is described in which a low-melting thermoplastic synthetic resin film is laminated and heated to foam the film into irregularities using the vapor pressure of moisture contained in the paper that is the base material. At this time, it is described that the other surface of the paper is laminated with a thermoplastic synthetic resin film that becomes a similar foamed layer or coated with an aluminum foil as a layer for maintaining the vapor pressure during heating. This container has a comparatively good heat insulating property, and has advantages such as being inexpensive and easy to manufacture.
Similarly, as a technique for foaming by heating and evaporation of moisture contained in paper, Patent Document 2 (Patent No. 3596681) discloses a thermoplastic resin having a low melting point on one wall surface of the body member from the surface side of the paper. And a non-foamed outer layer of a thermoplastic resin having a higher melting point than that of the inner layer of the foamed inner layer. The interlayer strength between the foamed inner layer and the paper, the basis weight of the paper, the foamed layer and A paper container that defines the thickness of the non-foamed outer layer is described. Patent Document 2 also describes laminating a thermoplastic resin having a high melting point as a layer for maintaining the vapor pressure during heating on the other side of the paper.

JP-A-57-110439 Japanese Patent No. 3596681

The container described in Patent Document 1 or 2 uses paper as a base material, and the laminate layer (resin layer) is made of petroleum as a raw material, but its thickness is suppressed to the minimum necessary for heat insulation. For this reason, the use of fossil fuels is reduced as much as possible, and the environmental load is small compared with a container made entirely of expanded polystyrene, and the printability is excellent.
However, it is difficult to control because it is a mechanism that heats and evaporates the moisture contained in the paper substrate, and foams the thermoplastic resin layer with this evaporated moisture to give heat insulation. Problems such as occurrence, over-foaming, partial rupture or peeling of the thermoplastic resin layer from the paper substrate are likely to occur. If the foamed state is not uniform, sufficient heat insulation cannot be obtained.
Then, an object of this invention is to provide the paper-made container from which a uniform foaming state is obtained and excellent in heat insulation.

(1) The time until the molten thermoplastic resin comes into contact with the paper substrate from the T die on at least one side of the paper substrate of the body member raw material sheet in the paper container is 0.11 to 0.33 seconds. A raw material sheet for a trunk member of a paper container provided with a thermoplastic resin layer by extrusion lamination.
(2) A paper container comprising a barrel member and a bottom plate member, wherein the barrel member is formed with a foamed thermoplastic resin layer on the paper base material, and the foamed thermoplastic resin layer is made of a paper base material. At least one surface is provided with a thermoplastic resin layer obtained by extruding and laminating a thermoplastic resin in a molten state from 0.1 to 0.33 seconds until it comes into contact with the paper substrate from the T die, and moisture in the paper substrate A paper container, wherein the thermoplastic resin layer is foamed by evaporating and heating.
(3) The paper container according to (2), wherein the thermoplastic resin layer obtained by extrusion lamination has an ESCA analysis value of 0.4% to 1.5%.
(4) The paper container according to (2) or (3), wherein the extrusion-laminated thermoplastic resin layer is made of low-density polyethylene.
(5) It has a thermoplastic resin layer on both wall surfaces of the body member, and the thermoplastic resin layer on one wall surface is made of a thermoplastic resin having a higher melting point than the thermoplastic resin layer on the other wall surface. The paper container according to any one of (2) to (4).
(6) Among the thermoplastic resin layers provided on both wall surfaces of the trunk member, the melting point of the thermoplastic resin having a high melting point is 125 ° C. or higher, and is a thermoplastic resin layer on the inner wall surface side of the trunk member. The paper container according to any one of (2) to (5).
(7) The manufacturing method of the paper container which consists of a trunk | drum member and a baseplate member which has the process of following AC.
A. Laminate a thermoplastic resin layer on at least one side of the paper substrate by extruding and laminating the molten thermoplastic resin so that the time from the T-die to contact with the paper substrate is 0.11 to 0.33 seconds. Producing a body member raw material sheet,
B. Assembling the body member raw material sheet and the bottom member raw material sheet to form a paper container,
C. A step of heat-treating the molded paper container to evaporate moisture in the paper base of the body member to foam the thermoplastic resin layer.
(8) The paper container according to (4), wherein the low density polyethylene is MFR 10.0 to 14.0 g / 10 min.

1. A uniform foamed state can be obtained, and a paper container with good heat insulation can be provided.
2. Since a uniform foam layer is formed, clean printing can be performed.
3. It is a container mainly composed of paper that does not use expanded polystyrene, and is an environment-friendly container or a container that has little adverse effect on the human body, and can be treated as paper-based waste.

  The paper container of the present invention is roughly divided into A. B. Production of body member raw material sheet; Molding of paper containers, C.I. Manufactured from three processes: foaming by heat treatment. Hereinafter, although the present invention is explained based on a drawing, the present invention is not limited to these.

A. Manufacture of body material sheet (configuration of paper container)
FIG. 1 is a cross-sectional view of an example of a paper container according to the present invention. The paper container 1 of the present invention is basically composed of a body member 2 and a bottom plate member 3.
FIG. 2 is a partially enlarged cross-sectional view of the body portion indicated by Y in FIG. In this example, a thermoplastic resin layer 5 (hereinafter referred to as a foamed thermoplastic resin layer 5) foamed on the surface of the paper base 4 is present on the outer wall surface side (outside of the container) of the body member, and the foamed thermoplasticity The resin layer 5 has a structure in which foamed cells 6 are arranged. A thermoplastic resin layer 7 made of a thermoplastic resin having a melting point higher than that of the thermoplastic resin of the foamed thermoplastic resin layer 5 (hereinafter referred to as a non-foamed thermoplastic resin layer 7) is provided on the inner wall surface side (inner side of the container) of the trunk portion. Is present. As will be described later, the non-foamed thermoplastic resin layer 7 does not foam during the heat treatment in the container production, prevents the escape of evaporated water from the paper base material, and makes the foamed thermoplastic resin layer 5 reliable and sufficient. It is made to foam.

  Although not shown, the bottom plate member 3 is preferably a bottom plate member raw material sheet provided with at least one thermoplastic resin layer, aluminum foil, or the like on at least one side of a paper substrate. This is to prevent penetration of liquid or the like into the paper. The thermoplastic resin used for the bottom plate member may be the same as or different from that of the barrel member, and the lamination method is not only the extrusion lamination method, but also a film-like one such as a wet lamination method or a dry lamination method. The method to combine can be used suitably.

(Extruded laminate)
FIG. 3 shows a manufacturing process of a sheet that is a raw material of the body member 2. A thermoplastic resin layer 5 ′ is extruded from a T die 9 in the form of a molten resin film onto one surface of the paper substrate 4 fed out from the winding 8, and cooled between the cooling roll 10 and the nip roll 11 facing the same. The body member raw material sheet 12 is obtained by pressure bonding. Here, the distance until the molten resin in the molten film extruded from the T-die contacts the paper substrate is called an air gap. In extrusion lamination, the operating conditions such as the melting temperature of the resin and the laminating speed may be appropriately set depending on the type of resin used and the apparatus, but generally the melting temperature is about 200 to 350 ° C. and the laminating speed is 50, for example. It is about ~ 200 m / min. In addition, in order to improve the adhesiveness of a paper base material or a thermoplastic resin, you may perform a corona treatment, an ozone treatment, etc. as needed. Further, it is preferable to use a nip roll having a hardness of 70 degrees or more (JIS K-6253) and pressing and pressure bonding with a linear pressure of 15 kgf / cm or more.

  Although not shown, a non-foamed thermoplastic resin layer 7 is laminated on the opposite surface of the body member raw material sheet 12 on which the thermoplastic resin layer 5 'is provided. The non-foamed thermoplastic resin layer 7 is thermoplastic. Before or simultaneously with or after the lamination of the resin layer 5 ′, the resin layer 5 ′ is laminated by a method of pasting with a film-like one such as extrusion lamination, wet lamination method, dry lamination method or the like.

In the present invention, it is important that the time required for the molten thermoplastic resin to pass through the air gap is 0.11 to 0.33 seconds. By being in the time range specified in the present invention, a uniform foamed state can be obtained when heat treatment is performed. The reason for this is not clear, but is presumed as follows.
Usually, in the extrusion laminating method, the higher the temperature of the molten thermoplastic resin, the higher the adhesiveness with the paper substrate, so the passage time of the air gap is set short. Usually, there is an example in which the air gap is 130 mm and the stacking speed is about 130 to 100 m / min (see, for example, Japanese Patent Laid-Open No. 2006-168775, Japanese Patent No. 3586868). This corresponds to 0.06 to 0.078 seconds in terms of transit time.
On the other hand, the present invention has been found that the time during which the thermoplastic resin passes through the air gap affects the foaming property. In the present invention, the thermoplastic resin is appropriately oxidized, so that the resin surface Is hard and easily stretched in the vertical direction, and it is considered that a good foamed state can be obtained. When the passage time of the air gap is shorter than 0.11 seconds, the foamed cell extends in the lateral direction instead of vertically because the foamed cell becomes soft when the foamed and foamed thermoplastic resin layer is insufficient. A uniform foamed state cannot be obtained, such as excessive foaming, a foamed cell wall is thin and weak and easily ruptured, and peeling between layers of the foamed cells occurs. On the other hand, when it is longer than 0.33 seconds, the adhesiveness with the paper base material is lowered, and the thermoplastic resin layer is pushed up by the evaporated water from the paper base material to cause peeling, thereby improving the adhesiveness with the paper base material. If it is inferior, it is easy to over foam. A more preferable passage time of the air gap is 0.15 seconds or more, 0.30 seconds or less, more preferably 0.25 seconds or less. The degree of oxidation is preferably 0.4 to 1.5% by ESCA analysis.

(Paper substrate)
The paper used in the present invention refers to a plant fiber or a product produced by tangling and sticking plant fibers and other fibers, and the raw material for plant fibers is wood fibers such as conifers or hardwoods, Mitsumata, Kozo, etc. Bast fibers, bagasse, kenaf, hemp and other non-wood fibers, cotton fibers, waste paper, etc., and the types of paper include fine paper, coated paper, recycled paper, etc., but are not limited thereto It is not a thing. The basis weight of the paper is preferably about 100 g / m ² or more and about 400 g / m ² or less. If the basis weight is too low, the water content necessary for foaming is low, or the foam is not sufficiently foamed. It is easy to feel the heat when you hold it with your hand. Preferably it is 200 g / m ² or more, more preferably 250 g / m ² or more. On the other hand, if the basis weight is too high, it is uneconomical because it exceeds the desired rigidity as a body member, and foaming or molding processability is reduced more than necessary. Further, the water content in the paper substrate is preferably 5 to 15% by weight because if it is too much, the rigidity is lowered and the moldability of the container is inferior, and overfoaming or rupture of the foamed cell is caused. 6 to 10% by weight is more preferable.

(Foamed thermoplastic resin layer)
The thermoplastic resin used as the foamed thermoplastic resin layer is not particularly limited as long as extrusion lamination is possible and foaming is possible, and either a crystalline resin or an amorphous resin can be used. Examples of crystalline resins include polyolefin resins such as high density polyethylene, medium density polyethylene, low density polyethylene, linear low density polyethylene, polypropylene, polymethylpentene, polyester resins, polyamides, polyacetals, PPS resins, etc. Can do. Examples of the amorphous resin include polystyrene, polyvinyl chloride, ABS resin, acrylic resin, modified PPE, polycarbonate, polyurethane, polyvinyl acetate, and amorphous polyethylene terephthalate (PET). These thermoplastic resins may be a single resin or a plurality of resins, but are preferably a single layer from the viewpoint of foamability.
The melting point of the thermoplastic resin is preferably about 80 to 120 ° C. In the present invention, polyethylene is preferred because of excellent laminating ability and foamability. Polyethylene is roughly classified into linear low density polyethylene, low density polyethylene, medium density polyethylene, and high density polyethylene. The density, linear low density polyethylene 888~910kg / ^{m 3,} low density polyethylene 910~925kg / ^{m 3,} medium density polyethylene 925~940kg / ^{m 3,} higher density polyethylene has 940~970kg / m ^{About three} . As the melting point, linear low density polyethylene is 55 ° C to 120 ° C, low density polyethylene is 105 ° C to 120 ° C, medium density polyethylene is 120 ° C to 125 ° C, and high density polyethylene is about 125 ° C to 135 ° C. When low density polyethylene is used as the thermoplastic resin, the melting temperature during extrusion lamination is 315 ° C. or higher, preferably 330 ° C. or higher. In a normal case, the temperature is about 300 ° C., but since the time passing through the air gap is longer than usual, the high temperature is set in consideration thereof.
In addition, when using a low density polyethylene as a thermoplastic resin, it is preferable that MFR is 10.0-14.0 g / 10min. MFR is an index of resin fluidity, and MFR low density polyethylene in this range is used under the conditions of the present invention in which the time required for the molten thermoplastic resin to pass through the air gap is 0.11 to 0.33 seconds. By doing so, the foamability is improved.

(Non-foamed thermoplastic resin layer)
In the present invention, in order to increase the foaming efficiency, the opposite wall surface side of the wall surface having the foamed thermoplastic resin layer of the body member is made of a thermoplastic resin having a melting point higher than that of the foamed thermoplastic resin layer and foamed when heat-treated. It is preferable to cover with an unheated thermoplastic resin layer (non-foamed thermoplastic resin layer) or an aluminum foil. If one side of the paper base is left ground, the moisture in the paper will evaporate from the uncoated surface into the atmosphere during the heat treatment, making it difficult to ensure sufficient foaming. Therefore, by providing such a coating layer, moisture in the paper can be efficiently contributed to foaming. It should be noted that these non-foamed thermoplastic resin layers, aluminum foils, and the like are preferably present on the inner wall surface side of the body member, so that the filling liquid or the like can be prevented from penetrating into the paper.
Similarly, a non-foamed thermoplastic resin layer can be provided on the foamed thermoplastic resin layer for the purpose of increasing the foaming efficiency. When the foamed thermoplastic resin layer is present on the outer wall surface of the body member, the surface is uneven and not smooth, so that the presence of the non-foamed thermoplastic resin layer provides a smooth hand and glossy appearance. And the waterproofness of the container is further improved.
The thermoplastic resin of these non-foamed thermoplastic resin layers may be the same as or different from the foamed thermoplastic resin layer. In the case of the same, a difference in the melting point can be caused by making a difference in density. For example, when polyethylene is selected as both thermoplastic resins, the foamed thermoplastic resin layer is low density polyethylene and the non-foamed thermoplastic resin layer is medium density or high density polyethylene. The difference in melting point between the thermoplastic resin layers of the foamed thermoplastic resin layer and the non-foamed thermoplastic resin layer is preferably 5 ° C. or more. The melting point of the thermoplastic resin of the non-foamed thermoplastic resin layer is a melting point during heating. There is no particular limitation as long as the diffusion of evaporated water can be suppressed, but 125 ° C. or higher is preferable.

  The method for forming the non-foamed thermoplastic resin layer is not particularly limited, and it may be laminated by extrusion lamination on the opposite side of the foamed thermoplastic resin layer of the paper substrate or on the foamed thermoplastic resin layer, or wet lamination. A method of laminating with a film-like one such as a method or a dry laminating method can be appropriately used. In addition, when a non-foamed thermoplastic resin layer is provided on the foamed thermoplastic resin layer, or when the foamed thermoplastic resin layer is formed of a plurality of thermoplastic resin layers, etc. From the viewpoint of adhesion between thermoplastic resin layers and production efficiency, it is suitable to use a plurality of extruders to guide each thermoplastic resin in a molten state to each T-die and simultaneously extrude from each T-die for lamination bonding. ing. Such a method capable of simultaneously forming two or more thermoplastic resin layers is called a co-extrusion laminating method among the extrusion laminating methods. Further, an adhesive resin layer may be sandwiched between the thermoplastic resin layers to improve the adhesion between the resin layers. In any case, corona treatment, ozone treatment, or the like may be performed to improve the adhesion of the paper base material or the thermoplastic resin as necessary.

(Other)
Regarding the thickness of each thermoplastic resin layer of the foamed thermoplastic resin layer and the non-foamed thermoplastic resin layer, the foamed thermoplastic resin layer should be thick enough to provide the desired heat insulation when foamed. Although it is not particularly limited, the thickness before foaming is about 40 to 80 μm, and after foaming is about 400 to 2000 μm. In addition, the non-foamed thermoplastic resin layer is also thick enough to prevent scattering of evaporated water, and if it is on the inner wall surface side of the body member, the thickness can ensure liquid penetration resistance. It is not specifically limited, It is about 20-50 micrometers.
Further, the outer wall surface side and the inner wall surface side of the body member may have the same laminated structure or may be different. The type of resin used and other materials may be the same or different.

  Moreover, various additives generally used in the range which does not inhibit a desired effect can be added to each thermoplastic resin layer of a foamed thermoplastic resin layer and a non-foamed thermoplastic resin layer. Examples of these additives include antistatic agents, white pigments (inorganic pigments such as titanium oxide, calcium carbonate, clay, talc, and silica), anti-blocking agents (acrylic beads, glass beads, silica, and the like), and ultraviolet absorption. There are agents.

B. In the present invention, the body member raw material sheet 12 and the bottom plate member raw material sheet are formed by a conventional cup manufacturing apparatus or cup molding machine. First, the body member raw material sheet 12 is fed out from the take-up roll, and necessary printing is performed at a predetermined location. At this stage, barcodes can be printed. The positioning of the printed part can be performed by conventional means or procedures.
Next, a blank for a trunk member and a blank for a bottom plate member are punched out from each raw material sheet, and assembled into a container shape by a conventional cup molding machine. Here, the foamed thermoplastic resin layer 5 may be present on one or both of the outer wall surface side and the inner wall surface side of the body member, and may be appropriately determined as desired, such as heat insulating properties, touch, and appearance aesthetics. However, when the inside of the container has a foamed surface, the foamed resin may be damaged by chopsticks, forks or the like during food and drink and enter the mouth. Therefore, for example, the bottom plate member is assembled so that the thermoplastic resin layer 5 'of the body member raw sheet 12 faces the outside of the container, and the bottom plate member faces the inside of the container.

C. Foaming by heat treatment The paper container after molding is subjected to heat treatment for foaming. In the present invention, due to the heat treatment, moisture contained in the paper base material 4 of the body member 2 is evaporated, and the thermoplastic resin layer 5 ′ is foamed to become the foamed thermoplastic resin layer 5.
The heating temperature and heating time vary depending on the type of paper substrate and thermoplastic resin to be used, and the optimum combination of heating temperature and heating time for the thermoplastic resin to be used can be appropriately determined. A temperature slightly higher than the melting point of the foaming thermoplastic resin (melting point +5 to 10 ° C.) is suitable, and generally the heating temperature is about 110 ° C. to about 200 ° C., and the heating time is about 1 minute to 6 minutes. . The heating means is not particularly limited, and any means such as hot air, electric heat, or electron beam can be used. If it is heated by hot air or electric heat in a tunnel equipped with a conveyor means, mass production can be performed at low cost.

Others.
In the present invention, a technique known in the field of paper containers can be applied as necessary within a range that does not impair the desired effect. For example, a technique for applying a paint containing 5 wt% to 40 wt% of a synthetic resin component on a part of a body member serving as an outer wall surface to partially suppress foaming (Japanese Patent No. 3014629), a body member serving as an outer wall surface A technique for applying a synchronized ink that forms a smooth printing surface in synchronization with foaming on the surface of the container (Japanese Patent No. 3408156), and a technique for providing a flange portion at the upper edge of the opening of the container body member, A technique (for example, Japanese Patent Application Laid-Open No. 2001-354226) and the like in which a forcible processing is performed and the inner winding end is superposed on the upper portion of the flange portion to form a double structure may be mentioned, but is not limited thereto. Moreover, in order to improve printability, you may provide the ink receiving layer which has a pigment and a binder as a main component in the outermost layer used as the outer wall surface of a trunk | drum member.

As described above, the present invention heats a paper provided with a thermoplastic resin layer, evaporates moisture contained in the paper, encloses bubbles of water vapor in the molten thermoplastic resin layer, and forms a foam layer. The technology to form the is used. If the molten state of the thermoplastic resin layer has a low viscosity, there is a risk that steam will escape and pinholes will be generated, or small bubbles will bond and become larger and torn.
On the other hand, the present invention forms the resin layer surface in a skin shape by advancing the oxidation of the resin, which is considered to be adversely affected by normal lamination, by increasing the time to pass through the air gap. The foam is retained in the resin layer, the small foam state is maintained, and the occurrence of pinholes and the like is prevented. Moreover, after extruding from a T-die, extrusion is performed at a higher temperature than usual in order to ensure the adhesive force that the thermoplastic resin contacts and adheres to the paper substrate. Moreover, this high temperature is considered to fulfill the function of promoting oxidation.
The present invention evaporates the moisture contained in the paper and confines it in a thin molten thermoplastic resin layer to form a large number of small bubbles to exert heat insulation, but its control is difficult and good It has been difficult to form a heat insulating layer in such a state, and it has been found that control can be performed by increasing the time required to pass through the air gap during lamination.
Furthermore, a resin layer having a high melting temperature is provided on the opposite surface of the paper base material to prevent vapor escape when moisture contained in the paper base material is vaporized, and the low temperature molten thermoplastic resin layer is vaporized. It is intended to increase the accuracy of securing the.

  Hereinafter, the effects of the present invention will be described in detail by way of examples.

[Example 1]
On one side of a base paper having a basis weight of 300 g / m ² (water content 8%), as a foamed thermoplastic resin layer that becomes the outer wall surface of the body member when used as a paper container, a melting point of 108 ° C. and MFR of 13.8 g / 10 min Low density polyethylene (LDPE) is extruded at a melting temperature of 340 ° C. to a thickness of 70 μm, and this molten resin and base paper are pressed and pressure-bonded at a linear pressure of 15 kgf / cm using a cooling roll and a nip roll having a hardness of 70 degrees. did. At this time, the time required for the molten resin discharged from the T die to contact the base paper (air gap passage time) was set to 0.112 seconds. Further, on the opposite side of the base paper, as a non-foamed thermoplastic resin layer serving as the inner wall surface of the body member, medium density polyethylene (medium density PE) having a melting point of 128 ° C. and MFR 6.5 g / 10 min is set to a thickness of 40 μm. And extruded and laminated at a melting temperature of 320 ° C. to obtain a barrel member raw material sheet.

[Example 2]
A body member raw material sheet was obtained in the same manner as in Example 1 except that the time until the molten resin discharged from the T-die contacted the base paper was 0.186 seconds.

[Example 3]
A body member raw material sheet was obtained in the same manner as in Example 1 except that the time until the molten resin discharged from the T-die contacted the base paper was 0.223 seconds.

[Example 4]
A body member raw material sheet was obtained in the same manner as in Example 1 except that the base paper having a basis weight of 300 g / m ² was changed to a base paper having a basis weight of 320 g / m ² (water content 8%).

[Example 5]
The same as in Example 1 except that the non-foamed thermoplastic resin layer that becomes the inner wall surface of the body member is changed to polypropylene (PP) having a melting point of 165 ° C. instead of medium density polyethylene (medium density PE) having a melting point of 128 ° C. Thus, a body member raw material sheet was obtained.

[Example 6]
A body member raw material sheet was obtained in the same manner as in Example 1 except that low density polyethylene (LDPE) having a melting point of 108 ° C. was laminated so as to have a thickness of 50 μm.

[Example 7]
The body member raw material sheet obtained in Example 1 was heated at 123 ° C. for 4 minutes to obtain a foam sample piece.

[Example 8]
As the foamed thermoplastic resin layer, a melting point of 108 ° C., MFR of 13.8 g / 10 minutes instead of low density polyethylene (LDPE), a melting point of 108 ° C., MFR of 13.8 g / 10 minutes of low density polyethylene (LDPE) of 88.5% by weight, Except for changing to a mixed resin (melting point 108 ° C., MFR 13.0 g / 10 min) consisting of 11.5% by weight of low density polyethylene (LDPE) with a melting point 107 ° C. and MFR 8.2 g / 10 min, the same as in Example 1. Thus, a body member raw material sheet was obtained.

In addition, MFR of mixed resin was calculated | required with the following formula.

logX = alogY + blogZ
(A, b: mixing ratio of each resin, X: MFR of mixed resin, Y, Z: MFR of each resin)

[Example 9]
As the foamed thermoplastic resin layer, a melting point of 108 ° C. and a low density polyethylene (LDPE) with a melting point of 108 ° C. and an MFR of 13.8 g / 10 minutes are replaced with 90.0% by weight of a low density polyethylene (LDPE) with a melting point of 108 ° C. and an MFR of 13.8 g / 10 minutes. Except for changing to a mixed resin (melting point: 108 ° C., MFR: 13.0 g / 10 min) consisting of 10.0% by weight of low density polyethylene (LDPE) with a melting point of 108 ° C. and MFR: 7.5 g / 10 min. Thus, a body member raw material sheet was obtained.

[Example 10]
As the foamed thermoplastic resin layer, a melting point of 108 ° C., MFR of 13.8 g / 10 minutes instead of low density polyethylene (LDPE), a melting point of 108 ° C., MFR of 13.8 g / 10 minutes of low density polyethylene (LDPE) of 20.0% by weight, Except for changing to a mixed resin (melting point 106 ° C., MFR 20.0 g / 10 min) consisting of 80.0% by weight of low density polyethylene (LDPE) with a melting point 106 ° C. and MFR 22.0 g / 10 min, the same as in Example 1. Thus, a body member raw material sheet was obtained.

[Example 11]
As the foamed thermoplastic resin layer, a melting point of 108 ° C., MFR of 13.8 g / 10 minutes instead of low density polyethylene (LDPE), a melting point of 108 ° C., MFR of 13.8 g / 10 minutes of low density polyethylene (LDPE) of 77.0% by weight, Except for changing to a mixed resin (melting point 108 ° C., MFR 12.0 g / 10 min) consisting of 23.0% by weight of low density polyethylene (LDPE) with a melting point 108 ° C. and MFR 7.5 g / 10 min, the same as in Example 1. Thus, a body member raw material sheet was obtained.

[Comparative Example 1]
A body member raw material sheet was obtained in the same manner as in Example 1 except that the time until the molten resin discharged from the T-die contacted the base paper was 0.335 seconds.

[Comparative Example 2]
A body member raw material sheet was obtained in the same manner as in Example 1 except that the time until the molten resin discharged from the T-die contacted the base paper was 0.098 seconds.
Table 1 shows the results of the following evaluation tests using the body member raw material sheets obtained in the above Examples and Comparative Examples. In addition, the case where it was not made to foam using the trunk | drum member raw material sheet | seat obtained in Example 1 was made into the reference example 1. FIG.

<Oxidation degree>
About the foamed thermoplastic resin layer of the body member raw material sheet before foaming, the degree of oxidation was measured by ESCA analysis. A smaller value indicates a lower degree of oxidation.
ESCA is an abbreviation for electron spectroscopy for analysis. X-ray irradiation is performed, the energy of photoelectrons from atoms excited by X-rays is measured, the energy specific to the atoms is analyzed, and the constituent elements are identified.
In the present invention, the polyethylene layer forming the surface layer is irradiated with X-rays, and the degree of oxidation is determined by the ratio of C and O ₂ . Usually, polyethylene contains only CH bonds and thus does not contain O ₂ (note that H is too low in energy and cannot be measured by X-ray analysis).
For measurement, a 5 mm square sample is cut and the surface layer is irradiated with X-rays. Although the irradiated X-rays reach the paper base paper, the photoelectrons excited from the base paper are absorbed and dispersed in the middle, so the energy of the surface layer number of μm is actually measured.

<Foaming (thickness)>
The total thickness of the body member raw material sheet before foaming was measured. Next, the sample piece (10 cm × 10 cm) was placed in a dryer at 115 ° C. or 123 ° C. and heated for 4 minutes to foam the foamed thermoplastic resin layer, thereby obtaining a foam sample piece. The total thickness after foaming was measured.

<Foaming (state)>
About said foam sample piece, the foaming state was visually evaluated on the following reference | standard.
A: Uniform and fine foamed state, good.
〇… There is no problem as a heat-insulating container although it is partially over-foamed.
Δ: Although it is slightly over-foamed, it can be used as a heat insulating container.
X: Overexpanded or insufficiently foamed and cannot be used as a heat insulating container.

<Adhesion with paper substrate>
The sample piece (10 cm × 10 cm) of the body member raw material sheet before foaming was manually peeled between the base paper and the low-density polyethylene layer, and the degree of ease of peeling at that time was evaluated according to the following criteria.
A: It is firmly attached and cannot be peeled off.
〇… Strongly attached and difficult to peel off.
Δ: There is resistance but peeling is possible.
X: Adhesion is weak or can be easily peeled off.

<Insulation>
Combining the body member raw material sheet with the bottom plate member raw material sheet (obtained by extruding and laminating medium density polyethylene to a base weight of 220 g / m ² to a thickness of 40 μm) to form a container having a diameter of 95 mm and a height of 115 mm And heated for 4 minutes in a dryer at 115 ° C. to cause foaming. Thereafter, 90 ° C. hot water was put into the foamed container, and after 3 minutes, the outer wall surface of the container was touched by hand and evaluated according to the following criteria.
A: It is not very hot, can hold the container sufficiently by hand, and has excellent heat insulation.
〇… Slightly hot, but the container can be held by hand and has good heat insulation.
Δ: It is hot, it is difficult to hold the container sufficiently by hand, and heat insulation is slightly good.
X: It is quite hot, it is difficult to hold the container by hand, and the heat insulation is poor.

  From this result, the air gap passing time is suitably in the range of 0.11 to 0.33 seconds, preferably 0.15 to 0.25 seconds. The degree of oxidation is preferably 0.4 to 1.5%, particularly preferably 1.0% or less.

It is sectional drawing of an example of the paper containers by this invention. It is the elements on larger scale of the trunk | drum shown by Y in FIG. It is explanatory drawing which shows the manufacturing method by extrusion lamination. It is an optical microscope photograph (magnification 150) of the cross section of the container trunk | body member shape | molded and foamed by the heat insulation test using the trunk | shell member raw material sheet | seat obtained in Example 1. FIG. The thickness of the foamed thermoplastic resin layer is about 700 μm. It is an optical microscope photograph (magnification 150) of the cross section of the container trunk | drum member shape | molded and foamed by the heat insulation test using the trunk | drum member raw material sheet | seat obtained in the comparative example 1. FIG.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Paper container 2 Body member 3 Bottom plate member 4 Paper base material 5 Foamed thermoplastic resin layer 5 'thermoplastic resin layer 6 Foamed cell 7 Non-foamed thermoplastic resin layer 8 Winding 9 T die 10 Cooling roll 11 Nip roll 12 Body member Raw material sheet 13 Air gap

Claims (8)

  Extrusion laminating at least one side of the paper base of the body member raw material sheet in the paper container so that the molten thermoplastic resin contacts the paper base from the T die between 0.11 and 0.33 seconds A raw material sheet for a trunk member of a paper container provided with a thermoplastic resin layer. A paper container comprising a body member and a bottom plate member,
The body member has a foamed thermoplastic resin layer formed on a paper base material,
The foamed thermoplastic resin layer is formed by extruding and laminating a thermoplastic resin in a molten state on at least one surface of a paper base material so that the time from the T die to contact with the paper base material is 0.11 to 0.33 seconds. A paper container, wherein a thermoplastic resin layer is provided and the thermoplastic resin layer is foamed by heating and evaporating moisture in the paper substrate.   The paper container according to claim 2, wherein the extrusion-laminated thermoplastic resin layer has a resin oxidation degree of 0.4% to 1.5% by ESCA analysis.   4. The paper container according to claim 2, wherein the extruded laminated thermoplastic resin layer is made of low density polyethylene.   A thermoplastic resin layer is provided on both wall surfaces of the body member, and the thermoplastic resin layer on one wall surface is made of a thermoplastic resin having a melting point higher than that of the thermoplastic resin layer on the other wall surface. Paper container in any one of 2-4.   Among the thermoplastic resin layers provided on both wall surfaces of the trunk member, the melting point of the thermoplastic resin having a high melting point is 125 ° C. or higher, and is a thermoplastic resin layer on the inner wall surface side of the trunk member. The paper container according to any one of claims 2 to 5. The manufacturing method of the paper container which consists of a trunk | drum member and a baseplate member which has the process of following AC.
A. Laminate a thermoplastic resin layer on at least one side of the paper substrate by extruding and laminating the molten thermoplastic resin so that the time from the T-die to contact with the paper substrate is 0.11 to 0.33 seconds. Producing a body member raw material sheet,
B. Assembling the body member raw material sheet and the bottom member raw material sheet to form a paper container,
C. A step of heat-treating the molded paper container to evaporate moisture in the paper base of the body member to foam the thermoplastic resin layer.   5. The paper container according to claim 4, wherein the low density polyethylene has an MFR of 10.0 to 14.0 g / 10 min.